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REQUEST FOR PROPOSAL RFP2020-02 Engineering Services for Energy Reduction Upgrades Lunenburg County Lifestyle Centre Important Notes for Bidding: Issued: September 4 th , 2020 Closing: September 29 th , 2020

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Page 1: Engineering Services for Energy Reduction Upgrades · 2020. 9. 4. · RFP2020-02 Engineering Services for Energy Reduction SEPTEMBER 2020 3 1.0 INTRODUCTION 1.1 OVERVIEW As part of

REQUEST FOR PROPOSAL

RFP2020-02

Engineering Services for Energy Reduction Upgrades

Lunenburg County Lifestyle Centre

Important Notes for Bidding:

Issued: September 4th, 2020

Closing: September 29th, 2020

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Table of Contents

Contents 1.0 INTRODUCTION .......................................................................................................................... 3

1.1 OVERVIEW................................................................................................................................................. 3 1.2 BACKGROUND .......................................................................................................................................... 3 1.3 OBJECTIVES ............................................................................................................................................. 4 1.4 PROJECT SCHEDULE .............................................................................................................................. 5 1.5 INQUIRIES.................................................................................................................................................. 5

2.0 SERVICE REQUIREMENTS ........................................................................................................ 5 2.1 PROJECT SCOPE ..................................................................................................................................... 5 2.2 PROJECT MANAGEMENT ...................................................................................................................... 10 2.3 COMMISIONING ...................................................................................................................................... 10 2.4 SCHEDULE OF EVENTS ......................................................................................................................... 10 2.5 DELIVERABLES/MILESTONES............................................................................................................... 11

3.0 ADMINISTRATIVE & LEGAL REQUIREMENTS ....................................................................... 14 3.1 PROPOSER DECLARES ......................................................................................................................... 14 3.2 PROPOSER AGREES ............................................................................................................................. 14 3.3 COMMERICAL LIABILITY & AUTOMOBILE INSURANCE...................................................................... 15 3.4 INDEMNITY .............................................................................................................................................. 16 3.5 LIABILITY OF ERRORS ........................................................................................................................... 16 3.6 BILLING and PAYMENT ........................................................................................................................... 16 3.7 CONTRACT AGREEMENT ...................................................................................................................... 17 3.8 TERMINATION ......................................................................................................................................... 17 3.9 CONFIDENTIALITY NOTICE ................................................................................................................... 17

4.0 OTHER IMPORTANT PROVISIONS .......................................................................................... 17 4.1 ADDENDA AND ADDENDA ACKNOWLEDGEMENT ............................................................................. 17 4.2 PUBLIC OPENING ................................................................................................................................... 18 4.3 CONSTRAINTS ........................................................................................................................................ 18 4.4 CONFLICT OF INTEREST ....................................................................................................................... 18

5.0 SUBMISSION INFORMATION ................................................................................................... 18 5.1 SUBMISSION FORMAT ........................................................................................................................... 18 5.2 SUBMISSION INFORMATION ................................................................................................................. 20

6.0 PROPOSAL EVALUATION CRITERIA ...................................................................................... 21

7.0 SIGNATURE .............................................................................................................................. 22

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1.0 INTRODUCTION

1.1 OVERVIEW As part of a larger commitment to the reduction of operating costs, as well as greenhouse gas emissions, the Lunenburg County Lifestyle Centre (LCLC) commissioned a Detailed Energy Audit in July of 2020. (Appendix A). We are now soliciting proposals for Design, Tender and Project Management services to implement the recommendations resulting from the Detailed Energy Audit.

The LCLC views the scope of work detailed in this document as Phase One. Phase Two will be the addition of an integrated dehumidification solution for the arena. We are not seeking proposals for dehumidification at this time however we will want to understand how modifications in the current Phase of the project will lend themselves to the dehumidification solutions in Phase Two.

The LCLC has worked with Efficiency Nova Scotia (ENS) to secure an incentive funding estimate based on the calculated energy savings through implementation of measures detailed throughout this document. The successful proponent will be required to meet ENS Custom Program requirements in the Measurement and Verification (M&V) in order to ensure that the realized savings match the projected savings.

1.2 BACKGROUND

The LCLC is a multi-purpose facility opened in 2013. The sport, recreation, and community facility houses an NHL-size arena (Clearwater Seafoods Arena) with a capacity to seat 1,200 spectators; an aquatic centre (BMO Financial Group Aquatic Centre) suited to both leisure and competitive users; a therapeutic pool; and a public library. Other multi-purpose spaces include administrative offices, community and cultural spaces, and areas capable of hosting meeting, exercise classes, senior citizens’ activities, and many other functions.

The exterior of the building consists of metal cladding walls with a built-up roof. Estimated insulation values of R-12 and R-25 have been attributed to the walls and roof respectively. The windows are aluminum frame double pane glass type with an estimated insulation value of R-2.5.

Mechanical Systems

A number of circulating loops provide heating and cooling for the facility. The facility is mainly heated by one (1) low-grade heating loop (at 105°F) and one (1) medium-grade heating loop (at 135°F). There is a rink cooling loop (20°F) and a chilled water loop (45°C) serving the ice rink and air handling unit cooling loads respectively, and a geothermal field water loop provided heat source and sink to the facility as required throughout the year. There is also a heat recovery loop which can be open to any of the above-mentioned loops (low-grade loop, medium-grade loop, chilled water loop, geothermal field loop, and ice rink cooling loop) used to share energy within the facility.

The low-grade heating loop operates at 105°F and is supplied by the heat rejection of the ice plant and serves the in-floor heating and all the air handling unit heating coils except for the pool AHU-3. If the heat rejected by the ice plant is greater than the demand for AHU heating and in-floor heating, the excess heat from the low-grade loop is rejected first to the heat recovery loop and as second stage to a cooling tower. If additional heat is required for the

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low-grade loop when the ice rink is satisfied, the ice plant can operate to transfer heat from the heat recovery loop to the low-grade loop. Due to the intermittent operation of the ice plant, the low-grade loop constantly switches from having to reject heat to the heat recovery loop and to the cooling tower and from requiring additional heat from the heat recovery loop. The lack of water volume storage for the low-grade loop prevents the ice plant and the low-grade loop from operating in unison based on steady load demand.

The medium-grade heating loop operates at 135°F and is heated by the condenser heat rejection of a Multistack chiller which simultaneously provides cooling to the chilled water loop which operates at 45°C. The Multistack chiller operates between a chilled water buffer tank and a medium-grade buffer tank. The medium-grade heating loop provides heating for the pool water heating (all three pools), the perimeter radiator heaters, the pool AHU-3 heating coil and also provides domestic hot water preheat for the Zamboni water and main domestic hot water systems. The Multistack operate to maintain the loop requiring the most demand between the chilled water and medium-grade loops. If excess heat is supplied to the medium-grade loop, the excess heat is rejected to the heat recovery loop and if additional heat is required for the chilled water loop, additional heat is provided by the heat recovery loop. An electric boiler is connected to the medium-grade heating loop for supplemental and backup heating capability, but according to the operational staff, the electric boiler does not require to operate often.

There is also a heat pump loop which connect directly to the heat recovery loop and supplies a number of distributed heat pumps that provide heating and cooling for the library and office areas of the facility. A geothermal field water loop is directly connected to the heat recovery loop and provides heat addition and rejection capability for the loop depending on the heating/cooling equilibrium of the facility. It was found that the geothermal loop operates almost continuously during the year and that the geothermal loop temperature is relatively high throughout the year suggesting that overall there is a yearly surplus of heat from the facility that continuously rejects to the geothermal field. As all the loops are openly interconnected via the heat recovery loop, all circulating loops utilize 40% ethylene glycol as a fluid medium. 40% ethylene glycol is required for freeze protection of the ice rink cooling loop and for the air handling units heating coils. The ice plant consists of a packaged CIMCO plant utilizing three (3) 40 ton capacity screw type compressors. The ice rink is controlled by an infra-red temperature sensor and the rink slab pump cycles as required to provide cooling for the ice pad. Zamboni uses 160°F hot water and requires on average 100 gallon of water per flood. The rink humidity is controlled by four (4) desiccant electric dehumidifiers.

The pool area is ventilated, dehumidified and heated by a mixed air rooftop unit (AHU-3). The AHU-3 has DX cooling to provide dehumidification and the excess heat from the dehumidification is used to heat the pools. Each pool has a filter pump that operates continuously to provide water filtration and chemical treatment. A rooftop solar water heater provides preheating for the lap pool. Ventilation for the rest of the facility (other than the pool area) is provided by five (5) rooftop air handling units. AHU-1 is a mixed air unit providing heating and cooling to the lobby area of the building, AHU-2 is a 100% outside air unit with heat recovery providing ventilation to the pool change rooms, AHU-3 serves the pool as described above, AHU-4 and AHU-5 are 100% outside air units with heat recovery providing ventilation to the ice rink and rink changing rooms.

1.3 OBJECTIVES

The objective of this RFP is to secure services to implement the Design, Tender and Project Management

phases of the energy reduction project outlined in the scope of work below. Additionally, to complete

the project on time and on budget using sound project management principles with minimal disruption to

the facility and its users, ice will be maintained throughout construction.

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The consultants will review the detailed energy audit and work closely with the LCLC to ensure the final

design maximizes energy conservation and minimizes overall cost.

1.4 PROJECT SCHEDULE

Below is the approximate schedule that is expected to be followed for this RFP. However, this may be

subject to change and is therefore presented primarily for guidance:

• Preferred work start date: October 1st, 2020

• Preferred design work completion November 16st, 2020

• Preferred tender issue December 14th, 2020

• Tender construction period January 15st, 2020

• Construction completion date March 31, 2020

1.5 INQUIRIES

All inquiries about this RFP shall be directed to the individuals listed below, by e-mail only, by no later

than September 21, 2020. Answers to all submitted questions will be responded to by Sebtember 23,

2020.

Information that is obtained from any other source is not official and may be inaccurate.

Facility Contact Technical Contact

Kent Walsh

Myles Cornish

General Manager On-site Engineer

Lunenburg County Lifestyle Centre 135 North Park St.

Bridgewater NS B4V 9B3 Email: [email protected]

Town of Bridgewater 60 Pleasant St Bridgewater NS B4V 3X9 Email: [email protected]

Phone: (902) 530-4101

2.0 SERVICE REQUIREMENTS

2.1 PROJECT SCOPE

The detailed energy audit outlined six measures to conserve water, energy and improve operations. For the measures listed below, the proponents will work with the general manage of the LCLC to ensure the final design details meet the operational needs of the facility. The proponent will prepare a detailed design in line with the

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energy saving outlined in the energy audit. Following that, the proponent will create tender documents for the LCLC to review and post. The Proponent will provide Engineering Services throughout the build phase for each of the following measures.

2.1.1 GROUND LOOP FLUID REPLACEMENT AND ISOLATION Scope of work

The facility uses a number of separate water loops to provide heating and cooling for the building and its process loads including two separate cooling loops for the ice pad and AHU cooling coils, two heating loops for the in-floor heating, AHU heating coils and DHW and pool water heating, one heat recovery loop which can tie in to any of the above-mentioned loops and a geothermal field loop. As all the circulating loops are directly interconnected, the fluid medium are currently the same for all loops and satisfy the most critical freezing protection scenarios of any of the loops. The current fluid medium for the circulation loops is a mixture of 40% ethylene glycol which provides freeze protection down to -23°C (-10°F) which can be encountered at the AHU coils during extreme cold days.

For this measure the consultant will design, tender and project manage work as required to :

1) isolate this loop from the remainder of the building and replace the existing hydraulic separator;

2) serve the geothermal loop with a new heat exchanger that will act to isolate the geothermal loop fluid from the rest of the building loops. Ethylene Glycol will be removed and a new fluid medium for the geothermal loop consisting of 25% propylene glycol will be put in its place.

The addition of the new heat exchanger will result in additional pressure drop for the heat recovery loop and the geothermal loop, however this increase in pressure drop will be mitigated for the geothermal loop as the 25% propylene glycol solution has better heat transfer properties and lower viscosity which will generate pumping savings for the geothermal loop.

3) As part of this measure, new variable speed drives will be installed on the geothermal pumps to balance the system and allow variable flow through the geothermal loop to meet demand from the system while generating pumping energy savings.

2.1.2 ICE PLANT OPTIMIZATION AND HOT WATER STORAGE TANK Detailed Scope of Work

The facility uses a number of separate water loops to provide heating and cooling for the building and its process loads including two separate cooling loops for the ice pad and AHU cooling coils, two heating loops for the in-floor heating, AHU heating coils and DHW and pool water heating, one heat recovery loop which can tie in to any of the above-mentioned loops and a geothermal field loop.

The ice plant operates primarily to satisfy the ice pad cooling load and is currently controlled via an infrared temperature sensor monitoring the surface temperature of the ice. Upon a signal from the infrared sensor during resurfacing of the ice, the plant operates at high capacity to freeze the ice as quickly as possible until the ice surface temperature returns to setpoint. During this high capacity operation, large amount of heat is rejected to the low-grade loop which serve the in-floor and AHU heating. This energy rejected in most times surpasses the heating

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capacity of the low-grade loop, thus excess heat is rejected to the geothermal field and through the cooling tower. Once the ice plant turns off when the ice temperature is satisfied, the low-grade heating loop loses all heating sources. To serve the heating low-grade loop when the ice pad does not require cooling, the ice plant is required to operate to ‘cool’ the geothermal loop thus providing heating to the low-grade loop. This imbalance in cooling and heating loads between the ice rink and the low-grade loop and the lack direct storage water volume on the low-grade heating loop results in additional energy use resulting from having to constantly transfer energy to and from the geothermal loop via the ice plant compressors.

Based on the annual energy use of the ice plant, there is constantly an annual surplus of heat available from the ice plant heat rejection to more than satisfy the heating load of the low-grade loop.

For this measure the consultant will design, tender and project manage work required to:

a) install a new storage tank on the low-grade loop sized to store all the heat rejection of the ice plant during a resurfacing cycle in order to use the energy directly by the low-grade loop once the ice plant shuts off. This would prevent the ice plant from having to constantly operate open to the geothermal loop in order to satisfy the heating demand of the low-grade loop. The new storage tank would have to be between 6,000 to 8,000 gallons in water volume capacity in order to store the entire heat rejection of the ice plant during an ice resurfacing cycle. The new storage tank would be insulated and installed outside by the existing cooling tower.

2.1.3 HEATING LOOPS PIPING MODIFICATIONS AND MERGING Detailed Scope of Work

Currently, there are two (2) separate heating loops serving the facility. There is the low-grade heating loop which is served by heat rejection of the ice plant and serves the air handling units heating and in-floor heating and operates at 105°F. There is also the medium-grade heating loop which is served by the Multistack chiller and serves pool heating, DHW preheat and perimeter heating and operates at 135°F. Currently, energy sharing between the two loops is only achievable through the geothermal loop system. There is continuously excess heat being rejected from the low-grade loop to the geothermal field, and simultaneously, the Multistack constantly operates to provide heat to the medium-grade loop via the geothermal field. This simultaneous heat rejection and extraction from the geothermal field through pumping and compressor energy of the chillers and ice plant results in additional energy.

In this measure the consultant will:

1. Design, tender and project manage the work required to : merge the two heating loops together to be able to take advantage of energy sharing directly between the two loops without the use of the geothermal field and Multistack chiller.

2. Convert the 135°F loop to 105°F and then directly connect the two low-grade loops. This would minimize the use of the geothermal field and thus the use of the Multistack chiller. The Multistack chiller would then primarily be used to provide cooling for the chilled water loops and occasionally some heat to the low-grade loop only during peak heating periods.

This measure would include the replacement of the AHU-3 heating coil, and the pool water heating heat exchangers to operate at 105°F at design condition.

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2.1.4 AHU COILS FLUID REPLACEMENT AND ISOLATION Detailed Scope of Work

The facility uses a number of separate water loops to provide heating and cooling for the building and its process loads including two separate cooling loops for the ice pad and AHU cooling coils, two heating loops for the in-floor heating, AHU heating coils and DHW and pool water heating, one heat recovery loop which can tie in to any of the above-mentioned loops and a geothermal field loop. As all the circulating loops are directly interconnected, the fluid medium are currently the same for all loops and satisfy the most critical freezing protection scenarios of any of the loops. The current fluid medium for the circulation loops is a mixture of 40% ethylene glycol which provides freeze protection down to -23°C (-10°F) which can be encountered at the AHU coils during extreme cold days.

After the implementation of measure 2.1.1- Ground Loop Fluid Replacement and Isolation, the geothermal field would be isolated from the rest of the building loops. After the implementation of measure 2.1.2 - Ice Plant Optimization and Storage tank, the ice pad cooling loop can be isolated from the heat recovery loop as the ice plant would not require to ‘cool’ the geothermal loop to provide heat to the low-grade loop. As such, having the geothermal loop and the ice pad cooling loops isolated from the rest of the circulation loops, the only freeze protection remaining would be the water going to the AHU coils.

For this measure the consultant will design, tender and project management work required to :

1) isolate the AHU coil water from the remainder of the building by installing new heat exchangers for each AHU coil and new coil circulation pumps. The AHU coil loops would utilize a solution of 40% propylene glycol to provide freeze protection and the rest of the building loops (both heating loops, the heat recovery loop and the chilled water loop) can now utilize water as the fluid medium. Using water instead of the existing 40% ethylene glycol for the building loops will result in significant pumping energy savings as water has far superior heat transfer properties and lower viscosity than ethylene glycol.

2.1.5 HIGH GRADE HEAT PUMP FOR DHW AND THERAPY POOL Detailed Scope of Work

After implementation of measure 2.1.3 -Heating Loops Piping Modifications and Merging, all heating loops would operate at 105°F which would not be hot enough to provide for the heating of the domestic hot water and of the Therapy Pool. These heating loads would have to be provided by electric DHW tanks and electric boiler respectively.

In this measure the consultant will design, tender for and project manage the installation of a new high grade heat pump that would operate to produce 160°F water from the 105°F loop which would serve the high grade loads of the building including the DHW heating and the Therapy pool heating. The new heat pump would operate at a coefficient of performance (COP) of 4 which would be four times more efficient than electric elements.

2.1.6 Building Automation System (BAS) OPTIMIZATION AND ANALYTICS Detailed Scope of Work

Currently the facility is controlled by a combination of a Cimco Direct Digital Control system controlling the ice plant and a Building Automation System (BAS) controlling the space heating, air handlers and heating and cooling pumps. The pool dehumidifiers have stand-alone digital controls.

The consultant will re-commission some of the sequences to implement enhanced energy saving strategies with the

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existing Direct Digital Control systems. The strategy and changes proposed include:

• Enhanced time of day scheduling for air handlers. • Re-commissioning of critical control devices including CO2 sensors, pressure sensors, damper actuators, etc. • Temperature reset based on demand for the chilled water and hot water loops.

• Ice temperature reset based on activity level. The retrofit opportunity will require an automated method of identifying whether the BAS is consistently controlling the systems optimally or per design conditions once the site is retrofitted for a seasonal changeover. The goal will be to optimally utilize the infrastructure and setup rules to ensure continued operation and optimization over the life of the assets.

Analytics solutions will provide for optimal resets to occur to achieve the energy savings as outlined and also notify the staff in the event the systems are not reacting as expected given the conditions.

2.1.7 MEASUREMENT AND VERIFICATION METHODOLOGY

The consultant will be required to submit a Measurement and Verification Plan which shall adhere to Efficiency Nova Scotia (ENS) custom program requirements and the International Performance Measurement and Verification Protocol. The following is shown for reference and verification purposes. The contractor is expected to verify the savings shown below in their modelling prior to installation. The savings will be verified during the commissioning phase of this project. Savings that differ from the figures given below shall be brought to the Clients attention by the contractor during the bid process.

Annual cost savings from implementation are expected at the rate shown above. The successful contractor will be required to work toward this savings level during the measurement and verification stage.

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2.1.8 Project Related Documents

Energy Audit is available as Appendix A. Any additional project related documents will be made available as requested.

2.2 PROJECT MANAGEMENT

The Successful proponent shall be responsible for the project management of the portfolio for the duration of the project. The proponent shall designate in their proposal a Project Manager. All coordination for services with the LCLC and the successful proponent shall be the responsibility of the Project Manager. The Project Manager shall ensure that any substitution in proponent team personnel are approved by the LCLC General Manager. The Project Manager will update the General Manager of the LCLC bi-weekly and be available to attend the monthly meeting of the board. The works progress shall be measured against a defined budget and work schedule. As well as meet, liaise with regulatory bodies, utilities, stakeholder groups, other levels of government and members of the community, as required.

2.3 COMMISIONING The consultant will:

• Witness start up and commissioning performed by contractors and equipment manufacturer

• Verify all infrastructure has been commissioned by the contractor. Verify connectivity between all control devices in the building and the sequence of operation is as per design intent

• Facilitate training as required to ensure facility staff are confident in maintaining facility operations in optimal conditions

2.4 SCHEDULE OF EVENTS

The following shall be the proposed timeline for this project. Dates may be subject to change based on

circumstances:

EVENT Date

1. RFP Distribution to Vendors September 4, 2020

2. Questions from Vendors about scope/duties September 4 to 21, 2020

3. Responses to Vendors September 4 to 23, 2020

4. Proposal due date September 29, 2020

5. Target date for review of proposals October 6, 2020

7. Award October 8, 2020

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2.5 DELIVERABLES/MILESTONES

2.5.1 Kick Off Meeting

The consultants project team will meet with the facility Manager and the Technical Consultant from the Town of Bridgewater to set the course for the project.

2.5.2 Project Administration/Management The consultant is responsible for ensuring that the project is maintained within scope, budget and schedule and to ensure that appropriate quality control / quality assurance practices are used to provide the best project possible to the client. Major consultant activities include:

• Confirm client requirements and objectives at project outset

• Initiate meetings;

• Maintain all project documentation;

• Provide detailed project updates to General Manager on a biweekly basis;

• Provide detailed project updates in to the board of directors as requested, either in writing or in person.

• Identify and manage risks associated with the project;

• Manage communication expectations throughout the project;

• Manage overall project scope, schedule, budget and quality control;

• Ensure all project changes are discussed and approved in writing by the client in advance of proceeding with the work;

Key Deliverables:

• All recorded information including project reports, project construction documents, templates, surveys, calculations, sketches, plans, meeting minutes, correspondence, operating manuals and training documents;

• Regular project updates outlining progress for the review period;

• At project outset develop risk management plan including all mitigative measures used to manage project risks;

• Documentation of any project changes (scope, schedule, budget & quality impacts) including correspondence reflecting LCLC’s approval prior to proceeding with the proposed changes.

2.5.3 Preliminary Design Study and investigate the project area, review available LCLC records, reports and collect data from other sources as required. The major tasks of this phase will be to design changes outlined in the scope of work to maximize the efficiency and operational performance of the facility. Any additional elements of redundancy or long term cost

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saving measures will be entertained at this stage. The consultant should allow for discussions with LCLC Staff, Nova Scotia Power, Efficiency Nova Scotia (as required) and other approval agencies and incentive support agencies that may be required.

2.5.4 Approvals The purpose of this tasks is to ensure all pertinent legislation is followed and the necessary approvals are in place in a timely manner. Major consultant activities include:

• Identify & obtain the appropriate approvals required for this project, including: compilation of applications, obtain permission to act as owner’s representative in this regard, submit application including all fees, follow up and supply additional information to authority as required, and receive approval;

• Consult with all relevant approval authorities to ensure the approval requirements are incorporated into the design;

• Meet with approval agencies as needed. Key Deliverables: • Documented legislation & approvals required for this project;

• Final approval certificates or authorizations from the relevant approval authority including all supporting documentation.

2.5.5 Detailed Design The purpose of this component is to complete the detailed design for all aspects of this project. In addition to meeting LCLC standards, the engineering design shall meet the requirements of Nova Scotia Environment (NSE) and conform to the requirements of other regulatory agencies, from which approval may be necessary i.e. Nova Scotia Power and Nova Scotia Department of Labor. Major consultant activities include:

• Complete the detailed design for all aspects of this project.

• Prepare the design drawings, specifications.

• Cost estimates. Key Deliverables: • Detailed design drawings, specification and detailed cost estimate.

2.5.6 Tender Phase Services

The purpose of this component is to prepare and issue a tender package on behalf of LCLC. Major consultant activities include:

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• Prepare draft tender package and submit to LCLC for review;

• Prepare and issue a tender package on behalf of LCLC;

• Respond to bidder enquiries & prepare addenda during the tendering process.

• Accept Submissions, Open, Review/Evaluate and make Recommendation on Selection in conjunction with LCLC Key Deliverables: • Tender package for issuing to bidders;

• Addenda during tendering process as needed.

• Review/Evaluate and make Recommendation on Selection in conjunction with LCLC

2.5.7 Construction and Contract Administration / Management Major activities for this component shall include:

• Perform construction management/administration & part time site inspection services;

• Facilitate and host the pre-construction meeting;

• Provide bi-weekly updates to LCLC;

• Review of shop drawings as required;

• Review all payment certificates and recommend amounts for payment based on the consultant’s determination of the work completed in a timely manner;

• Manage & resolve construction deficiencies;

• Manage site instructions, directives, contemplated change orders, and changed orders;

• Coordinate the commissioning process. Consultant is to specify in the tender documents the requirement for a methodical and organized commissioning plan and process;

• Coordinate training for LCLC staff in the operation and maintenance of the infrastructure. Training is to be provided by individuals competent in the operation of the equipment in question.

• Facilitate wrap-up meeting. This meeting shall serve as a general review of the project. It shall also serve as the appropriate setting for dissemination of information such as presentation of the project certification, record information package, operation and

maintenance manuals and the handing over of spare parts and warranties to LCLC operations staff.

Key Deliverables:

• Log of documented issues including recommended resolutions to issues;

• Record meeting minutes, reports and other correspondence related to design and construction;

• In advance of any training, provide the Record Information Package including final record drawings, Operation & Maintenance Manual, and Commissioning Report for the facility (including all setpoints, units and values);

• Provide training for LCLC Staff;

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• Provide project certification.

2.5.8 Record Information Package The purpose of this task is to provide LCLC with a complete record information package for the project. All electronic information created for the project shall be provided to LCLC and this information shall be in a format that is acceptable to LCLC. The scope of requested information includes all reports, drawings, figures, schedules, specifications and calculations etc. The consultant is to forward a draft record information package to LCLC for review and are to assume that this review will be completed in two weeks. Major consultant activities include:

• Collect and compile all necessary information for inclusion in the record information package;

• Provide a draft record information package to be submitted for review to LCLC within four weeks of the issuance of substantial completion. The final record information package is to be received by LCLC within two weeks of the consultant’s receipt of LCLC comments on the draft record information package submission.

Key deliverables:

• Provide a hard copy and an electronic copy of the complete record information package, including manuals and training documents.

3.0 ADMINISTRATIVE & LEGAL REQUIREMENTS

3.1 PROPOSER DECLARES

a. That this proposal is made without collusion or fraud.

b. That he/she has carefully examined the Contract Documents and taken all the information

provided into consideration in preparation of his/her proposal.

3.2 PROPOSER AGREES

a. To enter into a contract to provide Engineering Services to design and construct the energy

reduction upgrades to the LCLC as described and specified herein

b. That the total proposed price shall be the price given in page 28 hereunder.

c. That the proposal is valid for acceptance for 60 days from the time of proposal closing

d. Project award may be subject to approval by Board of Directors

e. That payment for items awarded by the LCLC, listed in page 28 be paid by the LCLC within 30

days of invoice receipt by the LCLC.

f. That by this Request for Proposal, the LCLC does not imply that any proposal will be accepted,

or that the lowest priced proposal will be accepted. All received proposals will be reviewed as

to their compliance with the requirements of this RFP.

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3.3 COMMERICAL LIABILITY & AUTOMOBILE INSURANCE

a. The Successful Proponent shall, at its sole cost and expense, procure, maintain, pay for and keep

in full force and effect for the entire duration of the project, Commercial General Liability

Insurance against claims for bodily injury including death, personal injury and property damage

including loss of use thereof. Prior to the commencement of any work, the Proponent shall

provide a Certificate of Insurance to the LCLC evidencing commercial general liability in the

minimum amount of $2,000,000 naming the Lunenburg County Lifestyle Centre as additional

insured and shall include cross liability and severability of interest clauses. The per occurrence

deductible shall not exceed $2,500, or in the case of a per claimant deductible, the deductible

amount shall not exceed $1,000. The certificate will also name the facilities/projects subject to

this agreement and contain a 30-day notice period of cancellation or material change

detrimental to the LCLC.

b. Coverage for all operations and liability assumed under the contract shall include but not be

limited to the following:

• Products & Completed Operations • Blanket Contractual

• Hostile Fire • Broad Form Property Damage

• Employees as Additional Insured’s • Contingent Employer’s Liability

• Non-Owned Automobile Liability • Written on an occurrence form

c. The Successful Proponent shall also provide the LCLC with a certificate of insurance

evidencing vehicle insurance with minimum limits of $2,000,000 for third party liability on

all owned and operated vehicles.

d. The Successful Proponent shall take out and keep in force Professional Liability (Errors and

Omissions) insurance in the amount of $2,000,000 minimum providing coverage for acts, errors

and omission arising from their professional services performed under this RFP. The policy

SIR/deductible shall not exceed $5,000 per claim and if the policy has an aggregate limit, the

amount of the aggregate shall be double the required per claim limit. The policy shall be

underwritten by an insurer licensed to conduct business in the Province of Nova Scotia and

acceptable to the LCLC. If policy is to be cancelled or non-renewed for any reason, 0-day notice

of said cancellation or non-renewal must be provided to the LCLC. A certificate of insurance

evidencing renewal is to be provided each and every year.

e. The insurance coverage must be maintained in force throughout the term of the agreement,

and, if applicable, any renewal after, with evidence by way of a certificate of insurance provided

to the LCLC yearly 10 days prior to the expiry of the insurance coverage. It is the responsibility of

the Successful Proponent to have this information provided to the LCLC.

f. The Successful Proponent shall be responsible for the payment of any insurance deductible

amount.

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3.4 INDEMNITY

The successful Proponent shall defend, indemnify and save harmless the LCLC, its officers, employees

and agents from and against any and all claims of any nature, actions, causes of action, losses,

expenses, fines, costs (including legal costs), interest or damages of every nature and kind whatsoever,

including but not limited to bodily injury, sickness, disease or death or to damage to or destruction of

tangible property including loss of revenue or incurred expense resulting from disruption of service,

arising out of or allegedly attributable to the negligence, acts, errors, omissions, misfeasance,

nonfeasance, fraud or willful misconduct of the successful Proponent, its directors, officers, employees,

agents, contractors and subcontractors, or any of them, in connection with or in any way related to the

delivery or performance of this Contract. This indemnity shall be in addition to and not in lieu of any

insurance to be provided by the successful Proponent in accordance with this Contract and shall

survive this Contract.

3.5 LIABILITY OF ERRORS

While the LCLC has made considerable effort to ensure an accurate representation of information in this

Request for Proposal, the information contained in this Request for Proposal is supplied solely as a

guideline for proponents. The information is not guaranteed or warranted to be accurate by the LCLC, nor

is it necessarily comprehensive or exhaustive. Nothing in this Request for Proposal is intended to relieve

proponents from forming their own opinions and conclusions with respect to matters addressed in this

Request for Proposal.

3.6 BILLING and PAYMENT

The Proponent shall submit a detailed invoice for services provided to the client at the

following address:

Lunenburg County Lifestyle Centre

135 North Park St

Bridgewater, NS B4V 9B3

Attn: Accounts Payable

A proper invoice from the Proponent shall be submitted in five identical instalments at the completion of

each significant milestone:

• Design Completion

• Tender Issued

• Construction 50% completion

• Construction completion

• Measurement & Verification

Normal payment terms for the LCLC are 30 days from receipt of invoice.

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3.7 CONTRACT AGREEMENT

The LCLC will provide notice in writing to the Proponent of the acceptance of its proposal. The proposal

forms one part of the contract and as second contract laying out terms will be provided to the proponent

and will be returned to the LCLC. . No Proponent will acquire any legal or equitable rights or privileges to

the goods or services until the occurrence of these events.

3.8 TERMINATION

a. Termination for Convenience: The LCLC may terminate a contract, in whole or in part, if

determined that such a termination is in its best interest, without showing cause, upon giving

written notice to the Proponent. The LCLC shall pay all reasonable costs incurred by the

Proponent up to the date of termination. However, in no event shall the Proponent be paid an

amount which exceeds the bid price for the work performed. The Proponent shall not be

reimbursed for any profits which may have been anticipated but which have not been earned up

to the date of termination.

b. Termination for Default: When the Proponent has not performed or has unsatisfactorily

performed the contract; the LCLC may terminate the contract for default. Upon termination for

default, payment will be withheld at the discretion of the LCLC. Failure on the part of the

Proponent to fulfill the contractual obligations shall be considered just cause for termination of

the contract. The Proponent will be paid for work satisfactorily performed prior to termination,

less any excess costs incurred by the LCLC in re- procuring and completing the work.

3.9 CONFIDENTIALITY NOTICE

The selected Proponent agrees not to release or in any way cause to release any confidential

information that pertains to the LCLC unless they have been specifically approved to do so in writing.

4.0 OTHER IMPORTANT PROVISIONS

4.1 ADDENDA AND ADDENDA ACKNOWLEDGEMENT

Responding to this RFP may require the acknowledgement of a specific addendum or multiple addenda

as part of the submission. Acknowledgement requirements, whether optional or mandatory, will be

specified in the applicable addendum. The proponent must monitor the Procurement Services website

for any addenda that may be issued during the open period of the RFP.

Proponents are responsible to ensure that they are aware of and have complied with any addenda

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issued in respect of this RFP, by visiting the Procurement Services Web site at

https://procurement.novascotia.ca.

4.2 PUBLIC OPENING

The opening of the proposals is not open to the Public due to COVID-19, for opening results please email [email protected]

4.3 CONSTRAINTS

Personal Information International Disclosure Protection

The ‘Personal Information International Disclosure Protection Act‘ of Nova Scotia (PIIDPA, creates

obligations for the LCLC and its service providers when personal information is collected or used and

disclosure of personal information. Provisions related to PIIDPA requirements are included in the contract

terms. A copy of the Act is available online at: http://nslegislature.ca/legc/statutes/persinfo.htm

4.4 CONFLICT OF INTEREST

The LCLC reserves the right to disqualify any proponent that in the LCLC’s sole opinion has an actual or

potential conflict of interest or an unfair advantage in respect of this RFP, whether existing now or is likely

to arise in the future, or may permit any such proponent to continue and impose such terms and

conditions on that proponent, as the LCLC in its sole discretion may require.

Proponents are required to disclose, to the RFP Contacts, any potential or perceived conflict of interest

issues immediately upon becoming aware of any such conflict.

5.0 SUBMISSION INFORMATION

To help ensure consistency in proponent responses and facilitate the evaluation process, the proposal

should be prepared and packaged, as outlined in the sections that follow. Please print double-sided

whenever possible and limit promotional and/or marketing materials to the information specifically

requested in this RFP.

5.1 SUBMISSION FORMAT

To ensure similarity in Proposal presentation and to facilitate the review of Proposals by the LCLC Proponents are advised to include the required material formatted as follows:

A. Cover Letter

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B. Executive Summary

• Brief overview of your company

• Description of similar work including work in the Municipal sector • Include a summary of your understanding of the service requirements specified in

this RFP. This content should be expressed in your own words.

• Highlight the key features of your proposal. It should allow the Evaluation Team to quickly gain an overall perspective of your proposal, prior to reviewing it in detail.

• Complete and include Signature form from Page 36

C. Qualifications

• Professional experience and qualifications of team members who will be assigned to this engagement, including curriculum vitae

• List of clients (including municipalities) that you have provided similar service to within the last five years along with brief summary of the engagement

• Proponent shall list the subcontractors (if any) that will assist in the completion of the work. Subcontractors must not be used without prior written approval by the LCLC

D. References

• Provide three references for any work done by your firm in the past three years that is similar in nature, complexity and size to the requirements specified in this RFP. Provide the name of each project reference, along with his/her phone number and email address. The project reference information provided should identify the size of the projects conducted, as well as demonstrate the extent of your previous experience, the clients’ overall satisfaction with your services and the results achieved, including your adherence to interim and final deadlines.

• References for the Selected Proponents may be contacted and considered in the award decision

E. Scope, Approach & Methodology

The submission of proposal on this service will be considered as a representation that the proponent has carefully investigated all conditions which may affect or may not, at some future date, affect the performance of the services covered by the proposal, the entire area to be services as described in the attached specifications and other contract documents and that the proponent is fully informed concerning the conditions to be encountered, quality and quantity of work to be performed and materials to be furnished; also, that the proponent is familiar with all Federal and Provincial laws, all codes which in any way affects the prosecution of the work or persons engaged or employed in the work. At a minimum, each submission must:

• Describe the approach and/or process proposed to address the service requirements. Include any notable methodologies, innovative solutions, tools and techniques, and their respective suitability to this project.

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• Provide a project plan and resources that reflects your proposed approach/process and demonstrates your ability to meet the schedule requirements for this project. This section should include a detailed schedule that includes critical milestones

• This section should include a description of each major type of work being done by the vendor

F. Project Management Methodology

• An organizational chart clearly identifying team roles and primary contacts to be Provided.

• A Work Breakdown Structure indicating each team member’s responsibility and contribution to be provided.

G. Detailed & Itemized Cost Proposal

• Include a detailed fee breakdown per task, associated resources and estimate of expenses

• The cost proposal shall be submitted at the same time as the technical proposal.

• Cost Proposal shall include a single page duly signed stating the proponent’s firm fixed total price for this service as outlined in the Request for Proposal.

5.2 SUBMISSION INFORMATION

a. The deadline for proposal submission is 3:00 p.m. local time September 29, 2020 at the LCLC. Proposals are to be submitted in a sealed envelope clearly marked LCLC RFP2020-02 and to be addressed to:

Lunenburg County Lifestyle Centre Co/Kent Walsh 135 North Park St. Bridgewater, NS B4V 9B3

b. Late proposals shall not be accepted by the LCLC and will be returned unopened to the

proponent. Submissions by fax and email will not be accepted.

c. Proposals may be amended or withdrawn by post, courier or fax, if the amendment or notice of

withdrawal is received prior to closing. Amendments or withdrawals must be clearly identified as such.

d. One (1) Original Proposal Package – The title page should be marked with the text ‘ORIGINAL’ at the top. The Original should be left unbound. The Original and Copies should be identical (excluding any obvious differences in labelling, as noted). If discrepancies between these items are discovered during the evaluation or during the life of any contract that emerges from this RFP, the Original retained by Purchasing shall be taken as the correct version and the proponent will be advised accordingly.

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e. Three (3) Copies of Proposal Package –. The title pages for the Copies should be prepared in the same way as the title page for the Original, except these should be marked with the text ‘COPY’ at the top. One of the Copies should be left unbound. In the interest of sustainability, please refrain from using binders, binding, plastic covers, etc. when submitting the proposal.

f. One (1) Electronic Copy – Prepare an electronic copy of your proposal as either a Portable

Document Format (PDF) file (preferably) or as an MS-Word file, and include this in your proposal. The file name should include an abbreviated form of the proponent’s name and RFP2020-02. Copies must be on Electronic Media and must be virus-free. Label the electronic media with the proponent’s name a LCLC RFP 2020-02.

g. Ensure the external packaging reflects the information listed below:

Proponent’s name LCLC RFP 2020-02

6.0 PROPOSAL EVALUATION CRITERIA

The LCLC shall review and evaluate all proposals. Evaluation will be based on the proposals as submitted. The selected vendor and proposal may be recommended to the LCLC Board of Directors for consideration for approval. When evaluating proposals, the weighting of the aforementioned criteria shall be as follows:

Item No.

Criteria Available Points

Technical Response:

1.0 Executive Summary 5

2.0 Qualifications 10

3.0 References 20

4.0 Scope, Approach & Methodology 35

SUBTOTAL ITEMS 1.0 – 4.0 70

5.0 Cost/Price _____________ / ____________ = _________________ Proposed price subtotal score price per weighted pt. Lowest price per weighted pt. ratio = 30 2nd lowest = 25 3rd lowest = 20 4th lowest = 15 5th lowest ratio (and under) = 10

30

TOTAL POINTS AVAILABLE 100

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7.0 SIGNATURE

Dated this day of 2020.

Name of Firm Proposing (seal) (SEAL)

Address

Address Telephone

Signature – Name and Title Printed

Signature – Name and Title Printed

Witness – Name and Title Printed

Note: Proposals submitted by or on behalf of any Corporation, must be signed in the Name of such Corporation by a duly authorized officer or agent, who shall also Subscribe his own name and office. AFFIX seal

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LUNENBURG COUNTY LIFESTYLE

CENTRE

ENERGY AUDIT REPORT

PROJECT #10-20-039

JULY 2020

77 VAUGHAN HARVEY BLVD., SUITE 200

MONCTON, NEW BRUNSWICK

E1C 0K2

WWW.MCW.COM

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ENERGY AUDIT REPORT

PAGE 1 JUNE 2020 CONFIDENTIAL

1 BUILDING SUMMARY ............................................................................ 2

1.1 ENERGY USAGE COMPARISON .................................................................... 5

1.2 CONSERVATION MEASURES PRIORITY MATRIX ........................................... 5

2 BACKGROUND AND METHODOLOGY ..................................................... 6

2.1 OBJECTIVES .................................................................................................. 6

2.2 ENERGY AUDIT AND ANALYSIS METHODOLOGY ......................................... 6

3 BUILDING AND SYSTEMS DESCRIPTION ................................................. 10

3.1 GENERAL FACILITY DESCRIPTION ................................................................. 10

4 UTILITY USE AND COST SUMMARY ........................................................ 13

4.1 ENERGY CONSUMPTION .............................................................................. 13

4.2 RATES USED FOR CALCULATIONS ................................................................ 15

4.3 ENERGY ACCOUNT SUMMARIES .................................................................. 15

4.4 ENERGY ALLOCATION .................................................................................. 16

5 ENERGY EFFICIENCY AND CONSERVATION MEASURES ........................... 17

5.1 ENERGY CONSERVATION MEASURE (ECM) SUMMARY ............................... 17

5.2 SHORT TERM MEASURES (IN) ...................................................................... 19

5.2.1 ECM A01: LIGHTING RETROFITS ......................................................................................... 19 5.2.2 ECM B01: GROUND LOOP FLUID REPLACEMENT AND ISOLATION .................................... 21 5.2.3 ECM B02: ICE PLANT OPTIMIZATION AND HOT WATER STORAGE TANK ........................... 23 5.2.4 ECM B03: HEATING LOOPS PIPING MODIFICATIONS AND MERGING ................................ 25 5.2.5 ECM B04: AHU COILS FLUID REPLACEMENT AND ISOLATION ............................................ 27 5.2.6 ECM B05: HIGH GRADE HEAT PUMP FOR DHW AND THERAPY POOL ............................... 29 5.2.7 ECM C01: BAS OPTIMIZATION AND ANALYTICS ................................................................. 31

5.3 LONG TERM MEASURES (OUT) .................................................................... 34

5.3.1 ECM B06: RINK DEHUMIDIFICATION UPGRADE ................................................................. 34 5.3.2 ECM D01: SOLAR PV INSTALLATION ................................................................................... 36

6 CONCLUSION ........................................................................................ 38

APPENDICES:

APPENDIX A - LIGHTING RETROFIT SUMMARY SHEET (NOT USED)

APPENDIX B - ENERGY UTILITY DATA

APPENDIX C - ENERGY BALANCE

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1 BUILDING SUMMARY

The purpose of this feasibility study is to identify and analyze energy efficiency and conservation

opportunities, which could result in energy savings for the facility. There is potential to improve

energy efficiency through upgrades and integrating technology advancements in the following areas:

• Energy efficient lighting technology;

• System Re-piping & Energy Sharing Optimization;

• Controls Optimization; and

• Variable Flow Pumping Technology.

To improve the facility’s operation and performance, energy conservation opportunities have been

identified that will reduce energy consumption and demand. An overall summary of the building’s

energy usage and proposed energy program is summarized in Table 1.1 – Building Energy Usage and

Savings Summary. A more detailed summary of the savings opportunities for all energy conservation

measures is presented in Table 1.2 – Energy Conservation Measure Summary. Section 5 – Energy

Efficiency and Conservation Measures summarizes the recommended improvements that have been

identified for Lunenburg County Lifestyle Centre.

The energy savings associated with the recommended program represent an 18.1% reduction in

annual energy consumption from the existing usage. The program has the benefit of reducing the

facility’s average energy intensity from 33.8 ekWh/ft²/year to 27.7 ekWh/ft²/year and the utility cost

intensity from $4.90 per ft²/year to $4.12 per ft²/year. Implementation of the proposed program will

eliminate 460 tonnes of eCO2 per year which is an 18.1% greenhouse gas emissions reduction.

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Table 1.1 – Building Energy Usage and Savings Summary

Current Usage Energy Savings and Implementation Costs

Building Size 94,280 ft² Total Implementation Cost $1,024,248

Total Annual Electrical

Consumption 3,182,400 kWh

Annual Electrical Consumption

Savings 574,524 kWh

Total Annual Electrical Demand 6,952 kW Annual Electrical Demand

Savings 740 kW

Total Annual Water Consumption 7,283 m3 Annual Water Consumption

Savings 0 m3

Annual Total Energy Cost $461,076 Total Energy Cost Savings $72,676

Current GHG Emissions 2,540 Tonnes

of eCO2 Simple Payback 14.1 years

Energy Use Intensity GHG Emission Savings 460 tonnes of eCO2

Total Energy Use Intensity (EUI) 33.8 ekWh/ft²-yr Potential Efficiency NS

Incentives $43,792

Demand Intensity 73.7 W/ft²-yr Simple Payback with Incentives 13.5 years

Electrical Consumption Cost $0.10453/kWh Water Consumption Cost $1.353/ m3

Electrical Demand Cost $17.055/kW

Notes

• Total Implementation Cost includes soft costs such as engineering fees and construction management.

These costs do not include contingencies and taxes.

• The Electrical Demand Cost is a true cost rate factoring the change in Electrical Consumption rates

dependent on the monthly demand (200kWh*kW monthly*($0.13732-$0.10453)+$10.497 = $17.055/kW)

Performance Review

The Energy Utilization Indices (EUI) represents the equivalent kilowatt hours/per square feet (ekWh/ft2) of energy

intensity for a building and is used to index the energy performance a building. The Lunenburg County Lifestyle Centre

has a EUI of 33.8 ekWh/ft2-yr, which seems average for a building of this type. Its Demand Intensity of 74 W/ft2-yr is

also average for this type of building. Refer to Table 1.3 Energy Usage Comparison for comparison with similar

Canadian Recreation facilities.

Efficiency NS - Commercial Program

This building may be eligible for a possible implementation incentive through the Efficiency NS Incentive program.

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PAGE 4 JUNE 2020 CONFIDENTIAL

Table 1.2 – Energy Conservation Measure Summary

Note: Measure A01 – Lighting Retrofits is not included for incentives through the Custom program since other ENS programs are available for lighting upgrades. Incentive funding would still be available through

the Business Energy Rebate (BER) Program.

BLDG #

MSR TAG

BUILDING

MEASUREIN/O UT

TO TAL

SAVINGS

[$]

ELECTRICITY

CO NSUMPTIO N

[kWh]

ANNUAL

ELECTRICITY

DEMAND

[kW]

ENERGY

[GJ]

eCO 2

[Tonnes]

CO NSTRUCTIO N

TO TAL

[$]

TO TAL

FEES

[$ ]

TO TAL

MEASURE CO ST

[$]

SIMPLE

PAYBACK

[Years]

EFFICIENCY NS

INCENTIVES

[$ ]

SIMPLE

PAYBACK

w/INCENTIVES

[Years]

01 - LUNENBURG COUNTY LIFESTYLE CENTRE 72,676$ 574,524 740.0 2,068 460 890,650$ 133,598$ 1,024,248$ 14.1 43,792$ 13.5

A01 Lighting Retrofits IN 18,713$ 136,600 260.0 492 109 147,850$ 22,178$ 170,028$ 9.1 - 9.1

B01 Ground Loop Fluid Replacement and Isolation IN 904$ 8,649 - 31 7 66,000$ 9,900$ 75,900$ 84.0 865$ 83.0

B02 Ice Plant Optimization & Hot Water Storage Tank IN 11,386$ 108,929 - 392 87 200,000$ 30,000$ 230,000$ 20.2 10,893$ 19.2

B03 Heating Loops Piping Modifications & Merging IN 7,782$ 74,448 - 268 60 186,800$ 28,020$ 214,820$ 27.6 7,445$ 26.6

B04 AHU Coils Fluid Replacement and Isolation IN 7,285$ 69,694 - 251 56 80,000$ 12,000$ 92,000$ 12.6 6,969$ 11.7

B05 High Grade Heat Pump for DHW and Therapy Pool IN 16,252$ 77,159 480.0 278 62 170,000$ 25,500$ 195,500$ 12.0 7,716$ 11.6

B06 Rink Dehumidification Upgrade OUT -14,876$ -56,657 -525.0 -204 -45 600,000$ 90,000$ 690,000$ -46.4 - -46.4

C01 BAS Optimization and Analytics IN 10,353$ 99,045 - 357 79 40,000$ 6,000$ 46,000$ 4.4 9,905$ 3.5

D01 Solar PV Installation OUT 5,540$ 53,000 - 191 42 150,000$ 22,500$ 172,500$ 31.1 5,300$ 30.2

$ 72,676 574,524 740.0 2,068 460 $ 890,650 $ 133,598 $1,024,248 14.1 $ 43,792 13.5

SAVINGS INCENTIVES

PROGRAM TOTAL

COSTS BUILDING / MEASURE

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1.1 ENERGY USAGE COMPARISON

The following provides a summary of comparable energy use (ekWh/ft2) for similar community

centres with pools and ice rinks within Eastern Canada. This information is based on our previous

assessments on similar centres.

Table 1.3 – Energy Usage Comparison

Facility Facility Description Energy Usage Intensity

Lunenburg County Lifestyle Centre 1 indoor rink + Indoor Pool 33.8 ekWh/ft2

Comparable NS Community Centre 1 indoor rink + Indoor Pool 32.9 ekWh/ft2

Comparable Ontario Community Centre 2 indoor rinks + Indoor Pool 41.5 ekWh/ft2

Energy Star Portfolio – Canadian National Median –

Recreation Centres

Various Indoor rinks & Pools 45.4 ekWh/ft2

1.2 CONSERVATION MEASURES PRIORITY MATRIX

The proposed energy conservation measure program can be implemented in phases following

priorities based on risk mitigation and energy potential as per the following matrix. Note that some

measures are interdependent to other measures and therefore the following measure

implementation priority should be followed based on a phased approach.

Table 1.4 – Energy Conservation Measures Priority Matrix

Priority

Measures Energy Cost

Savings (Rolling

Total)

Implementation Cost

(Rolling Total)

Potential ENS

Incentive (Rolling

Total)

Simple Payback

w/ Incentive

(Rolling Total)

1 B01 $904 $75,900 $865 83.0 yrs

2 Priority 1 + C01 $11,257 $121,900 $10,770 9.9 yrs

3 Priority 2 + A01 $29,970 $291,928 $10,770 9.4 yrs

4 Priority 3 + B02 $41,356 $521,928 $21,663 12.1 yrs

5 Priority 4 + B03 $49,138 $736,748 $29,108 14.4 yrs

6 Priority 5 + B04 $56,423 $828,748 $36,077 14.0 yrs

7 Priority 6 + B05 $72,676 $1,024,248 $43,792 13.5 yrs

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PAGE 6 JUNE 2020 CONFIDENTIAL

2 BACKGROUND AND METHODOLOGY

2.1 OBJECTIVES

The objective of this ASHRAE Level II energy audit was to provide the Lunenburg County Lifestyle

Centre with a comprehensive plan to outline, evaluate, and report on the following:

• The current state of energy usage within the audited facility;

• Opportunities for “Greenhouse Gas Reductions”;

• Measures for improving energy efficiency and conservation;

• Measures for reducing the cost of energy and providing equipment renewal;

• The financial impact of implementing the energy efficiency and conservation measures (ECM),

including capital cost and projected annual savings; and

• Provide guidelines for making future decisions related to capital investments and operational

changes which impact energy usage.

The project approach included preliminary planning sessions, meetings with key personnel identified

by the client, site work, and a full energy consumption analysis for the facilities. Our methodology

included continuous communications with key client contacts. The process explained in subsequent

sections was followed to ensure a systematic and comprehensive approach to the project.

2.2 ENERGY AUDIT AND ANALYSIS METHODOLOGY

In order for audit results to be both meaningful and reliable, a strategic approach was taken. All

energy consuming systems were evaluated in conjunction with the intended use of the building. The

proposed measures bring value from both an energy reduction and a building operation standpoint.

The purpose of the energy audit is to identify current condition of the facility, building equipment,

mechanical and electrical systems, and the potential improvements that would result in energy and

energy cost savings. The facility’s equipment and systems were reviewed to evaluate and confirm

current conditions, remaining useful life, operating profiles, efficiencies, methods of control and the

quality of maintenance.

Site Visits and Interviews

A site visit was carried out on May 27, 2020 to review the building systems. Interviews were

conducted with building operation and maintenance staff to obtain an understanding of the building

systems operations, occupancy patterns, existing problems, past upgrades and renovations and

energy challenges. Building drawings, maintenance manuals and energy consumption information

were collected.

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Lighting Audit and Analysis

The purpose of the lighting study is to conduct an audit of the existing lighting systems and its

controls, to evaluate the potential savings opportunities and to report the recommended lighting

retrofits or replacement for the facility. The audit process included a general walk through of the

buildings. An inventory of the current lighting systems of each room was documented and factors

such as the type and quantity of the lighting system installed, their hours of operation and the level

of lighting they provided in the area they serve were noted. The analysis of the lighting systems

consisted of entering the inventory into a database where possible measures were determined.

Note that a full lighting audit has not been completed for the facility and lighting consumption and

potential savings were approximated based on a lighting fixture count from the original

construction drawings and compared to similar facilities. It is recommended that a detailed lighting

study be completed and measure savings updated prior to implementing any lighting upgrades.

Mechanical Audit and Analysis

The purpose of the mechanical study is to conduct an audit of the existing mechanical systems and

its operations, to evaluate the potential savings opportunities and to report the recommended

mechanical improvements for the facility. The mechanical audit consists of an on-site review of the

buildings and key process equipment, mechanical and electrical system components.

The audit process included the collection of information such as equipment schedules, condition and

control settings. An inventory of the major electrical and mechanical systems was documented.

Operational review of the existing energy management control system (EMCS) was used to provide

insight into how systems operated. The analysis of the mechanical systems consisted of entering the

gathered data into an energy modeling program where possible measures were determined.

Note that at the time of the audit, most equipment were not operational including the ice plant as

the ice was removed and two of the three pools were drained for yearly cleaning. As such, a number

of assumptions were applied to model the operation of the building when fully operational. It is

recommended to revisit the site to gather operational information once the ice plant is in use and

to make any adjustments to the energy model accordingly prior to implementing any upgrades as

outlined in this report.

Energy Analysis Methodology

Energy modeling provides a thorough review and evaluation of the energy use profiles of the facility.

This analysis established a baseline of energy consumption from which savings were measured and

serves as a guide to investigate certain building systems and operations exhibiting energy saving

potential.

The energy analyses were carried out based on the gathering of building equipment data and

information on the hours of operation for all building equipment through system schedules,

discussion with building operators and site observations. The energy consumption for each system

was calculated and the breakdown of the energy consumption and demand was determined.

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Once the model is reconciled with the actual energy consumption, the total energy use is broken

down into the relative proportion of the overall use for each main system. The energy use analysis is

conducted to summarize the total energy use and cost and is used to assist in the identification of the

measures.

For most projects, the value used for energy consumption analysis is the Energy Utilization Index

(EUI), an industry approved method of estimating energy consumption for all fuel sources. The EUI

represents the equivalent kilowatt hours/per square feet (ekWh/ft2). The EUI helps to understand

how the facility is consuming energy, as well as an indicator of the potential for energy savings for the

future.

Measure Selection Criteria

Once the energy analysis and reconciliation was completed, Energy Conservation Measures (ECMs)

were developed on the basis of looking at each of the energy consuming systems and, in conjunction

with the information gathered on how the facility is used, determining the most energy efficient way

of operating the facility.

As well as the obvious choices of either replacing or retrofitting inefficient equipment, the impact of

each ECM on the operation of the facilities, its maintenance programs, applicability and

constructability was considered.

Measures proposed for implementation on this project were selected based on the viability of the

measure against the following criteria:

• costs and savings within overall payback;

• condition of existing systems and requirements for short term equipment renewal;

• cost to retrofit the existing system compared to the cost to replace the system;

• overall impact on occupants and general acceptance of changes; and

• equipment approval by facilities personnel.

Cost Estimation Methodology

Costs were determined from data from previous projects, not theoretical pricing. In some

circumstances, the measures were reviewed with equipment suppliers before finalizing our cost

estimates. It is our intent to provide accurate pricing; however, the pricing provided should be used

as budgets only and not fixed prices. Pricing summary tables does include professional fee budgets

for engineering and construction management.

Savings Methodology

The savings for lighting and mechanical measures were calculated by customized spreadsheets and

databases wherein existing and proposed energy use can be tabulated. Savings estimates are based

on engineering calculations.

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Cost / Benefit Analysis

Retrofit alternatives were evaluated and measures were selected to yield a positive net present value.

Measures were evaluated on simple payback, return on investment and net present value. More

details about the assumptions used for the measure savings and cost analysis are included below:

1. The costs included are based on installed costs. These costs include materials and labour. Costs

do not include possible extra costs for painting, asbestos abatement, PCB Ballast disposal or costs

for other unknown installation factors.

2. Electrical costs are based on published NS Power rates. Water charges are based on published

Town of Bridgewater rates.

3. Electrical saving estimates include consumption and demand savings.

4. Hours of operation are based on information provided by staff, information gathered on-site,

and direct observation of operations. Where hours of operation are not fixed or are variable,

effort has been made to use conservative estimates for hours of operation.

5. All lamp and ballast watts are based on published figures from manufacturer literature.

6. The saving calculations are estimates of savings potential. The impact of building changes, use

changes, new equipment, additional computers and weather need to be considered when

evaluating savings.

7. Applicable taxes are not included in the budget costs or savings.

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3 BUILDING AND SYSTEMS DESCRIPTION

3.1 GENERAL FACILITY DESCRIPTION

Facility Name: Lunenburg County Lifestyle

Centre

Facility Location: 135 N Park Street

Bridgewater, NS

Building Type: Multi-Purpose Recreation &

Cultural Centre

The Lunenburg County Lifestyle Centre is a multi-purpose facility opened in 2013. The sport,

recreation, and community facility houses an NHL-size arena (Clearwater Seafoods Arena) with a

capacity to seat 1,200 spectators; an aquatic centre (BMO Financial Group Aquatic Centre) suited to

both leisure and competitive users; a therapeutic pool; and a public library. Other multi-purpose

spaces include administrative offices, community and cultural spaces, and areas capable of hosting

meeting, exercise classes, senior citizens’ activities, and many other functions.

The address of the facility is 135 N Park Street, Bridgewater, Nova Scotia.

The exterior of the building consists of metal cladding walls with a built-up roof. Estimated insulation

values of R-12 and R-25 have been attributed to the walls and roof respectively. The windows are

aluminum frame double pane glass type with an estimated insulation value of R-2.5.

The facility is mostly occupied from 6 am to 10 pm Monday to Sunday.

Lighting Systems Description

The Lunenburg County Lifestyle Centre is currently utilizing mostly a combination of T8 fluorescent

lighting complete with electronic ballasts.

The lighting levels in most of the above areas were reported as being adequate by facilities staff. In

general, the original luminaires in this facility are nearing 6 years old and are in relatively good

condition.

The high bay luminaires that are presently illuminating the arena ice surface are T8 technology. These

luminaires have switching abilities.

More details on the lighting systems can be found in Appendix A – Lighting Retrofit Summary Sheet.

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Mechanical Systems

A number of circulating loops provide heating and cooling for the facility. The facility is mainly heated

by one (1) low-grade heating loop (at 105°F) and one (1) medium-grade heating loop (at 135°F). There

is a rink cooling loop (20°F) and a chilled water loop (45°C) serving the ice rink and air handling unit

cooling loads respectively, and a geothermal field water loop provided heat source and sink to the

facility as required throughout the year. There is also a heat recovery loop which can be open to any

of the above-mentioned loops (low-grade loop, medium-grade loop, chilled water loop, geothermal

field loop, and ice rink cooling loop) used to share energy within the facility.

The low-grade heating loop operates at 105°F and is supplied by the heat rejection of the ice plant

and serves the in-floor heating and all the air handling unit heating coils except for the pool AHU-3. If

the heat rejected by the ice plant is greater than the demand for AHU heating and in-floor heating,

the excess heat from the low-grade loop is rejected first to the heat recovery loop and as second stage

to a cooling tower. If additional heat is required for the low-grade loop when the ice rink is satisfied,

the ice plant can operate to transfer heat from the heat recovery loop to the low-grade loop. Due to

the intermittent operation of the ice plant, the low-grade loop constantly switches from having to

reject heat to the heat recovery loop and to the cooling tower and from requiring additional heat

from the heat recovery loop. The lack of water volume storage for the low-grade loop prevents the

ice plant and the low-grade loop from operating in unison based on steady load demand.

The medium-grade heating loop operates at 135°F and is heated by the condenser heat rejection of

a Multistack chiller which simultaneously provides cooling to the chilled water loop which operates

at 45°C. The Multistack chiller operates between a chilled water buffer tank and a medium-grade

buffer tank. The medium-grade heating loop provides heating for the pool water heating (all three

pools), the perimeter radiator heaters, the pool AHU-3 heating coil and also provides domestic hot

water preheat for the Zamboni water and main domestic hot water systems. The Multistack operate

to maintain the loop requiring the most demand between the chilled water and medium-grade loops.

If excess heat is supplied to the medium-grade loop, the excess heat is rejected to the heat recovery

loop and if additional heat is required for the chilled water loop, additional heat is provided by the

heat recovery loop. An electric boiler is connected to the medium-grade heating loop for

supplemental and backup heating capability, but according to the operational staff, the electric boiler

does not require to operate often.

There is also a heat pump loop which connect directly to the heat recovery loop and supplies a

number of distributed heat pumps that provide heating and cooling for the library and office areas of

the facility. A geothermal field water loop is directly connected to the heat recovery loop and provides

heat addition and rejection capability for the loop depending on the heating/cooling equilibrium of

the facility. It was found that the geothermal loop operates almost continuously during the year and

that the geothermal loop temperature is relatively high throughout the year suggesting that overall

there is a yearly surplus of heat from the facility that continuously rejects to the geothermal field.

As all the loops are openly interconnected via the heat recovery loop, all circulating loops utilize 40%

ethylene glycol as a fluid medium. 40% ethylene glycol is required for freeze protection of the ice rink

cooling loop and for the air handling units heating coils.

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The ice plant consist of a packaged CIMCO plant utilizing three (3) 40 ton capacity screw type

compressors. The ice rink is controlled by an infra-red temperature sensor and the rink slab pump

cycles as required to provide cooling for the ice pad. Zamboni uses 160°F hot water and requires on

average 100 gallon of water per flood. The rink humidity is controlled by four (4) desiccant electric

dehumidifiers.

The pool area is ventilated, dehumidified and heated by a mixed air rooftop unit (AHU-3). The AHU-3

has DX cooling to provide dehumidification and the excess heat from the dehumidification is used to

heat the pools. Each pool has a filter pump that operates continuously to provide water filtration and

chemical treatment. A rooftop solar water heater provides preheating for the lap pool.

Ventilation for the rest of the facility (other than the pool area) is provided by five (5) rooftop air

handling units. AHU-1 is a mixed air unit providing heating and cooling to the lobby area of the

building, AHU-2 is a 100% outside air unit with heat recovery providing ventilation to the pool change

rooms, AHU-3 serves the pool as described above, AHU-4 and AHU-5 are 100% outside air units with

heat recovery providing ventilation to the ice rink and rink changing rooms.

Controls Systems

Most of the buildings ventilation, heating and cooling systems are controlled by a modern building

automation system. The CIMCO ice plant and the pool dehumidifier are controlled each by their

individual stand-alone controller.

Domestic Water System

Domestic hot water is provided by a combination of preheat tanks from the medium-grade loop, and

electric tank heaters. The washrooms generally uses low flow fixtures.

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4 UTILITY USE AND COST SUMMARY

4.1 ENERGY CONSUMPTION

MCW Maricor was provided with utility data from the client. The data was compiled and entered into

an energy accounting database in order to conduct a utility bill analysis. The analysis is based on the

most representative year, selected from the data received. Energy usage was analyzed for the

following periods:

• Electricity: January 2016 to December 2018

• Water: January 2016 to December 2017

The following figures illustrate the monthly profiles for the representative utility usages. The yearly

profiles and monthly consumption summaries are found in Appendix B – Energy Utility Data.

Figure 4.1.1 – Electrical Consumption Profile

The above electrical consumption profile shows no correlation with the heating degree day (HDD)

profile which is typical for this type of building as the major energy usage of the building (pool and

rink energy) are not affected much by the exterior environment. Throughout the summer months

(June and August), the consumption is reduced due to the removal of the ice and subsequent shut off

of the ice plant.

0

200

400

600

800

1,000

1,200

0

50,000

100,000

150,000

200,000

250,000

300,000

350,000

400,000

450,000

Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec

De

gre

e D

ays

Co

nsu

mp

tio

n (

kWh

)

2016 2017 2018 HDD (2018)

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Figure 4.1.2 – Electrical Demand Profile

The above electrical demand profile is consistent with the consumption profile which is to be

expected. The electrical demand drop during the summer months is attributed to the ice plant being

not operational.

Figure 4.1.3 – Water Consumption Profile

The above water consumption profile shows a pretty consistent usage throughout the year with a

slight increase during the winter due to the additional water use for ice resurfacing.

0.0

0.2

0.4

0.6

0.8

1.0

1.2

1.4

1.6

0

100

200

300

400

500

600

700

800

Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec

Loa

d F

act

or

De

ma

nd

(kW

)

2016 2017 2018

2016 2017 2018

(Demand)

(Load Factor)

0

500

1,000

1,500

2,000

2,500

Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec

Co

nsu

mp

tio

n (

m3)

2016 2017

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4.2 RATES USED FOR CALCULATIONS

In order to evaluate the savings potential of the energy efficiency and conservation measures, the

following energy rates were used. The information is based on the most recent rates published by NB

Power and Town of Sussex.

Table 4.2.1 – Utility Rates (Not including HST)

Utility Vendor Rate Marginal Rates

Electricity Nova Scotia Power

Account #1849728-9 11M

Energy Rate

First 200 kWh per kW of

monthly demand

Balance kWh

$0.13732 / kWh

$0.10453 / kWh

Demand Charge $10.497 / kW

Water

Bridgewater Public

Service Commission

Account #0025684251

Account #0025684261

WBCM

WBCM5

First 100,000 m3

> 100,000 m3

$1.353 / m3

$0.586 / m3

4.3 ENERGY ACCOUNT SUMMARIES

The energy cost allocation of the facility was based on the utility data received and is summarized in

Table 4.3.1 – Energy Usage Summary. Note that the applicable taxes and the utility base charges are

not included in any cost calculations. The analysis is based on the most recent year of data.

Table 4.3.1 – Energy Usage Summary

Utility Baseline Amount Unit Utility Cost

Electricity

Electrical Consumption Jan/18-Dec/18 3,182,400 kWh $378,247

Electrical Demand Jan/18-Dec/18 6,952 kW $72,975

Water

Water Consumption Jan/16-Dec/17 7,283 m3 $9,854

Total Utility Cost $461,076

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4.4 ENERGY ALLOCATION

The energy usage profiles for electricity and water are illustrated in the following figures. Appendix C

– Energy Balance provides details on the energy end use of each utility.

Figure 4.4.1 – Electrical Consumption Breakdown

Ventilation Fans:

11%

Lighting:

10%Space Heating:

5%

Ventilation

Heating:…

Pool

Dehumidification:

3%Cooling:

1%Pool Pumps:

8%

Heating Pump:

17%

Ice Plant:

24%

Rink

Dehumidification:

5%

Misc. Elec:

3%

DHW:

2%

Pool Makeup Water:

3%

Ice Resurfacing:

1%

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5 ENERGY EFFICIENCY AND CONSERVATION MEASURES

This section will provide the conceptual and financial information related to the various energy

efficiency and conservation measures (ECM) that were identified during our investigation and

analysis. It should be noted that each opportunity was evaluated independently of the others in order

to eliminate the impact of one opportunity on the results of another. Therefore, the energy and

financial savings resulting from the implementation of all opportunities may not result in the total of

all the savings listed below.

The estimated implementation costs are based on our knowledge of industry pricing, equipment

supplier pricing and past experiences. The key retrofit features and benefits are:

• Facility renewal and lowered maintenance;

• Conservation of water and energy, environmental benefits; and

• Energy cost savings.

5.1 ENERGY CONSERVATION MEASURE (ECM) SUMMARY

Table 5.1.1 – Energy Conservation Measure (ECM) Summary

ECM Tag Measure Name Measure Summary

A Lighting Retrofits

A01 Lighting Retrofits Installation of new LED lamps and electronic ballasts throughout the facility.

B Mechanical

B01 Ground Loop Fluid

Replacement and

Isolation

Install new heat exchanger for geothermal loop and isolate from rest of

building water loops. Change geothermal loop fluid to environment friendly

propylene glycol.

B02 Ice Plant

Optimization & Hot

Water Storage Tank

Install new 6,000 gallons hot water storage tank located outside by existing

cooling tower to store ice plant heat rejection energy for direct use for the low-

grade heating loop.

B03 Heating Loops

Piping Modifications

& Merging

Piping modification to combine both the low-grade loop and medium-grade

loop to both use the ice plant heat rejection energy directly.

B04 AHU Heating Coils

Fluid Replacement

and Isolation

Install new heat exchangers and heating coil pumps to isolate the heating coil

fluid from the rest of the building water loops. Change the building loops fluid

to water.

B05 High Grade Heat

Pump for DHW and

Therapy Pool

Install new high grade heat pump to provide all the DHW and Therapy Pool

heating.

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Table 5.1.1 – Energy Conservation Measure (ECM) Summary

ECM Tag Measure Name Measure Summary

B06 Rink

Dehumidification

Upgrade

Replace the existing four (4) dehumidification units with a new rooftop

desiccant AHU to serve the rink utilizing low-grade heat from the ice plant for

desiccant wheel regeneration.

C Controls

C01 BAS Optimization

and Analytics

Retro-Commissioning and Optimization of the controls and Analytics package

for continuous monitoring and optimization.

D Renewable Energy

D01 Solar PV Installation Installation of a solar photovoltaic array.

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5.2 SHORT TERM MEASURES (IN)

5.2.1 ECM A01: LIGHTING RETROFITS

Detailed Scope of Work

The Lunenburg County Lifestyle Centre is currently using a variety of fluorescent luminaires complete

with T8 lamps and electronic ballasts for their main source of interior lighting.

The luminaires within this complex were found to be rather new and in very good condition. It is

recommended that the complex go through a re-lamp and re-ballast of these fixtures. This measure

would include re-lamping with new 15 watt LED tubes and low ballast factor electronic ballast.

The high bay luminaires that are presently illuminating the arena ice surface are T8 technology. These

luminaires have switching abilities.

It is recommended that the existing T8 luminaire technology in the arena, illuminating the ice surface,

be replaced with new high bay LED luminaires. This measure will lower the power requirement within

the space and will hold the existing light level on the playing surface. With this new LED system we

recommend a new controller for the arena lighting, which will have the ability to set light levels for

different activities on the ice surface. It is recommended that this new controller be located in a more

convenient location than the existing system as discussed with the operations staff. Energy savings

will be realized by giving the operators the ability to control this system from a much more convenient

location.

Note that a full lighting audit has not been completed for the facility and lighting consumption and

potential savings were approximated based on a lighting fixture count from the original

construction drawings and compared to similar facilities. It is recommended that a detailed lighting

study be completed and measure savings updated prior to implementing any lighting upgrades.

Impact on Maintenance

Although it is difficult to put an actual number in place for maintenance savings, there will be a certain

degree of maintenance savings by applying these measures. With the guarantees from the

manufacturers on the application of new linear fluorescent lamps, as well as the long life expectancy

of new LED technology, the measures will represent an estimated annual maintenance savings of

several days.

The proposed retrofit will have the short term benefit of delaying the need for replacement of lamps

and ballasts. Because LED’s lumen output depreciates over time rather than instant failures, the

facility can choose to embark on a group re-lamping program in the future, where all lamps in a

section of the building are changed, once typical lumen output has depreciated to ~70% original

output; this is a common industry practice.

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Expected Service Life of Measure

From the time the work has been performed the new LED tubes and electronic ballasts come with a

six year manufacturer’s guarantee and the new luminaires have a warranty of five years with a life

expectancy of 20 years.

Assumptions & Calculations

The following assumptions were applied:

• Estimates for hours based on talks with building staff.

• Pre and post wattages used gathered from fixture manufacturers.

Heating penalty and cooling credit are calculated using engineering calculation spreadsheets.

Impact on GHG Emissions

Reduction in electrical energy related to lighting would have a direct impact on greenhouse gas

emissions.

Cost & Savings Summary

Annual consumption savings:

Annual demand savings:

136,600

260

kWh

kW

Savings reconciled at:

Total implementation cost:

Simple payback:

$18,713

$170,028

9.1

years

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5.2.2 ECM B01: GROUND LOOP FLUID REPLACEMENT AND ISOLATION

Detailed Scope of Work

The facility uses a number of separate water loops to provide heating and cooling for the building and

its process loads including two separate cooling loops for the ice pad and AHU cooling coils, two

heating loops for the in-floor heating, AHU heating coils and DHW and pool water heating, one heat

recovery loop which can tie in to any of the above-mentioned loops and a geothermal field loop. As

all the circulating loops are directly interconnected, the fluid medium are currently the same for all

loops and satisfy the most critical freezing protection scenarios of any of the loops. The current fluid

medium for the circulation loops is a mixture of 40% ethylene glycol which provides freeze protection

down to -23°C (-10°F) which can be encountered at the AHU coils during extreme cold days.

Ethylene glycol typically is not used for geothermal loop application as it is poisonous and pose a risk

to the underground water aquifers in the event of leaks, etc. The CSA C448 item 5.7.1.1.2 specifically

states that: “Potassium acetate or ethylene glycol shall not be used within heat transfer fluid solutions

in ground source heat pumps systems”. Acceptable anti-freeze fluids include ethanol, propylene

glycol, and methanol solutions.

In order to comply with the local codes and standards and to reduce the environmental risk associated

with the use of ethylene glycol solutions for the geothermal field loop, it is recommended to isolate

this loop from the remainder of the building and to use an acceptable anti-freeze solutions for the

geothermal loop. It is proposed to replace the existing hydraulic separator 2 serving the geothermal

loop with a new heat exchanger that will act to isolate the geothermal loop fluid from the rest of the

building loops. It is proposed to use a new fluid medium for the geothermal loop consisting of 25%

propylene glycol, which would provide freeze protection down to -6°C (21°F) which is suitable for

geothermal applications. The addition of the new heat exchanger will result in additional pressure

drop for the heat recovery loop and the geothermal loop, however this increase in pressure drop will

be mitigated for the geothermal loop as the 25% propylene glycol solution has better heat transfer

properties and lower viscosity which will generate pumping savings for the geothermal loop. As part

of this measure, new variable speed drives will be installed on the geothermal pumps to balance the

system and allow variable flow through the geothermal loop to meet demand from the system while

generating pumping energy savings.

Impact on Maintenance

The addition of a second type of glycol anti-freeze will add to the maintenance and result in additional

stored products.

Impact on Indoor Environment

No impact.

Expected Service Life of Measure

Variable Frequency Drives: 15 years

Heat Exchangers: 25 years

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Assumptions

The following assumptions were applied:

• Existing Geothermal Pumps P-2 and P-3 operation; 15HP @ 80% motor load

• Existing Heat Recovery Loop Pumps P-4 and P-5 operation; 7.5 HP @ 80% motor load

• New Geothermal Pumps P-2 and P-3 c/w VFD operation; 15HP @ 70% yearly average motor

load

• New Heat Recovery Loop Pumps P-4 and P-5 operation; 7.5 HP @ 85% yearly average motor

load

Impact on GHG Emissions

Reduction in pumping energy will result in electrical consumption savings which will have a direct

impact on greenhouse gas emissions.

Cost & Savings Summary

Annual consumption savings: 8,649 kWh

Savings reconciled at:

Total implementation cost:

Simple payback:

$904

$75,900

84.0

years

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5.2.3 ECM B02: ICE PLANT OPTIMIZATION AND HOT WATER STORAGE TANK

Detailed Scope of Work

The facility uses a number of separate water loops to provide heating and cooling for the building and

its process loads including two separate cooling loops for the ice pad and AHU cooling coils, two

heating loops for the in-floor heating, AHU heating coils and DHW and pool water heating, one heat

recovery loop which can tie in to any of the above-mentioned loops and a geothermal field loop.

The ice plant operates primarily to satisfy the ice pad cooling load and is currently controlled via an

infrared temperature sensor monitoring the surface temperature of the ice. Upon a signal from the

infrared sensor during resurfacing of the ice, the plant operates at high capacity to freeze the ice as

quickly as possible until the ice surface temperature returns to setpoint. During this high capacity

operation, large amount of heat is rejected to the low-grade loop which serve the in-floor and AHU

heating. This energy rejected in most times surpasses the heating capacity of the low-grade loop, thus

excess heat is rejected to the geothermal field and through the cooling tower. Once the ice plant turns

off when the ice temperature is satisfied, the low-grade heating loop loses all heating sources. To

serve the heating low-grade loop when the ice pad does not require cooling, the ice plant is required

to operate to ‘cool’ the geothermal loop thus providing heating to the low-grade loop. This imbalance

in cooling and heating loads between the ice rink and the low-grade loop and the lack direct storage

water volume on the low-grade heating loop results in additional energy use resulting from having to

constantly transfer energy to and from the geothermal loop via the ice plant compressors.

Based on the annual energy use of the ice plant, there is constantly an annual surplus of heat available

from the ice plant heat rejection to more than satisfy the heating load of the low-grade loop. It is

proposed to install a new storage tank on the low-grade loop sized to store all the heat rejection of

the ice plant during a resurfacing cycle in order to use the energy directly by the low-grade loop once

the ice plant shuts off. This would prevent the ice plant from having to constantly operate open to

the geothermal loop in order to satisfy the heating demand of the low-grade loop. The new storage

tank would have to be between 6,000 to 8,000 gallons in water volume capacity in order to store the

entire heat rejection of the ice plant during an ice resurfacing cycle. The new storage tank would be

insulated and installed outside by the existing cooling tower.

Impact on Maintenance

The addition of a storage tank will have marginal impact on the maintenance of the facility.

Impact on Indoor Environment

No impact.

Expected Service Life of Measure

Insulated Storage Tank: 30 years

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Assumptions

The following assumptions were applied:

• Existing heat rejected from the ice plant estimated at an annual average of 5,640,000 kBTU

• Existing annual average heating energy demand of the low-grade loop estimated at 1,875,000

kBTU

• Existing annual average percentage of the heating energy demand of the low-grade loop

provided directly by the heat rejected form the ice plant estimated at 28%.

• Existing ice plant energy required to provide heating demand for the low-grade loop during

times of no ice pad cooling demand estimated at 131,500 kWh annually.

• New annual average percentage of the heating energy demand of the low-grade loop provided

directly by the heat rejected form the ice plant with new storage tank estimated at 78%.

• New ice plant energy required to provide heating demand for the low-grade loop during times

of no ice pad cooling demand estimated at 39,500 kWh annually.

Impact on GHG Emissions

Reduction in ice plant energy will result in electrical consumption savings which will have a direct

impact on greenhouse gas emissions.

Cost & Savings Summary

Annual consumption savings: 108,929 kWh

Savings reconciled at:

Total implementation cost:

Simple payback:

$11,386

$230,000

20.2

years

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5.2.4 ECM B03: HEATING LOOPS PIPING MODIFICATIONS AND MERGING

Detailed Scope of Work

Currently, there are two (2) separate heating loops serving the facility. There is the low-grade heating

loop which is served by heat rejection of the ice plant and serves the air handling units heating and

in-floor heating and operates at 105°F. There is also the medium-grade heating loop which is served

by the Multistack chiller and serves pool heating, DHW preheat and perimeter heating and operates

at 135°F. Currently, energy sharing between the two loops in only achievable through the geothermal

loop system. Currently, there is continuously excess heat rejected from the low-grade loop to the

geothermal field, and simultaneously, the Multistack constantly operates to provide heat tot the

medium-grade loop via the geothermal field. This simultaneous heat rejection and extraction from

the geothermal field through pumping and compressor energy of the chillers and ice plant results in

additional energy.

As such, it is proposed to merge the two heating loops together to be able to take advantage of energy

sharing directly between the two loops without the use of the geothermal field and Multistack chiller.

It is proposed to convert the 135°F loop to 105°F and then directly connect the two low-grade loops.

This would minimize the use of the geothermal field and thus the use of the Multistack chiller. The

Multistack chiller would then primarily be used to provide cooling for the chilled water loops and

occasionally some heat to the low-grade loop only during peak heating periods.

This measure would include the replacement of the AHU-3 heating coil, and the pool water heating

heat exchangers to operate at 105F at design condition.

Impact on Maintenance

The reduction in yearly runtime for the Multistack chiller and associated pumps will prolong the useful

life of the equipment and will have a maintenance benefit for the building.

Impact on Indoor Environment

No impact

Expected Service Life of Measure

Piping & Insulation: 40 years

Controls devices: 15 years

Assumptions

The following assumptions were applied:

• Existing heat rejected from low-grade loop to geo-field estimated at an annual average of

2,500,000 kBTU

• Existing annual average heating energy demand of the medium-grade loop estimated at

2,760,000 kBTU

• Existing Multistack chiller energy required to provide heating demand for the medium-grade

loop estimated at 188,380 kWh annually.

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• New Multistack chiller energy required to provide heating demand for the medium-grade loop

after loop merging estimated at 78,280 kWh annually.

Impact on GHG Emissions

Reduction in Multistack chiller energy will result in electrical consumption savings which will have a

direct impact on greenhouse gas emissions.

Cost & Savings Summary

Annual consumption savings: 74,448 kWh

Savings reconciled at:

Total implementation cost:

Simple payback:

$7,782

$214,820

27.6

years

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5.2.5 ECM B04: AHU COILS FLUID REPLACEMENT AND ISOLATION

Detailed Scope of Work

The facility uses a number of separate water loops to provide heating and cooling for the building and

its process loads including two separate cooling loops for the ice pad and AHU cooling coils, two

heating loops for the in-floor heating, AHU heating coils and DHW and pool water heating, one heat

recovery loop which can tie in to any of the above-mentioned loops and a geothermal field loop. As

all the circulating loops are directly interconnected, the fluid medium are currently the same for all

loops and satisfy the most critical freezing protection scenarios of any of the loops. The current fluid

medium for the circulation loops is a mixture of 40% ethylene glycol which provides freeze protection

down to -23°C (-10°F) which can be encountered at the AHU coils during extreme cold days.

After the implementation of measure B01 - Ground Loop Fluid Replacement and Isolation, the

geothermal field would be isolated from the rest of the building loops. After the implementation of

measure B02 – Ice Plant Optimization and Storage tank, the ice pad cooling loop can be isolated from

the heat recovery loop as the ice plant would not require to ‘cool’ the geothermal loop to provide

heat to the low-grade loop. As such, having the geothermal loop and the ice pad cooling loops isolated

from the rest of the circulation loops, the only freeze protection remaining would be the water going

to the AHU coils.

It is recommended to isolate the AHU coil water from the remainder of the building by installing new

heat exchangers for each AHU coil and new coil circulation pumps. The AHU coil loops would utilize a

solution of 40% propylene glycol to provide freeze protection and the rest of the building loops (both

heating loops, the heat recovery loop and the chilled water loop) can now utilize water as the fluid

medium. Using water instead of the existing 40% ethylene glycol for the building loops will result in

significant pumping energy savings as water has far superior heat transfer properties and lower

viscosity than ethylene glycol.

Impact on Maintenance

The reduction of the amount of glycol anti-freeze within the building circulating loops will result in a

reduction to the maintenance of the building.

Impact on Indoor Environment

No impact.

Expected Service Life of Measure

Circulating Pumps 20 years

Heat Exchangers: 25 years

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Assumptions

The following assumptions were applied:

• Existing circulation pumps operating at annual average motor loads of 80% with 40% ethylene

glycol as fluid medium.

• New annual average motor loads for circulating pumps reduced by 20% with water as fluid

medium.

• Add new coils circulating pumps for the AHU coils; new 1 HP pump per coil.

Impact on GHG Emissions

Reduction in pumping energy will result in electrical consumption savings which will have a direct

impact on greenhouse gas emissions.

Cost & Savings Summary

Annual consumption savings: 69,694 kWh

Savings reconciled at:

Total implementation cost:

Simple payback:

$7,285

$92,000

12.6

years

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5.2.6 ECM B05: HIGH GRADE HEAT PUMP FOR DHW AND THERAPY POOL

Detailed Scope of Work

After implementation of measure B03 – Heating Loops Piping Modifications and Merging, all heating

loops would operate at 105°F which would not be hot enough to provide for the heating of the

domestic hot water and of the Therapy Pool. These heating loads would have to be provided by

electric DHW tanks and electric boiler respectively.

It is proposed to install a new high grade heat pump that would operate to produce 160°F water from

the 105°F loop which would serve the high grade loads of the building including the DHW heating and

the Therapy pool heating. The new heat pump would operate at a coefficient of performance (COP)

of 4 which would be four times more efficient than electric elements.

Impact on Maintenance

The addition of a new high grade heat pump and associated circulation pumps will add to the number

of systems within the facility and will result in an increase of maintenance requirement.

Impact on Indoor Environment

No impact

Expected Service Life of Measure

Piping & Insulation: 40 years

Controls devices: 15 years

High Grade Heat Pump: 20 years

Assumptions

The following assumptions were applied:

• Existing Therapy Pool estimated annual heating energy of 607,500 kBTU

• Existing DHW estimated annual heating energy of 467,000 kBTU

• Existing Therapy and DHW heating COP of 1.0

• Existing Therapy and DHW heating COP of 4.0

Impact on GHG Emissions

Reduction in total energy to heat DHW and therapy pool will result in electrical consumption savings

which will have a direct impact on greenhouse gas emissions.

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Cost & Savings Summary

Annual consumption savings:

Annual demand savings:

77,159

480

kWh

kW

Savings reconciled at:

Total implementation cost:

Simple payback:

$16,252

$195,500

12.0

years

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5.2.7 ECM C01: BAS OPTIMIZATION AND ANALYTICS

Detailed Scope of Work

Currently the facility is controlled by a combination of a Cimco DDC system controlling the ice plant

and a Building Automation System (BAS) controlling the space heating, air handlers and heating and

cooling pumps. The pool dehumidifiers has stand-alone digital controls.

It is proposed re-commission some of the sequences and to implement enhanced energy saving

strategies with the existing DDC systems. The strategy and changes proposed include:

• Enhanced time of day scheduling for air handlers;

• Re-commissioning of critical control devices including CO2 sensors, pressure sensors, damper

actuators, etc.

• Temperature reset based on demand for the chilled water and hot water loops.

• Ice temperature reset based on activity level.

MCW believes this proposed retrofit opportunity will require an automated method of identifying

whether the BAS is consistently controlling the systems optimally or per design conditions once the

site is retrofitted for a seasonal changeover. The goal will be to optimally utilize the infrastructure

and setup rules to ensure continued operation and optimization over the life of the assets. The BAS

performance is reliant on Operators visually analysing performance on the graphics, or via trend logs

or automated alarms where programmed. Practically, this approach is limited by the time Operators

can dedicate to constantly monitor the graphics to find situations where the BAS cannot meet the

design requirements. Trend logs and triggered alarms programmed into the BAS are intended to catch

excursions, but without proper insight into what events lead to excursions the programming is

iterative and costly.

Analytics will allow for optimal resets to occur to achieve the energy savings as outlined and also

notify the staff in the event the systems are not reacting as expected given the conditions.

MCW proposes that this measure utilize a Building Performance Monitoring & Analytics system to

optimize and maintain performance of the opportunity. The recommendation is to utilize a new

Cooper Tree data analytic platform.

Data collection is achieved through a physical or virtual device, depending on the situation. Physical

data acquisition devices, can be connected locally to the BAS with manual or automated uploads.

Alternatively, a virtual device can be created and connected to the BAS. The data is uploaded to cloud-

based software platform, aggregated into a single database, and analyzed with algorithms.

The software will offer automated application of pre-defined smart rules to the BAS information

captured from site. MCW will create fault detection and diagnostic (FDD) algorithms from a library of

insights to capture excursions in operations by the BAS or building equipment. The advent of ‘big-

data’ storage and automation allows for visibility of the entire BAS and connected equipment.

Predicted faults (performance excursions) include:

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• Systems that are commanded to be disabled, but are showing status due to starters being in

hand.

• Ongoing drift associated with the operation of a motor, whether its current is deviating from

normal levels.

• Whether speed is changing as a function of expected load (potentially indicative of poor set-

point or sensor placement).

• System input values that have not changed over hours, based on COV reporting (indicative of

faulty sensors).

• Execution of calibration routines to assess whether the mixed air dampers are holding shut

through temperature monitoring during full recirculation morning warm-up.

• Assessment of leaking valves through the application of differential temperature

measurement while valves are closed.

Impact on Maintenance

Building analytics is a method of identifying long-term trends to optimize energy usage and

implement fault detection diagnostics. A Data Acquisition Device (DAD) pulls up to 5000 data points

from the BAS, such as AHU supply air temperature, building return water temperature or valve

position, every 15 minutes and stores it on an internal hard drive and if enabled, uploads it to a secure

server. At this point, the analytics engine process this data into actionable insights which deliver

critical information identifying energy and maintenance savings opportunities. Initially showing up as

trends, this data provides significant insight into how the BAS systems are operating.

This information is served to users in a series of dashboards, reports and alerts to help users take

charge of their building performance. This insight allows for an in-depth view of how the building

HVAC systems operate and clearly outlines inefficiencies and highlights opportunities for improved

performances.

Impact on Indoor Environment

No impact.

Expected Service Life of Measure

Control components: 15 years

Assumptions

The following assumptions were applied:

• Existing BAS does not currently have any analytics capabilities.

• Network architectural can facilitate the installation of data analytics with minor adjustments.

Impact on GHG Emissions

Reduction in electrical energy related to this measure would have a direct impact on greenhouse gas

emissions.

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Cost & Savings Summary

Annual consumption savings: 99,045 kWh

Savings reconciled at:

Total implementation cost:

Simple payback:

$10,353

$46,000

4.4

years

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5.3 LONG TERM MEASURES (OUT)

5.3.1 ECM B06: RINK DEHUMIDIFICATION UPGRADE

Detailed Scope of Work

The arena seating area is equipped with 4 electric powered dehumidification units. These units are

set to maintain space conditions in the arena. The capacity of the installed units is significantly

deficient to provide the required dehumidification capacity for a fully occupied ice event in summer

design conditions.

It is proposed to install a new rink dehumidification unit to replace the four (4) existing electric

desiccant dehumidifiers. The new rink dehumidifier would provide the ventilation requirement for

the rink area, thus existing AHU-5 and AHU-6 air handlers would be re-balanced and re-duct to only

supply the change rooms Level 1 areas. The new dehumidification unit would have twice the

dehumidification capacity of the exiting dehumidifiers and would operate as a desiccant wheel,

however the new unit would utilize low-grade water from the existing 105°F loop for regeneration of

the desiccant wheel. There is currently an access of heat rejection from the plant that could be used

for regeneration.

Even though the new rink dehumidifier would be more efficient than the existing dehumidifiers, it

would still consume more energy than the existing system in order to properly dehumidify the space

and prevent fog build-up on the ice. This measure would have to be considered as an improvement

to the condition and comfort of the ice rink rather than an energy reducing measure.

Impact on Maintenance

The addition of a new rooftop rink dehumidifier to replace the existing four dehumidification will

result in an increase of maintenance requirement.

Impact on Indoor Environment

The new rink dehumidifier will have the capacity to properly dehumidify the rink area under a fully

occupied ice event even during the peak summer months.

Expected Service Life of Measure

Piping & Insulation: 40 years

Controls devices: 15 years

Rink Desiccant Dehumidifier AHU: 25 years

Assumptions

The following assumptions were applied:

• Existing Electric Desiccant dehumidification regeneration provided by electric coil at an

efficiency of 100%

• New Rink Desiccant Dehumidifier regeneration provided by low-grade heat from the ice plant

at a COP of 4

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• New Rink Desiccant Dehumidifier to provide ventilation for the ice rink and be sized for 10,000

cfm

• Existing AHU-5 unit to only serve Level 0 areas and be re-balanced

• Existing AHU-6 unit to only serve Level 0 areas and be re-balanced

Impact on GHG Emissions

This measure will result in an overall energy penalty which will have a direct impact on greenhouse

gas emissions.

Cost & Savings Summary

Annual consumption savings: (56,657)

(525)

kWh

kW

Savings reconciled at:

Total implementation cost:

Simple payback:

($14,876)

$690,000

-

years

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5.3.2 ECM D01: SOLAR PV INSTALLATION

Detailed Scope of Work

There is currently no solar generation onsite. Roof space is available for the installation of solar

photovoltaic panels.

Photovoltaic (PV) is the conversion of light into electricity. Solar Photovoltaic modules (panels)

generate electricity from the sun’s rays. Inverters are used to convert the Direct Current (DC)

electricity generated by Solar PV panels into Alternating Current (AC) electricity. Two types of

inverters are available for installation and have been compared in this report:

• String inverter with Solaredge technology optimization system

• Enphase micro-inverter based system

In general, Solar PV panels offer the following benefits:

• Low maintenance

• Long lifecycle

• Visibility for public awareness

• Silent operation

• Sustainable performance maintained at 80% over the system’s lifecycle

In order to harvest solar energy, individual solar panels must be arranged in an array and strategically

oriented for maximum solar exposure. In order to angle the array of panels to maximize exposure,

they must be mounted on a stable, durable racking system of sound structural integrity in order to

withstand wind, hail and corrosion over decades. A structural stand will tilt the PV array at a fixed

angle to obtain the highest annual solar energy harvest. PV arrays can be installed in a variety of

locations as the racking system and stand can be engineered to accommodate many different types

of footing. The most typical installations are rooftop mounted and ground mounted.

It is also important to understand that renewable energy production does not always follow the

facility’s energy demands. During a sunny weekend, the on-site energy generation may exceed the

building energy requirements In the case of this hospital, 50 kW of PV would be utilized and directly

synced into the building.

Impact on Maintenance

Impact on Indoor Environment

Expected Service Life of Measure

Solar photovoltaic equipment: 25 years

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Assumptions

The following assumptions were applied:

• Estimates for hours based on talks with building staff

• Existing optimal south facing exposure

• Proposed solar modules (panels) rated wattage: 351 Watts

• Proposed inverter/micro-inverter efficiency: 96%

Impact on GHG Emissions

Generation in electrical energy related to this measure would have a direct impact on greenhouse gas

emissions.

Cost & Savings Summary

Annual consumption savings: 53,000 kWh

Savings reconciled at:

Total implementation cost:

Simple payback:

$5,540

$172,500

31.1

years

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6 CONCLUSION

As part of their initiative to reduce energy consumption and the environmental footprint, the

Lunenburg County Lifestyle Centre commissioned MCW Maricor to conduct an energy study of the

facility.

Having conducted a site review and analyzed the existing systems, energy efficiency and conservation

measures (ECM) were developed which, if implemented, will provide both consumption and financial

savings in addition to reducing the environmental footprint of the facility.

The more attractive ECMs proposed result in an energy performance improvement project requiring

a capital investment of $1,024,248 and will reduce annual energy consumption by 574,524 kWh of

electricity consumption and 740 kW of electrical demand. This represents a financial savings of

$72,676 (based on current energy pricing) and a payback of 14.1 years, not including any incentives

and carbon reduction credits. It is our opinion that these measures be pursued in order to reduce

energy consumption and improve the overall performance of the facility.

Like many building owners and managers, the Lunenburg County Lifestyle Centre must now include

energy efficiency and conservation in the equation when making decisions on facility renewal and

operation. The implementation of this report should be considered as a stepping-stone towards a

continued focus on reducing energy consumption. This opportunity will allow the Lunenburg County

Lifestyle Centre to reap the financial and operational benefits of improved energy performance while

demonstrating leadership in environmental responsibility.

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APPENDIX A

LIGHTING RETROFIT

SUMMARY SHEET

(NOT USED)

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APPENDIX B

ENERGY UTILITY DATA

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Project Name: Lunenburg County Lifestyle Centre

Project Number: 10-20-039

94,280 sq.ft.

33.8 Total EUI

Utility Usage - Jan 2016 to Dec 2019 11M Elect. Rate Code

DateReading

Date

Billing

Days

Electrical

Consumption

(kWh)

Electrical

Demand

(kW)

Load

Factor

Water

(m3)

HDD @ 18°C

(Halifax)

Jan-16 1-28-16 31 262,080 603.8 0.58 556

Feb-16 2-24-16 27 249,600 639.4 0.60 508

Mar-16 3-29-16 34 295,680 647.0 0.56 2,018 530

Apr-16 4-27-16 29 240,960 654.7 0.53 445

May-16 5-30-16 33 250,560 570.2 0.55 308

Jun-16 6-28-16 29 150,720 264.8 0.82 1,600 179

Jul-16 7-27-16 29 151,680 350.4 0.62 48

Aug-16 8-26-16 30 283,200 679.7 0.58 3

Sep-16 9-28-16 33 381,120 715.2 0.67 1,552 44

Oct-16 10-27-16 29 330,240 702.7 0.68 169

Nov-16 11-25-16 29 311,040 710.4 0.63 302

Dec-16 12-28-16 33 295,680 623.0 0.60 2,136 497

Jan-17 1-26-17 29 262,080 611.5 0.62 638

Feb-17 2-23-17 28 248,640 648.0 0.57 607

Mar-17 3-28-17 33 312,000 606.7 0.65 1,931 648

Apr-17 4-25-17 28 251,520 667.2 0.56 399

May-17 5-26-17 31 257,280 611.5 0.57 274

Jun-17 6-27-17 32 191,040 420.5 0.59 1,471 120

Jul-17 7-27-17 30 170,880 409.0 0.58 43

Aug-17 8-28-17 32 270,720 679.7 0.52 36

Sep-17 9-26-17 29 299,520 653.8 0.66 1,686 62

Oct-17 10-26-17 30 298,560 642.2 0.65 170

Nov-17 11-27-17 32 291,840 629.8 0.60 389

Dec-17 12-22-17 25 221,760 573.1 0.64 2,195 602

Jan-18 1-29-18 38 335,040 567.4 0.65 672

Feb-18 2-28-18 30 269,760 631.7 0.59 538

Mar-18 3-27-18 27 251,520 592.3 0.66 547

Apr-18 4-26-18 30 253,440 590.4 0.60 430

May-18 5-30-18 34 256,320 601.9 0.52 250

Jun-18 6-26-18 27 143,040 335.0 0.66 166

Jul-18 7-26-18 30 187,200 412.8 0.63 24

Aug-18 8-27-18 32 299,520 667.2 0.58 14

Sep-18 9-26-18 30 318,720 666.2 0.66 80

Oct-18 10-26-18 30 303,360 640.3 0.66 278

Nov-18 11-27-18 32 309,120 624.0 0.65 449

Dec-18 12-24-18 27 255,360 623.0 0.63 648

Baseline

Jan/18-Dec/18 3,182,400 6,952 0

Year 2018 3,182,400 6,952 0

Year 2017 3,075,840 7,153 7,283

Year 2016 3,202,560 7,161 7,306

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APPENDIX C

ENERGY BALANCES

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Data Input Sheet - Existing

Project Name:

Building Name:

Date:

Name:

Building Information

Floor Area ft²: Heating Season Hours: Averaged OAT:

Area 94,280 ft² Hours 5,808 Hr Hours 37.0 °F

Schedule Hours: Temperature Setpoints: Heating Source:

Occupied 110.00 Hr/Wk Occupied 70.0 °F Code e

Unoccupied (NSB) 58.00 Hr/Wk Unoccupied (NSB) 70.0 °F

Type

Building Area Take-Offs: UA

Exterior Wall Gross 8,367 ft² Btu/Hr-F

Roof Gross 9,587 ft² Window 2.00 3,151

Window 6,301 ft² Door Glass 1.50 121

Door Glass 182 ft² Door Steel 2.70 8 9587 ft²

Door Steel 21 ft² O/H Door 4.20 0

O/H Door ft² Skylights 1.00 0

Interior wall gross ft² Interior Wall 4.00 0

Skylights ft² Wall 12.00 155

Wall Net 1,863 ft² Roof 25.00 383

Roof Net 9,587 ft² 1.00

Slab-on-Grade Perimeter ft

Total UA: 3,818

Energy Consumption - Skin Loss

Combustion Efficiency 420% Occupied 24,776 Kwh/Yr

System Efficiency 85% Unoccupied 13,064 Kwh/Yr Total: 37,840 Kwh/Yr

Energy Consumption - Infiltration Loss

Air Changes Occupied 0.100 Ventilated y

Air Changes Unoccupied 0.100 Volume Of Area 237,164 ft³

Infiltration Occupied CFM Occupied Hours With Vent Off 110.00 Hr/Wk

Inflitration Unoccupied CFM Unoccupied Hours With Vent Off 58.00 Hr/Wk

Occupied 4,397 Kwh/Yr

Unoccupied 2,318 Kwh/Yr Total: 6,715 Kwh/Yr

Schedule Hours: Temperature Setpoints: Heating Source:

Occupied 65.00 Hr/Wk Occupied 70.0 °F Code e

Unoccupied (NSB) 103.00 Hr/Wk Unoccupied (NSB) 70.0 °F

Type

Building Area Take-Offs: UA

Exterior Wall Gross 1,312 ft² Btu/Hr-F

Roof Gross 7,542 ft² Window 2.00 0

Window ft² Door Glass 1.50 0

Door Glass ft² Door Steel 2.70 0 7542 ft²

Door Steel ft² O/H Door 4.20 0

O/H Door ft² Skylights 1.00 0

Interior wall gross ft² 4.00

Skylights ft² Wall 12.00 109

Wall Net 1,312 ft² Roof 25.00 302

Roof Net 7,542 ft² 1.00

Slab-on-Grade Perimeter ft

Total UA: 411

Energy Consumption - Skin Loss

Combustion Efficiency 420% Occupied 1,576 Kwh/Yr

System Efficiency 85% Unoccupied 2,497 Kwh/Yr Total: 4,073 Kwh/Yr

Energy Consumption - Infiltration Loss

Air Changes Occupied 0.100 Ventilated y

Air Changes Unoccupied 0.100 Volume Of Area 120,672 ft³

Infiltration Occupied CFM Occupied Hours With Vent Off 65.00 Hr/Wk

Inflitration Unoccupied CFM Unoccupied Hours With Vent Off 103.00 Hr/Wk

Occupied 1,322 Kwh/Yr

Unoccupied 2,095 Kwh/Yr Total: 3,417 Kwh/Yr

Schedule Hours: Temperature Setpoints: Heating Source:

Occupied 168.00 Hr/Wk Occupied 82.0 °F Code e

Unoccupied (NSB) .00 Hr/Wk Unoccupied (NSB) 82.0 °F

Type

Building Area Take-Offs: UA

Exterior Wall Gross 5,367 ft² Btu/Hr-F

Roof Gross 9,996 ft² Window 2.00 641

Window 1,281 ft² Door Glass 1.50 0

Door Glass ft² Door Steel 2.70 0 9996 ft²

Door Steel ft² O/H Door 4.20 0

O/H Door ft² Skylights 1.00 0

Interior wall gross ft² Interior Wall 4.00 0

Skylights ft² Wall 12.00 341

Wall Net 4,086 ft² Roof 25.00 400

Roof Net 9,996 ft² 1.00

Slab-on-Grade Perimeter ft

Total UA: 1,381

Energy Consumption - Skin Loss

Combustion Efficiency 300% Occupied 26,124 Kwh/Yr

System Efficiency 85% Unoccupied 0 Kwh/Yr Total: 26,124 Kwh/Yr

Energy Consumption - Infiltration Loss

Air Changes Occupied 0.100 Ventilated y

Air Changes Unoccupied 0.100 Volume Of Area 219,912 ft³

Infiltration Occupied CFM Occupied Hours With Vent Off .00 Hr/Wk

Inflitration Unoccupied CFM Unoccupied Hours With Vent Off .00 Hr/Wk

Occupied 0 Kwh/Yr

Unoccupied 0 Kwh/Yr Total: 0 Kwh/Yr

Schedule Hours: Temperature Setpoints: Heating Source:

Occupied 65.00 Hr/Wk Occupied 70.0 °F Code e

Unoccupied (NSB) 103.00 Hr/Wk Unoccupied (NSB) 70.0 °F

Zone #4 - Library (AHU-4 & Heat Pumps)

Zone #3 - Pool (AHU-3)

Electrical

R Value

F-ft2-Hr/Btu Heat Loss Coefficient (Fp) of

Slab floor Construction:

Electrical

R Value

Heat Loss Coefficient (Fp) of

Slab floor Construction:0.60 Btu/h-ft-°F

Lunenburg County Lifestyle Centre Energy Study

Lunenburg County Lifestyle Centre

May 25, 2020

Emilie Landry

Zone #1 - Galleria (AHU-1)

Zone #2 - Admin, Change Rooms (AHU-2)

Zone Floor Area =

F-ft2-Hr/Btu

0.60 Btu/h-ft-°F

Zone Floor Area =

Zone Floor Area =

Electrical

R Value

F-ft2-Hr/Btu Heat Loss Coefficient (Fp) of

Slab floor Construction:0.60 Btu/h-ft-°F

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Type

Building Area Take-Offs: UA

Exterior Wall Gross 4,543 ft² Btu/Hr-F

Roof Gross 6,629 ft² Window 2.00 787

Window 1,573 ft² Door Glass 1.50 0

Door Glass ft² Door Steel 2.70 16 8698 ft²

Door Steel 42 ft² O/H Door 4.20 0

O/H Door ft² Skylights 1.00 0

Interior wall gross ft² Interior Wall 4.00 0

Skylights ft² Wall 12.00 244

Wall Net 2,928 ft² Roof 25.00 265

Roof Net 6,629 ft² 1.00

Slab-on-Grade Perimeter ft

Total UA: 1,311

Energy Consumption - Skin Loss

Combustion Efficiency 300% Occupied 7,039 Kwh/Yr

System Efficiency 85% Unoccupied 11,153 Kwh/Yr Total: 18,192 Kwh/Yr

Energy Consumption - Infiltration Loss

Air Changes Occupied 0.100 Ventilated y

Air Changes Unoccupied 0.100 Volume Of Area 139,168 ft³

Infiltration Occupied CFM Occupied Hours With Vent Off 65.00 Hr/Wk

Inflitration Unoccupied CFM Unoccupied Hours With Vent Off 103.00 Hr/Wk

Occupied 2,134 Kwh/Yr

Unoccupied 3,382 Kwh/Yr Total: 5,517 Kwh/Yr

Schedule Hours: Temperature Setpoints: Heating Source:

Occupied 110.00 Hr/Wk Occupied 65.0 °F Code e

Unoccupied (NSB) 58.00 Hr/Wk Unoccupied (NSB) 65.0 °F

Type

Building Area Take-Offs: UA

Exterior Wall Gross 1,420 ft² Btu/Hr-F

Roof Gross ft² Window 2.00 0

Window ft² Door Glass 1.50 0

Door Glass ft² Door Steel 2.70 23 24146 ft²

Door Steel 63 ft² O/H Door 4.20 31

O/H Door 130 ft² Skylights 1.00 0

Interior wall gross ft² 4.00

Skylights ft² Wall 12.00 102

Wall Net 1,227 ft² Roof 25.00 0

Roof Net ft² 1.00

Slab-on-Grade Perimeter ft

Total UA: 157

Energy Consumption - Skin Loss

Combustion Efficiency 420% Occupied 862 Kwh/Yr

System Efficiency 85% Unoccupied 454 Kwh/Yr Total: 1,316 Kwh/Yr

Energy Consumption - Infiltration Loss

Air Changes Occupied 0.100 Ventilated y

Air Changes Unoccupied 0.100 Volume Of Area 275,748 ft³

Infiltration Occupied CFM Occupied Hours With Vent Off 110.00 Hr/Wk

Inflitration Unoccupied CFM Unoccupied Hours With Vent Off 58.00 Hr/Wk

Occupied 4,338 Kwh/Yr

Unoccupied 2,287 Kwh/Yr Total: 6,625 Kwh/Yr

Schedule Hours: Temperature Setpoints: Heating Source:

Occupied 110.00 Hr/Wk Occupied 65.0 °F Code e

Unoccupied (NSB) 58.00 Hr/Wk Unoccupied (NSB) 65.0 °F

Type

Building Area Take-Offs: UA

Exterior Wall Gross 9,670 ft² Btu/Hr-F

Roof Gross 3,344 ft² Window 2.00 49

Window 98 ft² Door Glass 1.50 0

Door Glass ft² Door Steel 2.70 132 10764 ft²

Door Steel 357 ft² O/H Door 4.20 33

O/H Door 140 ft² Skylights 1.00 0

Interior wall gross ft² Interior Wall 4.00 0

Skylights ft² Wall 12.00 756

Wall Net 9,075 ft² Roof 25.00 134

Roof Net 3,344 ft² 1.00

Slab-on-Grade Perimeter ft

Total UA: 1,105

Energy Consumption - Skin Loss

Combustion Efficiency 420% Occupied 6,081 Kwh/Yr

System Efficiency 85% Unoccupied 3,206 Kwh/Yr Total: 9,288 Kwh/Yr

Energy Consumption - Infiltration Loss

Air Changes Occupied 0.100 Ventilated y

Air Changes Unoccupied 0.100 Volume Of Area 189,310 ft³

Infiltration Occupied CFM Occupied Hours With Vent Off .00 Hr/Wk

Inflitration Unoccupied CFM Unoccupied Hours With Vent Off 58.00 Hr/Wk

Occupied 0 Kwh/Yr

Unoccupied 1,570 Kwh/Yr Total: 1,570 Kwh/Yr

Schedule Hours: Temperature Setpoints: Heating Source:

Occupied 110.00 Hr/Wk Occupied 40.0 °F Code e

Unoccupied (NSB) 58.00 Hr/Wk Unoccupied (NSB) 40.0 °F

Type

Building Area Take-Offs: UA

Exterior Wall Gross 6,406 ft² Btu/Hr-F

Roof Gross 31,457 ft² Window 2.00 0

Window ft² Door Glass 1.50 0

Door Glass ft² Door Steel 2.70 0 19885 ft²

Door Steel ft² O/H Door 4.20 0

O/H Door ft² Skylights 1.00 0

Interior wall gross ft² 4.00

Skylights ft² Wall 12.00 534

Wall Net 6,406 ft² Roof 25.00 1,258

Roof Net 31,457 ft² 1.00

Slab-on-Grade Perimeter ft

Total UA: 1,792

Energy Consumption - Skin Loss

Combustion Efficiency 420% Occupied 1,057 Kwh/Yr

System Efficiency 85% Unoccupied 557 Kwh/Yr Total: 1,615 Kwh/Yr

Energy Consumption - Infiltration Loss

Electrical

R Value

F-ft2-Hr/Btu Heat Loss Coefficient (Fp) of

Slab floor Construction:0.60 Btu/h-ft-°F

Zone Floor Area =

Zone #5 - Rink Area - NE & SE Sides (AHU-5)

Electrical

R Value

F-ft2-Hr/Btu Heat Loss Coefficient (Fp) of

Slab floor Construction:0.60 Btu/h-ft-°F

Zone Floor Area =

Zone #6 - Rink Area - SW Side (AHU-6)

Electrical

R Value

F-ft2-Hr/Btu Heat Loss Coefficient (Fp) of

Slab floor Construction:0.60 Btu/h-ft-°F

Zone Floor Area =

Zone #7 - Rink (AHU-5 & AHU-6)

Electrical

R Value

F-ft2-Hr/Btu Heat Loss Coefficient (Fp) of

Slab floor Construction:0.60 Btu/h-ft-°F

Zone Floor Area =

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Air Changes Occupied 0.100 Ventilated y

Air Changes Unoccupied 0.100 Volume Of Area 437,470 ft³

Infiltration Occupied CFM Occupied Hours With Vent Off 110.00 Hr/Wk

Inflitration Unoccupied CFM Unoccupied Hours With Vent Off 58.00 Hr/Wk

Occupied 737 Kwh/Yr

Unoccupied 389 Kwh/Yr Total: 1,126 Kwh/Yr

Schedule Hours: Temperature Setpoints: Heating Source:

Occupied 65.00 Hr/Wk Occupied 70.0 °F Code e

Unoccupied (NSB) 103.00 Hr/Wk Unoccupied (NSB) 70.0 °F

Type

Building Area Take-Offs: UA

Exterior Wall Gross 2,758 ft² Btu/Hr-F

Roof Gross 3,662 ft² Window 2.00 328

Window 655 ft² Door Glass 1.50 14

Door Glass 21 ft² Door Steel 2.70 8 3662 ft²

Door Steel 21 ft² O/H Door 4.20 0

O/H Door ft² Skylights 1.00 0

Interior wall gross ft² Interior Wall 4.00 0

Skylights ft² Wall 12.00 172

Wall Net 2,061 ft² Roof 25.00 146

Roof Net 3,662 ft² 1.00

Slab-on-Grade Perimeter ft

Total UA: 668

Energy Consumption - Skin Loss

Combustion Efficiency 300% Occupied 3,583 Kwh/Yr

System Efficiency 85% Unoccupied 5,678 Kwh/Yr Total: 9,261 Kwh/Yr

Energy Consumption - Infiltration Loss

Air Changes Occupied 0.100 Ventilated y

Air Changes Unoccupied 0.100 Volume Of Area 58,592 ft³

Infiltration Occupied CFM Occupied Hours With Vent Off .00 Hr/Wk

Inflitration Unoccupied CFM Unoccupied Hours With Vent Off 103.00 Hr/Wk

Occupied 0 Kwh/Yr

Unoccupied 1,424 Kwh/Yr Total: 1,424 Kwh/Yr

Equipment Inventory

Domestic Hot Water Consumption - Zamboni

Combustion Efficiency 150% Days/Years 195

System Efficiency 90% DHW Temperature 160.0 °F Heat Recovery

Ice Floods/day 8 Heating Source Code e

Gallons/Floods 100 Heating Source Type Electrical Total: 33,844 Kwh/Yr

Domestic Hot Water Consumption - Arena

Combustion Efficiency 150% Days/Years 195

System Efficiency 85% DHW Temperature 140.0 °F Heat Recovery

Population 50 Heating Source Code e

Gallons/Person/Day 6 Heating Source Type Electrical Total: 11,198 Kwh/Yr

Domestic Hot Water Consumption - Pool

Combustion Efficiency 150% Days/Years 350

System Efficiency 85% DHW Temperature 140.0 °F Heat Recovery

Population 100 Heating Source Code e

Gallons/Person/Day 6 Heating Source Type Electrical Total: 40,199 Kwh/Yr

Domestic Hot Water Consumption -

Combustion Efficiency 150% Days/Years 260

System Efficiency 85% DHW Temperature 140.0 °F

Population 20 Heating Source Code e

Gallons/Person/Day 6 Heating Source Type Electrical Total: 5,972 Kwh/Yr

Miscellaneous Electrical Loads

Occupied .200 W/Ft² 94,280 ft² ft²

Unoccupied .025 W/Ft² Occupied 63,908 Kwh/yr

Hours per Week 65 Unoccupied 12,659 Kwh/yr Total: 76,567 Kwh/Yr

Play Pool Evaporative Cooling

Schedule Hours: Temperature Setpoints: See Table Heating Source:

Active Hours / Week 60.00 Hr/Wk Pool Space Setpoint 86.0 °F 0.068 Code e

Unoccupied Hours / Week 108.00 Hr/Wk Pool Water Setpoint 86.0 °F 0.054 Type

0.50

875 ft²

Energy Consumption - Evaporative Cooling

Evaporation Rate 397 Litre / Day

Combustion Efficiency 300% Active Hours 11,764 Kwh/Yr

System Efficiency 85% Unoccupied Hours 8,408 Kwh/Yr Total: 20,172 Kwh/Yr

Main Pool Hot Water Consumption

Combustion Efficiency 300% Days/Years 365

System Efficiency 85% DHW Temperature 86.0 °F io

Population 1 Heating Source Code e

Gallons/Person/Day 1105 Heating Source Type Electrical Total: 17,754 Kwh/Yr

Lap Pool Evaporative Cooling

Schedule Hours: Temperature Setpoints: See Table Heating Source:

Active Hours / Week 60.00 Hr/Wk Pool Space Setpoint 82.0 °F 0.052 Code e

Unoccupied Hours / Week 108.00 Hr/Wk Pool Water Setpoint 82.0 °F 0.038 Type

0.50

3320 ft²

Energy Consumption - Evaporative Cooling

Evaporation Rate 556 Litre / Day

Combustion Efficiency 300% Active Hours 34,133 Kwh/Yr

System Efficiency 85% Unoccupied Hours 22,449 Kwh/Yr Total: 56,582 Kwh/Yr

Electrical

Pool Surface Area =

Zone #8 - Offices (Heat Pumps & AHU-2)

Electrical

R Value

F-ft2-Hr/Btu Heat Loss Coefficient (Fp) of

Slab floor Construction:0.60 Btu/h-ft-°F

Electrical

Pool Surface Area =

Zone Floor Area =

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Main Pool Hot Water Consumption

Combustion Efficiency 300% Days/Years 365

System Efficiency 85% DHW Temperature 82.0 °F io

Population 1 Heating Source Code e

Gallons/Person/Day 2147 Heating Source Type Electrical Total: 31,502 Kwh/Yr

Therapy Pool Evaporative Cooling

Schedule Hours: Temperature Setpoints: See Table Heating Source:

Active Hours / Week 60.00 Hr/Wk Pool Space Setpoint 102.0 °F 0.148 Code e

Unoccupied Hours / Week 108.00 Hr/Wk Pool Water Setpoint 102.0 °F 0.134 Type

0.50

290 ft²

Energy Consumption - Evaporative Cooling

Evaporation Rate 151 Litre / Day

Combustion Efficiency 300% Active Hours 8,486 Kwh/Yr

System Efficiency 85% Unoccupied Hours 6,915 Kwh/Yr Total: 15,401 Kwh/Yr

Main Pool Hot Water Consumption

Combustion Efficiency 300% Days/Years 365

System Efficiency 85% DHW Temperature 102.0 °F io

Population 1 Heating Source Code e

Gallons/Person/Day 2040 Heating Source Type Electrical Total: 44,186 Kwh/Yr

Electrical Equipment Horsepower Table

Horsepower Phase Volts Motor Load %. Motor Eff. % Amps Hours

AHU-1 (SF) Galleria 10.00 3 575 80% 85% 5720 Total: 40,161 Kwh/Yr

AHU-1 (RF) 7.50 3 575 80% 85% 5720 Total: 30,121 Kwh/Yr

AHU-2 (SF) Admin & Pool, Change Rooms 5.00 3 575 80% 85% 3380 Total: 11,866 Kwh/Yr

AHU-2 (EF) 5.00 3 575 80% 85% 3380 Total: 11,866 Kwh/Yr

AHU-3 (SF) Pool 20.00 3 575 80% 85% 8760 Total: 123,011 Kwh/Yr

AHU-3 (EF) 2.00 3 575 80% 85% 8760 Total: 12,301 Kwh/Yr

AHU-4 (SF) Library 1.50 3 575 80% 85% 3380 Total: 3,560 Kwh/Yr

AHU-4 (EF) 1.00 3 575 80% 85% 3380 Total: 2,373 Kwh/Yr

AHU-5 (SF) Rink Area (NE & SE Sides) 5.00 3 575 80% 85% 5720 Total: 20,081 Kwh/Yr

AHU-5 (EF) 5.00 3 575 80% 85% 5720 Total: 20,081 Kwh/Yr

AHU-6 (SF) Rink Area (SW Side) 5.00 3 575 80% 85% 5720 Total: 20,081 Kwh/Yr

AHU-6 (EF) 5.00 3 575 80% 85% 5720 Total: 20,081 Kwh/Yr

EF-1 Rink Exhaust 5.00 3 575 80% 85% 500 Total: 1,755 Kwh/Yr

EF-2 Rink Exhaust 5.00 3 575 80% 85% 500 Total: 1,755 Kwh/Yr

EF-5 Elect. 110 Exhaust 0.75 3 575 80% 85% 2000 Total: 1,053 Kwh/Yr

EF-6 Recyc. & Gar. Rm. 112 0.25 1 120 80% 85% 2000 Total: 351 Kwh/Yr

EF-7 Loading 113 Exhaust 0.25 1 120 80% 85% 2000 Total: 351 Kwh/Yr

EF-8 Large Equip. Storage 114 Exhaust 0.25 1 120 80% 85% 2000 Total: 351 Kwh/Yr

EF-10 Elec. Rm 245A 0.25 1 120 80% 85% 2000 Total: 351 Kwh/Yr

EF-11 WRS 246, 247 Exhaust 0.05 1 120 80% 85% 3380 Total: 119 Kwh/Yr

EF-12 Elevator Machine Room Exhaust 0.08 1 120 80% 85% 2000 Total: 105 Kwh/Yr

EF-13 Ice Resur. Exhaust Room 122 0.33 1 120 80% 85% 2000 Total: 463 Kwh/Yr

EF-14 Male WC 205 Exhaust 0.25 1 120 80% 85% 3380 Total: 593 Kwh/Yr

EF-15 Female WC 206 Exhaust 0.25 1 120 80% 85% 3380 Total: 593 Kwh/Yr

EF-16 Library Elevator Machine Room 1520.08 1 120 80% 85% 2000 Total: 105 Kwh/Yr

EF-17 WR 155 Exhaust 0.10 1 120 80% 85% 3380 Total: 237 Kwh/Yr

EF-18 Female WC 204 Exhaust 0.25 1 120 80% 85% 3380 Total: 593 Kwh/Yr

EF-19 Electical Room 261 0.25 1 120 80% 85% 2000 Total: 351 Kwh/Yr

EF-21 Rink Maintenance Areas Exhaust 0.25 1 120 80% 85% 2000 Total: 351 Kwh/Yr

EF-22 North Concession Range Hood 0.04 1 120 80% 85% 2000 Total: 56 Kwh/Yr

RF-1 Refrig. 126 Vent. 0.75 3 575 80% 85% 2000 Total: 1,053 Kwh/Yr

RF-2 Mechanical 129 Vent. 0.75 3 575 80% 85% 2000 Total: 1,053 Kwh/Yr

RF-3 Pool Mech Vent. 0.75 3 575 80% 85% 2000 Total: 1,053 Kwh/Yr

SF-1 2.00 3 575 80% 85% 3380 Total: 4,746 Kwh/Yr

SF-2 2.00 3 575 80% 85% 3380 Total: 4,746 Kwh/Yr

SF-3 0.75 3 575 80% 85% 3380 Total: 1,780 Kwh/Yr

WWHP-1 100.00 3 575 80% 85% Total: - Kwh/Yr

WWHP-2 100.00 3 575 80% 85% Total: - Kwh/Yr

WWHP-3 100.00 3 575 80% 85% Total: - Kwh/Yr

Equipment Description

Electrical

Pool Surface Area =

Heat Pumps

Air Handling Units

Exhaust/Supply Fans

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P-2 Geothermal Loop Glycol Pump 15.00 3 575 80% 85% 8760 Total: 92,258 Kwh/Yr

P-3 Geothermal Loop Glycol Pump 15.00 3 575 80% 85% 0 Total: - Kwh/Yr

P-4 Heat Recovery Pump 7.50 3 575 80% 85% 8760 Total: 46,129 Kwh/Yr

P-5 Heat Recovery Pump 7.50 3 575 80% 85% 0 Total: - Kwh/Yr

P-6 Arena Warm Glycol Pump 2.00 3 575 80% 85% 6500 Total: 9,128 Kwh/Yr

P-11A Glycol Heating Primary Loop 10.00 3 575 80% 85% 7000 Total: 49,148 Kwh/Yr

P-11B Glycol Heating Primary Loop 10.00 3 575 80% 85% 0 Total: - Kwh/Yr

P-12A Glycol Heating Primary Loop 10.00 3 575 80% 85% 7000 Total: 49,148 Kwh/Yr

P-12B Glycol Heating Primary Loop 10.00 3 575 80% 85% 0 Total: - Kwh/Yr

P-13A Glycol Heating (MT) Loop 15.00 3 575 80% 85% 8760 Total: 92,258 Kwh/Yr

P-13B Glycol Heating (MT) Loop 15.00 3 575 80% 85% 0 Total: - Kwh/Yr

P-14A Glycol Heating (MT) Loop 15.00 3 575 80% 85% 6500 Total: 68,456 Kwh/Yr

P-14B Glycol Heating (MT) Loop 15.00 3 575 80% 85% 0 Total: - Kwh/Yr

P-15A Heat Pump Loop 7.50 3 575 80% 85% 8760 Total: 46,129 Kwh/Yr

P-15B Heat Pump Loop 7.50 3 575 80% 85% 0 Total: - Kwh/Yr

P-16 Heating LT/MT Injection Pump 1.00 3 575 80% 85% 0 Total: - Kwh/Yr

P-17 Glycol Cooling Secondary Pump 3.00 3 575 80% 85% 2200 Total: 4,634 Kwh/Yr

P-18 Heat Recovery to Play Pool 2.00 3 575 80% 85% 8760 Total: 12,301 Kwh/Yr

P-19 Heat Recovery to Lap Pool 3.00 3 575 80% 85% 8760 Total: 18,452 Kwh/Yr

P-20 Solar Panel Glycol Loop 0.40 1 120 80% 85% 8760 Total: 2,474 Kwh/Yr

P-21 Stand By Boiler Pump 1.00 1 120 80% 85% 0 Total: - Kwh/Yr

PREC1 Hot Water Circ. Pump 0.17 1 120 80% 85% 8760 Total: 1,025 Kwh/Yr

PPH1 Hot Water Circ. Pump 0.50 1 120 80% 85% 8760 Total: 3,075 Kwh/Yr

PPH2 Hot Water Circ. Pump 0.50 1 120 80% 85% 8760 Total: 3,075 Kwh/Yr

PP1 Indoor Lap Pool Filter Pump 25.00 3 575 80% 85% 8760 Total: 153,764 Kwh/Yr

PP2 Indoor Play Pool Filter Pump 7.50 3 575 80% 85% 8760 Total: 46,129 Kwh/Yr

PP3 Indoor Play Pool Toys Pump 0.50 3 575 80% 85% 800 Total: 281 Kwh/Yr

PP4 Indoor Therapy Pool Filter Pump 7.50 3 575 80% 85% 8760 Total: 46,129 Kwh/Yr

PP5 Indoor Therapy Pool Hydrojet Pump5.00 3 575 80% 85% 800 Total: 2,808 Kwh/Yr

AC no.1 Comms Rm 107 1.30 1 208 80% 85% 1500 Total: 1,369 Kwh/Yr

AC no.2 Comms Rm 264 1.30 1 208 80% 85% 1500 Total: 1,369 Kwh/Yr

CU-1 Comms Rm 107 1.30 1 208 80% 85% 1500 Total: 1,369 Kwh/Yr

CU-2 Comms Rm 264 1.30 1 208 80% 85% 1500 Total: 1,369 Kwh/Yr

Ice Plant Compressors 3 575 80% 90% From RETScreen Total: 562,500 Kwh/Yr

P-1A Arena Cold Floor Pump 15.00 3 575 80% 85% 4000 Total: 42,127 Kwh/Yr

P-1B Arena Cold Floor Pump 15.00 3 575 80% 85% 0 Total: - Kwh/Yr

P-7 Cooling Tower HE Glycol Pump 10.00 3 575 80% 85% 4000 Total: 28,085 Kwh/Yr

P-17 HP Cooling Pump 10.00 3 575 80% 85% 6000 Total: 42,127 Kwh/Yr

P-18 HP Glycol Pump 2.00 3 575 80% 85% 6000 Total: 8,425 Kwh/Yr

P-19 HP Cooling Pump 10.00 3 575 80% 85% 1000 Total: 7,021 Kwh/Yr

P-20 HP Glycol Pump 2.00 3 575 80% 85% 1000 Total: 1,404 Kwh/Yr

P-21 HP Cooling Pump 10.00 3 575 80% 85% 1000 Total: 7,021 Kwh/Yr

P-22 HP Glycol Pump 2.00 3 575 80% 85% 1000 Total: 1,404 Kwh/Yr

25.00 3 575 50% 85% 2050 Total: 22,490 Kwh/Yr

3 575 80% 85% Total: - Kwh/Yr

EB-1 Electric Boiler 1 144.83 3 575 80% 85% Total: - Kwh/Yr

HUM1 AHU4 Humidifier 20.52 3 575 80% 85% 500 Total: 7,203 Kwh/Yr

HWT1 Electric DW Booster Tank 100.58 3 575 80% 85% Total: - Kwh/Yr

HWT2 Electric DW Booster Tank 100.58 3 575 80% 85% Total: - Kwh/Yr

HWT4 Electric DW Booster Tank 16.09 3 575 80% 85% Total: - Kwh/Yr

HWT5 Electric DW Booster Tank 16.09 3 575 80% 85% Total: - Kwh/Yr

HWT6 Electric DW Booster Tank 8.05 3 575 80% 85% Total: - Kwh/Yr

HWT7 Electric DW Booster Tank 8.05 3 575 80% 85% Total: - Kwh/Yr

DU1 Dehumidifier 1 16.09 3 575 80% 85% 3000 Total: 33,895 Kwh/Yr

DU2 Dehumidifier 2 16.09 3 575 80% 85% 3000 Total: 33,895 Kwh/Yr

DU3 Dehumidifier 3 16.09 3 575 80% 85% 3000 Total: 33,895 Kwh/Yr

DU4 Dehumidifier 4 16.09 3 575 80% 85% 3000 Total: 33,895 Kwh/Yr

80% 85% Total: - Kwh/Yr

Electrical Equipment Amps Table

Factor: 1.5

Amps Phase Volts Power Factor Hours

To add new measure Ctrl+Shift+KHP-1 Cooling 21.5 3 208 80% 350 From HAP Total: 3,249 Kwh/Yr

To add new measure Ctrl+Shift+KHP-2 Cooling 10.7 1 208 80% 200 From HAP Total: 534 Kwh/Yr

To add new measure Ctrl+Shift+KHP-3 Cooling 10.7 1 208 80% 350 From HAP Total: 935 Kwh/Yr

To add new measure Ctrl+Shift+KHP-4 Cooling 9.2 3 575 80% 350 From HAP Total: 3,844 Kwh/Yr

To add new measure Ctrl+Shift+KHP-5 Cooling 10.7 3 575 80% 300 From HAP Total: 3,832 Kwh/Yr

To add new measure Ctrl+Shift+KHP-6 Cooling 13.2 3 208 80% 400 From HAP Total: 2,280 Kwh/Yr

To add new measure Ctrl+Shift+KHP-7 Cooling 10.7 1 208 80% 250 From HAP Total: 668 Kwh/Yr

To add new measure Ctrl+Shift+KHP-12 Cooling 12.9 1 208 80% 100 From HAP Total: 322 Kwh/Yr

To add new measure Ctrl+Shift+KHP-14 Cooling 12.9 1 208 80% 600 From HAP Total: 1,932 Kwh/Yr

To add new measure Ctrl+Shift+KHP-15 Cooling 17.4 1 208 80% 350 From HAP Total: 1,520 Kwh/Yr

To add new measure Ctrl+Shift+KHP-16 Cooling 17.4 1 208 80% 125 From HAP Total: 543 Kwh/Yr

To add new measure Ctrl+Shift+KHP-17 Cooling 9.2 3 575 80% 300 From HAP Total: 3,295 Kwh/Yr

To add new measure Ctrl+Shift+KHP-18 Cooling 17.4 1 208 80% 300 From HAP Total: 1,303 Kwh/Yr

Ventillation Systems

CFM % Outdoor Air % Heat Recovery System Eff. Combustion Eff. Occupied Temp Hours/Week Code Heating Type

To add new measure Ctrl+Shift+Z 8,522 CFM 30% 0% 85% 300% 70.0 °F 110 Hr/Wk e Electrical Total: 39,816 Kwh/Yr

To add new measure Ctrl+Shift+Z 5,003 CFM 100% 60% 85% 300% 70.0 °F 65 Hr/Wk e Electrical Total: 18,416 Kwh/Yr

To add new measure Ctrl+Shift+Z 23,066 CFM 15% 0% 85% 420% 82.0 °F 168 Hr/Wk e Electrical Total: 80,152 Kwh/Yr

To add new measure Ctrl+Shift+Z 1,406 CFM 100% 60% 85% 300% 70.0 °F 65 Hr/Wk e Electrical Total: 5,174 Kwh/Yr

To add new measure Ctrl+Shift+Z 5,003 CFM 100% 60% 85% 300% 65.0 °F 110 Hr/Wk e Electrical Total: 26,444 Kwh/Yr

To add new measure Ctrl+Shift+Z 5,003 CFM 100% 60% 85% 300% 65.0 °F 110 Hr/Wk e Electrical Total: 26,444 Kwh/Yr

Building Lighting

Lighting -

3.18 kW-h/yr-sq.ft. Total Lighting Consumption: 300,000 Kwh/Yr

Total Heating - Lighting Heating Contribution: 100%

Building Summary

Total:

Electrical 2,965,399 Kwh/Yr Propane 0 PL/Yr

Oil # 2 0 #2L/Yr Natural Gas 0 GJ/Yr

Oil # 6 0 #6L/Yr Steam 0 Lbs/Yr

Heat Pumps

AHU-1 SF

Cooling Tower Fan

AHU-2 SF

AHU-3 SF

AHU-6 SF

Equipment Description

Pool Pumps

Heating/Cooling Pumps

Equipment Description

AHU-4 SF

AHU-5 SF

Misc.

Ice Plant

Cooling

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Page 77: Engineering Services for Energy Reduction Upgrades · 2020. 9. 4. · RFP2020-02 Engineering Services for Energy Reduction SEPTEMBER 2020 3 1.0 INTRODUCTION 1.1 OVERVIEW As part of

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