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ThermaTran Information Booklet 2017

TABLE OF CONTENTS

ITEM 0 - INTRODUCTION 2 PGS. ITEM 1 – REED MELTON’S RESUME 5 PGS. ITEM 2 – FIRE HEATER QUALIFICATIONS 5 PGS. ITEM 3 – DELAYED COKER CHARGE HEATER EXPERIENCE 2 PGS. ITEM 4 – EXPERIENCE IN MAJOR FIRED HEATERS AT RADCO, INC. 15 PGS. PART 1 – MAJOR RESPONSIBILITIES PART 2 – SPREAD SHEET BY RADCO JOB NO. ITEM 5 – THERMATRAN’S QUALITY ASSURANCE & PROJECT MANAGEMENT 18 PGS. ITEM 6 – PHOTOS OF TYPICAL THERMATRAN FIRED HEATERS 26 PGS.

New and/ or revamped Process Fired Heaters, Plant Heater Studies, Improved Throughput, Fuel Efficiency, Emissions Improvement, Combustion Systems and Spare Parts

ThermaTran, INC 8721 South 65th East Place Tulsa, Oklahoma 74133-5072 October 3, 2016 Attention: All Oil Refinery, Chemical Plant and Natural Gas Plant process engineers and capital project managers. Reference: Informational letter to any of the above noted personnel ThermaTran Reference: Introduction to ThermaTran, INC Dear Current or Future Customer: We are pleased to present an informational document to introduce you and your company to ThermaTran, INC. and a discussion as to our capabilities to Design, Document, Generate all necessary drawings for, Purchase materials for, Fabricate and Assemble, Ship, and Erect Process Fired Heaters built to API Standard 560. We can also perform all of the proceeding items in executing field modification and modernization of existing heaters in the refinery or gas processing plant or Petrochemical plant in which the heater is installed. To accomplish this we will provide the following items: 1) My Personal Resume of 48 years of fired heater experience. 2) Our Company’s Qualifications to provide New and Revamped Process Fired Heaters. 3) Delayed Coker Charge Heater Experience 4) A list of the Process Fired Heaters, I have had a major responsibility for, in those 48 years. 5) ThermaTran’s Quality Assurance & Project Management Procedure. 6) Typical pictures of different heater designs Reed Melton was responsible for. 7) We also do special heater studies to show our customers how their current heater is operating

and how to achieve an increased capability to produce a higher throughput or a higher outlet temperature or both may be achieved and at the same time providing equal or improved emissions and thermal efficiency.

ThermaTran utilizes quality subcontractors for a great deal of our work. These contractors include Mechanical / Structural Engineers, General Arrangement and Shipping Clearance CADD Designers, Detail Fabrication and Erection CADD Designers, Field Expediters and Inspectors, Tulsa Area Fabricators and their Subcontractors for major portions of the project work. There is a rich selection of these subcontractors in the Tulsa area and if necessary outside of the Tulsa area. An example of the latter group is our very experienced metallurgist. The above mentioned items provide a good documentation of our ability to resolve your current problems and / or potential need for new API Standard 560 design fired process heaters and related equipment or field modification and improvement of same.

New Introductory letter to ThermaTran, Inc. Former and Potential New Customers and Fabrication Shops

September 21, 2016

2

This would include: 1. Proposals for providing the equipment your group may request a quotation for in an inquiry

to us. 2. Proposals for field modifications to existing fired heaters in your existing plants. 3. Spare parts proposals for domestic and / or foreign fired heaters. 4. Paid studies of current problems with:

a. Your existing fired heater equipment b. Current emissions problems c. Desire for increased unit throughput, increased outlet temperatures, and or new

heater charge characteristics. d. Desire for providing new equipment that requires fewer decoking operations per

processing year. e. Better coil material to resolve current corrosion problems. f. Any other fired heater related problems with:

i. Coil hot spots. ii. Burner flame impingement on the process coil or internal tube supports.

iii. Explosions or major puffing of the heater fire box area. iv. Fuel skid control problems and other instrumentation problems. v. Structural Problems.

vi. Additional Convection Section for waste heat recovery as boiler feed water, steam generation coil and / or superheated steam.

vii. Fired heaters in extreme cold climate or high altitude We trust that we may be favored with future fired heater inquires and hopefully purchase orders. Our intent is to create repeat customer relationships and we sincerely look forward to working with you and your employees to resolve any needs you may have in the type API 560 fired heater field in the near future. Best Regards, ____________________________ Reed T. Melton President ThermaTran, Inc. 8721 South 65th East Place Tulsa, OK 74133-5072 Phone: 918-748-4406 Cell: 918-381-5696 E-Mail: [email protected] cc: Carol Melton Enclosures: New Customer Introduction to ThermaTran and support documents.

Item 1

Reed Melton Personal Resume

5 Sheets

Reed T. Melton President – ThermaTran, Inc.

August 30, 2016 Qualification Summary: Forty eight years of proven experience in design of various types of heat transfer

equipment, project management, production management, and various aspects of business development. Experience pertains to oil production and refinery related work. Extensive experience in computer applications of engineering design. Extensive knowledge of metallurgy, corrosion, fluid flow and heat transfer, fluid flow calculations in single or two-phase flow. PVT type calculations.

Understanding of the function of most major refinery units and their relation to the whole

refinery and other units in the refinery, natural gas plants and chemical plants. Major teaching experience with young engineers. Generated and presented several

Incinerator/ Fired Heater Schools. Substantial presentation experience. Major sales background both US and International. Overseas negotiating and engineering experience in Korea, Thailand, Venezuela, Saudi Arabia, Kuwait, Mexico, Canada and Taiwan.

College: University of Tulsa 1968/ BS - Chemical Engineering and BS - Engineering Mathematics Personal Details: US Citizen, Age 71, Married, Two (2) adult children both away from home. Organizations: Formerly member of AIChE local and national; OSPE; NSPE; API and NPRA. Member

and former Chair - Chemical Engineering Department – Industrial Advisory Board, University of Tulsa.

Experience: ThermaTran Inc. – Tulsa, OK / President and CEO and Owner March 9, 2012- Present ThermaTran was founded in June of 2000. See before Thermal Process Engineering Various Engineering Projects for Refining, Natural Gas Plants and Oil and Gas

Production Facilities Thermal Process Engineering, Inc. – Tulsa, Oklahoma (TPE) 2004-March 2012

• During my time at TPE, I worked on and sold many projects representing the bulk of TPE’s work and income during that period. Several projects come to mind:

• 2011 o Received P.O. for a new Double Fired Vacuum Heater – Cross Refining &

Marketing – Smackover, AR Received Order – 4/14/2012 Added numerous change orders as well as a P.O. for oversight of the

Vacuum Transfer Line Design. Shipped Unit February 27-29 and March 5, 2012

Now preparing for erection of unit in Mid April 2012 and Start up in early May 2012.

• 2010 o Received Phase II P.O. for the Coker Charge Heaters – Hunt Refining,

Tuscaloosa, AL Completed all items in 2010 o Received P.O. for new convection box for main Crude Heater – American

Refining Group – Bradford, PA. Included new Retractable Soot Blowers with local start buttons and Control Panel Order Date October 20, 2010 During the project we received a substantial amount for additional

engineering of the lift and replacement of several of the items not in the original order.

Shipped the order late in March of 2011. • 2008-2009

o Proposed and sold a revamp of the primary Crude Heater at Hunt Refining at Tuscaloosa, AL. Project start May 5, 2008 and Project completion was April 21, 2009 with successful restart of the refurbished heater. Items accomplished: New Radiant Section Refractory New Radiant Section Castable New Radiant Section Tube Supports New Radiant Section Coil Material New Low NOx Side Fired Burners. New Convection Section Tube Supports New Convection Section Coil Material including replacing the steam

generator coil with new process coil New Flue Gas Stack Erection oversight and Start up instruction and assistance

o Proposed and Sold Phase I of the Coker Charge Heater Revamp and Coker Pre Heater conversion to Coker Charge heater. Coker Charge Heater included

• New Low NOx burners Coker Preheater conversion to Coker Charge Heater New Radiant Coil Material 347 SS New Convection Section Boiler and BFW coil material – A-106B New Low NOx burners

o Both Heaters Erection Oversight Start Up instruction and assistance

o Proposed and Sold Study of 6 x 120 MMBtu/ hr Forced Draft Heaters with multifuel forced draft burners. For BP Alaska, May to December 2008. Attended off shore location ¼ Mi. off shore of North Slope of Alaska Met with and discussed heater operation with all available

operational personnel.

Visited and reviewed actual units inside a large partially submerged barge.

Collected all available data, drawings and documents on the original 1982 equipment.

Wrote a multipage report of the visit and conferences with numerous recommendations.

Received an additional purchase order for estimated pricing of the project. Responded with an approximate $ 20+ million project over six to eight months.

o Proposed and received a Purchase Order for review of the process and mechanical design of the transfer lines of two large Vacuum Charge Heaters at BP Texas City, TX refinery and Pipe Still 3A. Completed the project under budget and on time.

• 2007 o Started Work on a single Fired Coker Heater Evaluation for CoP at Japan

Energy, Mizushima Refinery. Included were Several teleconference calls from Ponca City, OK to Japan.

o Made new proposal, including material, labor, engineering and erection costs to the contractor for Hunt Refining, Al for modernization of their crude heater.

o Sold two Platformer Interheaters to Louisiana Refinery. o Sold a Design and Cost Estimate Proposal for a remote unmanned Turbine

Exhaust Heat Recovery System using a Hydrocarbon Working Fluid for a major supplier of this type of equipment.

• 2006 o Completed the Coker Charge Heater Study for CoP at PetroBras in Southern

Brazil. This study included Detailed API Spec Sheets in English and Metric Units of the Coker

Charge Heaters. Substantially Complete General Arrangement Drawings for the

Coker Charge Heaters with Balanced Draft Air Preheat Units. CFD Studies of both the Fired Heaters and the Flue Gas and

Combustion Air Ducts. Complete Mechanical and Process Design of the subject heaters. Complete evaluation of P & ID Drawings supplied to us with our

provision of set points and alarm points and shutdown points for all major control signals.

o Did initial proposal to Hunt Refining, Tuscaloosa, Al for modernization of their crude heater.

• 2004-2005 o A complete refinery study of Western Refining’s El Paso Plant as to NOx and

CO output and fuels efficiency and options for increased throughput, greater efficiency and lower NOx on every heater and boiler in the plant. This also included generating forms on each item for Western’s use in negotiating with the Texas Air Control Board and also the Regional EPA office for the El Paso

area. This discussion was successful in the months after we published our study.

o Made a study of another heater company’s double fired Coker Charge Heaters (2) at ConocoPhillips (CoP) Sweeny, TX Plant. Finished the study and proposed several alternate modifications with budgetary pricing and major operating cost savings in October of 2005.

o Generated a study proposal for evaluation of the Coker Charge Heaters at CoP’s Alliance Refinery at Belle Chase, LA. This was not followed up by CoP due to the impact of Hurricane Katrina around the same time.

o Proposed the scope of supply and pricing in late 2005 and sold in early 2006 an engineering project for a new set of Double Fired Coker Charge Heaters for PetroBras in Southern Brazil.

ThermaTran Inc. – Tulsa, OK / President and CEO and Owner 2000-Present ArrTech Environmental Systems. Inc. - Tulsa, OK / President, CEO and Principal Owner 1993-

2000 • Design and Project Management heat transfer, combustion, incineration and heat recovery units

including: Fume & Liquid Incinerators, Direct Fired Air Heaters, Direct Fired Process Heaters, Indirect Air Heaters and other Combustion and Heat Transfer Equipment.

• Experience in combustion emission knowledge and how to control same. • Metallurgy experience in specific materials for specific services and processes. Extensive

knowledge of service specific corrosion erosion problems. Knowledge of material testing, metallurgical - lab test and PMI, Refractory Testing - lab and shop test.

• Knowledge of structural design as relates to heater frame, stack, cast and plate tube supports and foundation loads

• ASME CODE (I & VIII), ASTM Standards, ANSI, AISI, AISC, NFPA, NEC, FM, IRI, API. Radco, Inc. - Tulsa, Oklahoma / Executive Vice President 1973 - 1993 • Extensive background in the design of Oil Refinery Heaters including: Crude Oil, Vacuum

Crude, Hydrotreater, Hydrocracker, Heat Medium, Natural Gas Regen Gas, Ethylene Cracking, Delayed Coker Charge heaters, Naphtha Reformer Heaters (CCR Platformer), Reboilers, and more. Petrochem - Acetic Acid Cracking Heaters. Experience in all design phases - Coil, Burners, Refractory, Structure, Tube Support, etc.

• Manager of Design Engineering, Project Management, Purchasing, and Production. All phases of Process Fired Heater Design, Fabrication, Installation, Operation as well as sales

• Manage Job Schedule Systems, Fabrication Status Reports and several other Management Information Systems. Managed approximately 40 people.

• Handle major client relations for ongoing projects. Participation in several API committees (see below).

1986 - 1991 • Generation and presentation of several Radco, Inc. Fired Heaters Schools. • Negotiation of and establishment of Radco, Inc. Incinerator Division. • Negotiation of and establishment of CetCon environmental testing division of Radco, Inc. • Responsible for record sales in 1990 of $ 32,500,000 • Participated in several different API fired heater committees including: Recommended Practice for design of Heat Recovery Steam Generator, Refractory and Blower

addendums to API Standard 560 - Design and Construction of General Purpose Refinery Fired

Heaters and Design stresses for return bend thickness calculation API Recommended Practice - 530.

• Responsible for sale of Radco's first Ethylene Cracking heater. • Development of new marketing tools such as brochures, diagrams, etc. • Responsible for filing of and pursuit of patent for double fired coker heater.

1980 - 1985 • Primary thermal design engineer and salesman. Management of the company. Computer

programming. • Hiring of new data processing head and selection of corporate new data processing system. • Chaired Stockholder and Board of Directors meetings. Dealt with legal consul. Several API

committees. Thermal Design Engineer. 1973 - 1980

• Thermal design, sales and generation of data sheets for fired process heaters. Initial project management for the fabrication and shipment of process fired heaters.

• Generate procedures for and write computer programs for numerous technical and cost estimation programs relating to fired process heaters. Maintain and document programs. Select and provide for purchase of and maintenance of data processing equipment.

• Participated in several API committees. Served as Chairman of Tulsa Section of AIChE. ConRad - Tulsa, Oklahoma/ Thermal Design Engineer. 1972 - 1973

• Thermal Design and data sheet generation of Shell & Tube and Air Cooled exchangers and tank heaters.

• Maintenance and documentation of existing thermal design, mechanical design, cost estimate and commercial programs. Programmed in FORTRAN IV and COBOL.

Econo-Therm Corporation - Tulsa, Oklahoma / Head of Data Processing 1969 - 1972 • Maintained and modified existing computer software. Generated new procedures for and

coded various technical computer programs that provide mathematical models of all styles of fired heaters. Integrate combustion calculations with process models such as two phase pressure drop calculations. Write programs in FORTRAN and documented all programs.

• Select and oversee purchase and maintenance of data processing equipment. Hire and train employees.

Dale L. Gulley and Assoc. - Tulsa, Oklahoma / Thermal Design Engineer and Programmer 1968 - 1969 • Thermal Design of Heat Exchangers, Mechanical Design of Shell and Tube Exchangers,

preparation of data sheets, design and write Thermal and Mechanical Design computer programs FORTRAN, major modification of HTRI Shell and Tube Exchanger design program for pull-through floating head exchangers.

Item 2

ThermaTran’s Qualifications for all phases of Fired Heater

Design and Supply and Support of a Fully Operating Process Fired Heater per

API Standard 560 – Fired Heaters for General Refinery Service

5 Sheets


ThermaTran, Inc. 8721 South 65th East Place Tulsa, Oklahoma 74133 August 30, 2016 Prospective Customers Attention: To whom it may concern Reference: ThermaTran, Inc. (TTI) qualifications for Fired Heater Design and Supply. ThermaTran Ref.: Same Dear Prospective Customer:

This document covers our capabilities for providing priced proposals for new fired heater services and modifications to existing units, spare parts for our heaters and the complete line of Radco heaters, or engineering studies as required by the project (s) you may be working on. I am also attaching my updated resume for your information.

ThermaTran represents over forty four years of heater experience. ThermaTran is my company and I bring all of my experience at TPE, Radco and Econo-Therm with me. TPE was a successor company to Radco, Inc. which sold fired heaters during the 1970’s, 80’s and 90’s. In turn, Radco was a successor company to Econo-Therm, Inc. which did business in the 1960’s and the early 70’s. My brother (now deceased) and I were deeply involved in all three of these companies. Our website (www.thermatran.com) includes lists of past heater experience for each of the several types of heaters discussed in that site. Below is a detailed description of our qualifications for this type of work and supply. TYPES OF HEATERS: In our long background in fired heaters, we have been involved in the following types of heaters: A. Oil Refinery Crude Oil Heaters - 5 MMBtu/Hr - 430 MMBtu/Hr B. Oil Refinery Vacuum Crude Heaters - 4 MMBtu/Hr - 120 MMBtu/Hr C. Oil Refinery, Chemical Plant and Natural Gas Plant reboiler heaters of all sizes and types.

5 MMBtu/Hr - 120 MMBtu/Hr D. Oil Refinery Hydrotreater Heaters - 15 to 35 MMBtu/Hr E. Oil Refinery Hydrocracker Heaters. - 15 to 35 MMBtu/Hr F. Numerous Delayed Coker Charge Heaters – all sizes G. Hot Oil Loop Heaters - 15 MMBtu/Hr - 215 MMBtu/Hr H. Natural Gas Plant Regeneration Gas Heaters - 3 to 30 MMBtu/Hr

I. Chem. Plant - Ethylene Cracking Heaters. - 4 @ 72 MMBtu/Hr

http://www.thermatran.com/

General Refinery, Chemical Plant and Natural Gas Plant Fired Heater Design Qualifications ThermaTran, Inc.

Prospective Customers of ThermaTran, Inc. Page 2, August 30, 2016


J. Various Fired Reboiler Heaters, Desalter Feed Heaters, and many more plus BFW heating coils, Steam Super Heater Coils, Steam Generation Coils and specific process service convection coils.

DELAYED COKER CHARGE HEATER DESIGN – THERMATRAN provides the finest model of the behavior inside the Coker Charge Heater coil during operation. This program came as a result of development we did in the 1980’s in preparation for our first double fired coker heater design. This was our flagship unit at Amoco Whiting. Further development continued on into the early 90’s and peaked with our landmark design of the coker heaters at Star (now Motiva) Refinery at Port Arthur, Texas in the early 90’s. These heaters held the record for the longest continuous service between de-cokings of about seven (7) years. We can and also have engineered the conversion of former single fired coker charge heaters to the double fired design. Additionally, our engineering expertise includes numerous SCR Units and Combustion Air Preheat Systems as well as control packages and fuel skids. OTHER ITEMS PROVIDED BY ThermaTran: Our experience includes, but is not limited to, the above heater list and covers world wide applications. DESIGN AND CONSTRUCTION MILESTONES: Between these three companies, Econo-Therm, Radco and TPE, well over 1,500 heaters were designed and sold and many other service and / or spare parts jobs were completed. A few highlights of this history are:

1. The first UOP designed inverted wicket heater for Coastal States Refinery at Corpus Christi Refinery.

2. The first wicket type Catalytic Reformer Charge / Inter-heaters for several oil companies including Amoco.

3. Major heater projects up to 500 MMBtu/ hour during the three companies’ existence (1961-1998).

4. Business History in all major oil markets in the world. 5. Some of the first fired heater projects on the North Slope. 6. Double fired Platformer Charge/ Interheaters and Hydro-Cracker Charge Heaters Vacuum Feed

heaters. 7. The first double fired Delayed Coker Charge Heater at Amoco Whiting in 1988. This heater

ultimately led to a patent of that design and to this day have been licensed worldwide. SOFTWARE: We have developed the finest suite of fired heater design and evaluation software in

the business. Some examples are:

1. Heater Combustion and Flue Gas Calculations




A. Both Horizontal Cabin and Vertical Cylindrical designs with the best correlations available. Also both Single and Double Fired Designs are provided for.

B. Double Fired Vertical and Horizontal Tube designs for Chemical and Petroleum Reactor Heaters. We also modeled Wicket Heater Coils and Vertical Harp Coils for Naphtha Reforming services.

C. All convection designs for heat recovery work and forced circulation heat recovery boiler coils.

D. Helical Coil Designs for Specialty Vertical Cylindrical Heaters. E. Various other design options cover virtually all types of Refinery Services. All of the above programs are available in an all-radiant version and a radiant-convection type design basis for the primary process. Also either design basis will accommodate one or multiple different services in the convection section. F. Flue Gas Program: This program does the combustion calculation(s) for multiple

fuels in one or multiple heaters with or without additive heat recovery and with or without Air Preheat. Additionally specialty air streams such as turbine exhaust(s) or pure O2 streams can be utilized.

Up to seven heaters can be combined for a single exhaust point and up to three different fuels may be used in the each heater and the combustion air stream for each fuel stream may be air preheated or not on a selective basis. Fuel options are:

i. Natural Gas model requiring only a mol weight and LHV value. ii. Refinery Gas model requiring only a mol weight and LHV value. iii. Refinery Fuel Oil requiring only a Degee API and LHV value. Atomization

Steam or air is provided for. iv. A defined gas mixture such as would be available from a chromatograph

output.

G. Coker Charge Heater Design - Full tube side kinetic, vaporization and hydraulic model of the “in tube” delayed coking process in the fired heater. This proprietary software allows us to correctly design coker charge heaters for the minimum rate of coke build up during operation.

2. AVAILABLE HEATER SERVICES:

A. Crude and Vacuum – Specific tube side calculations are provided that match with the various heater design programs in # 1 above. Provisions for TBP, D86, D1160, EFV or pseudo component input are available. Also provisions for multiple defined light components and steam and/ or water injection.

B. Transfer Line to tower design - Finally, if good quality data is not available at the heater outlet we can start at the tower flash zone and calculate our way back to the heater outlet, assuming that a transfer line Isometric drawing with segment lengths, pipe sizes and good flash zone pressure and temperature is available.




This last program is of growing popularity since heavier crude oils change the nature of the flow to the tower as well as increasing the vacuum unit flow.

C. Liquid Streams – Programs for the tube side calculation for various defined liquid streams such as water, HC and water (glycols and water mixtures, etc.) and standard heat transfer oils are provided for. Also these programs will handle high viscosity liquids where the wall viscosity effect is prominent. They will provide an inside heat transfer coefficient for both the bulk liquid and the film at the wall.

D. Hydro-Treater and Hydro-Cracker Heaters. Reactor and Feed heaters E. Naphtha Reformer Heaters and related units. F. Coker Charge Heaters – See below. G. Various steam services such as superheating, steam generation and feed water

preheating. H. A more complete list of programs available is attached for your review. I. Extensive experience in various forms of heater fouling and corrosion. J. Specific knowledge in virtually all areas of tubular metallurgy. Carbon, Mid Chromes

and Austenitic Stainless Steels and specialty Stainless Steels such as 317 SS or Specialty metals such as Incaloy 800, Hastelloy C276.

K. Knowledge of cast tubes, fittings and tube supports such as HH, HK and HP Modified. L. Specific knowledge of several processes such as SOR and EOR considerations and

catalyst regeneration operations (Heater Related). All together we represent close to half a century of fired heater design, fabrication and operational experience and have participated in numerous API Committees such as:

A. RP / STD 530 – Tube Thickness Calculations. B. RP / STD 560 – General Purpose Refinery Heater design. C. RP 533 - Air Preheater Systems D. RP 534 - HRSG Units. E. Heater Efficiency, Burner Design and Tube Support Design.

To summarize we can provide a complete and experienced design group ready to support your company in any way you see fit. We also can provide these services for virtually all types of refinery and natural gas plant fired heaters and most chemical plant uses.

We feel all of the above qualifies THERMATRAN for virtually any fired heater problem you or your colleagues at may put before us other than some reaction heaters such as Steam-Hydrocarbon Hydrogen Reformer Heaters or Ethylene Cracking Heaters and we might be of some service in those areas also.




We look forward to discussing this with you further to a favorable end for both parties. Yours Very Truly, ThermaTran, Inc. Reed T. Melton President THERMATRAN, Inc. 8721 South 65th East Place Tulsa, OK 74133 Phone: 918-748-4406 Cell: 918-381-5696 E-Mail: [email protected] cc: Carol Melton – ThermaTran, Inc.

mailto:[email protected]

Item 3

ThermaTran’s Experience in Delayed Coker Charge Heaters

2 Sheets

ThermaTran, Inc.Coker Charge Heater Experience

Through 10/3/2016Page 1

COKER CHARGE HEATERSUMMARY OF DESIGN & EVALUATION EXPERIENCE

DESIGN & SUPPLY OF COKER CHARGE HEATERS While Reed Melton is at Radco ( July 1973 - Dec 31 1994)AND AT TPE (September 1, 2004 - March 7, 2012)

RADCO ABSORBED DUTYJOB NO. CLIENT CONFIGURATION MM BTU/HR.

255 C. E. LUMMUS, HUNT REFINING, TUSCALOOSA, AL SINGLE FIRED BOX 44.35336 AMOCO CORP., TEXAS CITY, TX SINGLE FIRED BOX 40.70372 AMOCO CORP.,WHITING, IN DOUBLE FIRED BOX 182.00436 AMOCO CORP., YORKTOWN, VA DOUBLE FIRED BOX 56.84474 ULTRAMAR, WILMINGTON, CA DOUBLE FIRED BOX 86.30479 STAR ENTERPRISE, PORT ARTHUR, TX DOUBLE FIRED BOX 111.76480 STAR ENTERPRISE, PORT ARTHUR, TX DOUBLE FIRED BOX 111.76498 SUN OIL COMPANY, TULSA, OK DOUBLE FIRED BOX 52.90

EJ1161-1 & 2 HUNT REFINING, TUSCALOOSA, AL SINGLE FIRED BOXES 97.27REVAMP SINGLE FIRED

NOTE 1: TWO HEATERS AT 48.635 = 97.27 MMBtu/ hr Total COKER CHARGE HEATER #1AND CONVERT SINGLE FIREDCOKER PREHEATER TO COKER CHARGE SERVICE #2BOTH WITH ULTRA LOW NOXBURNERS

Total MMBtu/ hr 783.88

ThermaTran, Inc.Coker Charge Heater Experience

Through 10/3/2016Page 2

CONSULTING, DESIGN & EVALUATION CONTRACTS While Reed Melton is at Radco Inc. and/ or TPE Inc.

TPEJOB NO. CLIENT CONFIGURATION

EJ525 ARCO/CHERRY POINT, WA SINGLE FIRED BOXEJ543 ARCO/LAR, CA SINGLE FIRED BOXEJ868 AMOCO/TEXAS CITY, TX SINGLE FIRED BOXEJ893 ARCO/CHERRY POINT WA SINGLE FIRED BOXEJ899 B & V PRITCHARD/TEXACO El Dorado, KS SINGLE FIRED BOXEJ915 MARAVEN VENEZUELA DOUBLE FIRED BOXEJ999 TOSCO/SANTA MARIA, CA SINGLE FIRED BOX

EJ1022 KOCH, CORPUS CHRISTI, TX SINGLE FIRED BOXEJ1055 FRONTIER EL DORADO, KS SINGLE FIRED BOXEJ1062 BP CHERRY POINT, WA DOUBLE FIRED BOXEJ1070 HUNT REFINING, TUSCALOOSA, AL SINGLE FIRED COKEREJ1071 COASTAL ARUBA DOUBLE FIRED BOXEJ1078 FRONTIER EL DORADO SINGLE FIRED COKEREJ1100 PETRO CANADA LICENSE & DESIGN DOUBLE FIRED BOX

EJ1109-1 CONOCOPHILLIPS-SWEENEY DOUBLE FIRED BOXEJ1109-2 CONOCOPHILLIPS-BELLE CHASE DOUBLE FIRED BOXEJ1109-3 CONOCOPHILLIPS-PETROBRAS, BRAZIL DOUBLE FIRED BOX

Item 4

ThermaTran’s Experience (Reed Melton’s Experience) in Major Fired Heaters at Radco, Inc.

This comes in two (2) Parts:

1) A table of the subject heaters Reed Melton had major responsibility for – MS Word Document – 7 pages

2) Spread Sheet form by Radco Job Number – 8 pages

ThermaTran, LTD 8721 South 65th East Place, Tulsa, Oklahoma 74133 August 31, 2016 This letter concerns Process fired Heater Experience at my time at Radco, Inc. and afterward in accordance with the attached Selected Jobs Spread Sheet of the Radco, Inc. and TPE, Inc. taken from the Master Job list. Also note my resume attached and a ThermaTran introduction historical experience document. I started work at Radco on July 3 1973 after spending 1968 to 1972 working with and for Econo-Therm Corp. in Tulsa, OK, USA. The 1973 date was fortuitous for me because of the Israeli / Arab war of October 1973. This caused an overnight doubling of the price of a barrel of crude oil. The result of that price jump was that it instigated a very major increase in capital spending by the US refineries, in particularly for fired heaters. Comments: Job No. or Nos. Comments 32 and 33 This is a pair of Steam Superheaters Purchased by Brown and Root for a

Copper Smelter in New Mexico, in 1973. This is included to note that while Refinery and Gas Plant and Chemical Plant work is what Radco was principally noted for we also did many projects outside of that narrow grouping. Duty each is 37.3 MMBtu/ hr.

41 This was my first major sale after the October 4, 1973 Mideast war. It

was a replacement for the Hunt Refining major Crude Feed Heater and included a BW/ Boiler section in the top of the heater convection section. This was designed to UOP standards for Hunt Refining Company, Tuscaloosa, Alabama. Total duty 96.59 MMBtu/ hr

49 through 51 These were Radco’s first heaters for Exxon at the Baton Rouge, LA

Refinery. Two of the heaters were Vertical Crude Heaters with duty of 53.0 MMBtu/ hr each and the third heater was a Vertical Vacuum Crude Heater at 36.9 MMBtu/ hr.

Each of these Fired Heaters also included a finned tubular air preheat (APH) exchanger of my own design as was the rest of the APH system, again sold in 1973.

52 through 57 A complete UOP platformer set of heaters including HDS heaters. Sold in

1976. Normally these platformer heaters included a Charge Heater, and #1 and #2 Interheaters. The Interheaters were radiant heaters only with their flue gas ducted to Charge (Center) Heater between its radiant and convection. The convection was usually a combination Boiler Feed Water Heating Coil, A Steam Generation Coil and generally a Steam Superheat Coil.

The HDS heaters were generally radiant and convection vertical heaters. 72 and 100 These were two (2) Crude Feed Heaters that went into service, for ARCO,

on the north slope of Alaska and they both included a top convection section finned tube air preheater to keep the burners from having to start up totally cold. This exchanger was naturally drafted on the flue gas side. The customer was so pleased with the first unit that they later ordered the second unit. Heater Duty – 14.725 MMBtu/ hr each.

88 and 89 Two (2) major hot oil heaters for Amoco at the Whiting, Indiana Refinery

and designed and managed to Stone & Webster specifications. These heaters both fired both Natural Gas and No. 6 Fuel Oil and included air preheaters and soot blowers as well as a deep combustion tub to assure total combustions of the heavy fuel oil. Each at 215 MMBtu/ hr (LHV)

92 through 98 Similar to 52 through 57 above. Total Platformer Duty – 26.68 MMBtu/

hr 123 through 128 Again similar to 52-57, and 92-98. These are examples of the flexibility

of our process software. Total Platformer Duty – 135.45 MMBtu/ hr. 132 Large Crude Heater for Amoco at Wood River, IL (across the Mississippi

River from St. Louis, MO) Oil and Gas fired with the deep combustion chamber and Air Preheat System as in 88 and 89 above. The duty was 125 MMBtu/ hr.

133 through 139 Another UOP Platformer / HDS unit at Three Rivers, Texas East of San

Antonio, TX Howe Baker Engineers. Total Platformer Duty – 56.1 MMBtu/ hr

143 A recovered heater from an old refinery at Corpus Christi, TX now being

installed in the Atlas Processing Co. Refinery at Shreveport, LA. This required substantial structural fixing and additive support members as well as a new convection section. Crude Duty - 71.776 MMBtu/ Hr.

144-145 A small combined Crude and Vacuum unit with a preflash reboiler.

Another example of the range of sizes of heaters we were able to produce at Radco. Total Duty 51.58 MMBtu/ hr

178 to 179 Two HDS unit heaters that joined later with 52 through 57 above and

allow the Platformer to process higher sulfur streams. Total Duty – 42.87 MMBtu/hr

180,181 and 182 Three small to medium Crude Heaters for independent refineries in Farmington, NM and Abilene, TX. Total Duty – 97.56 MMBtu/ hr 183, 184 and 189 A preflash Crude Bottom (Vacuum) Heater (183) and a mixed gas oil

heater for Lion Oil in El Dorado, AR and a larger crude heater for export to the Middle East. Total Duty – 151.9 MMBtu/ hr

192 through 195 Four (4) vertical crude heaters for the Fina Refinery at Nederland, TX

(near Port Arthur, TX). Total Duty – 300.7 MMBtu/ hr 196 through 198 Three HDS unit heaters for Champlin, Refining at Wilmington, CA (Near

Long Beach, CA). Sold to Fluor E&C of Irvine, CA Total Duty – 39.37 MMBtu/ hr

199 A Vacuum Heater similar to Crude heaters 72 and 100 above in that it

contained a naturally drafted combustion air preheater for this Superior, WI Refinery on the far north side of the US. Duty 20.oo MMBtu/ hr

201 A medium large Crude Heater for an expansion project at Three Rivers,

TX. Duty – 80.00 MMBtu/ hr 202 A 30/ 70 EG/ Water heat medium heater at the Phillips 66 Adams

Terminal on the Houston, TX Ship Channel. Total Duty – 113.20 MMBtu/ hr

224, 225 A Reactor Charge Heater for Hawaiian Refinery in Oahu, HI. This

was high pressure double fired heater for a Hydrocracker Charge Duty. Also included a Reboiler Heater for the same unit. Total Duty – 84 MMBtu/ hr.

228, 229 Two Powerformer Reheaters Vertical. These were large Vertical

Cylindrical Heaters that shipped to Kenai Alaska through

Wyoming and Montana to get to an ocean going barge to Alaska. They were however held up for about five (5) days in Montana when Mount St. Helen in Southern Washington State erupted and dumped major amounts of volcanic ash on the highway in Montana. They were eventually erected and started up in Alaska and are still running today. Total Duty – 69.76 MMBtu/ hr.

237, 238 These are two small Crude and Vacuum Heaters for a refinery in

Northwest Louisiana. Purchased by Stone and Webster. Total Duty – 16.25 MMBtu/ hr.

244 Vacuum Feed Heater HIRI Hawaii Total Duty – 63.00 MMBtu/ hr. 250 One of our largest projects – Two parallel Crude Feed Heaters with remote

preheat convection boxes to get more absorbed duty. Replaced two (2) old MW Kellogg Crude heaters that were 90 Feet long. Duty for each of the two (2) units – 217.1 MMBtu/ hr or 434.2 MMBtu/ hr total

255, 256 & 257 Coker Feed Heater, Coker Feed Preheater and Oil Preheater for Lummus

and installed at Hunt Refining, Tuscaloosa, AL – Total Duty – 126.35 MMBtu/ hr

258, 259 & 260 Three heaters for Lube Oil / Wax Unit at Atlas Processing in Shreveport,

LA Total Duty – 77.96 MMBtu/ hr 280 FCC Power Recovery Boiler – Schedule A by UOP and built for

Champlin, Refining at Wilmington, CA. Bought and Installed by Fluor E&C Irving, CA. A major rail shipment of over 175 tons. Duty – 52.77 MMBtu/ hr

282 Vacuum Feed Heater - Gulf Oil, Port Arthur, TX purchased and installed

by Litwin Engineers – Duty 73.00 MMBtu/ hr 285-287 Three Heaters for a Platformer / HDS unit at Pertamina, Indonesia Duty

145.39 MMBtu/ hr 288-289 Two Cat Cracker Feed Hydrotreater Heaters Duty – 21.64 MMBtu/ hr

each

306 through 311 L-C Fining Oil and Hydrogen Heaters (3 of each) with 3,400 PSIG design Pressures. Very complicated due to the large design pressure. This high design pressure took the wall thickness out of the ability of API STD 530.

Total Duty (306 through 311) – 165 MMBtu/ hr 313 Quintana Petrochemical Crude Heater - Corpus Christi, TX – Duty 103.7

MMBu/ hr 315 Hydrocracker Feed Heater – 2,400 PSI Design double fired unit – Hawaii

Duty 47.268 MMBu/ hr 318 Ammonia Reformer Convection Section – Amoco, Texas City - Duty

142.5 MMBu/ hr 324 Hydrogen Reformer Convection Section – 340.00 MMBtu/ hr

Amoco, Texas City, TX 336 Coker Charge Heater – Amoco, Texas City, TX Duty 40.7 MMBu/ hr 339 Arco Petroleum Products – Air Preheater Pasadena, TX Duty 110.0

MMBu/ hr 341 Mapco at North Pole, AK Crude Heater – 193.88 MMBtu/ hr

Arctic conditions and design. 344 Ultraformer – Corpus Christi, TX – Koch Refining Duty 97.18 MMBtu/ hr 361 Amoco Oil Co. - Texas City, TX Two Vacuum Heaters/ Pipestill 3A

each with Air Preheat Total Duty 180.00 MMBtu/ hr 363 through 367 Beacon/ Amoco Production Wyoming 3 x 50/50 Glycol/ Water

heaters and 2 x 6 MMBtu/ hr Residue Gas Heaters Total Duty 96.39 MMBu/ hr

368, 369 and 370 Reformer Expansion Charge and #1 and #2 Interheater with combined Air

Preheat. Total Duty 72.0 MMBu/ hr 372 Coker Charge Heater – Amoco Whiting, IN 182 MMBtu/ Hr with Air

Preheat. This was our flagship double fired coker charge heater was the basis for our following patent on that design. This was also a major erection achievement as one half of the heaters was erected intact on a major crawler type trailer and pulled in over the original foundation piers

of the previous Coker Charge Heater and it fit perfectly as well as the second half of the heaters allowing the project to be finished in well below the project estimated time.

380 and 381 Two Vacuum Tower Feed Heaters for Exxon, Baytown, TX Duty 25.0

MMBu/ hr each 387 FCC Reactor Preheater - Unocal, Beaumont, TX Duty 65.0 MMBu/ hr 390-396 Crude Heaters for a Pipeline – Saudi Arabia 31.195 MMBtu/ hr each of 7 406-409 Four Ethylene Cracking Heaters – Quantum Chemical, Tuscola, IL each

was 79.91 MMBtu/ Hr 413 CCR Platformer Charge/ #1 and #2 Interheaters - total 98.71 MMBtu/ Hr

Kerr Magee - Wynnewood, OK 426-430 Five Heaters for Samsung General Chemicals – South Korea Total Duty

106.3 MMBu/ hr 436 Conversion of two single fired Coker Charge Heaters – Amoco,

Yorktown, VA - Duty 56.84 MMBu/ hr 445-446 Navajo Refining – Clovis, NM 3 Cell CCR Platformer Heater

134.90 MMBtu/ hr and one Depropanizer Reboiler, Fluor Daniel 448-453 4 Cell UOP CCR Platformer Charge/ Interheaters and 5 additional process

heaters – The CCR Platformer Heaters were rated at 300 MMBtu/ hr and was at that time (1990) the largest CCR Platformer Charge / Interheater Heater ever designed by UOP. The 5 additional heaters operate on a combined Air Preheat System. Total Additional Duty 162.2 MMBu/ hr

Or 462.2 MMBtu/ hr total unit.

All Heaters still operating at this time as Valero 466 Tazca, Venezuela Isostripper Reboiler Heater -35.40 MMBtu/ hr 467-468 Hydrotreater Rx Charge Heater and Hydrotreater Fractionator Reboiler

Heater – Total Duty 130.75 MMBtu/ Hr - Texaco, Anacortes, WA 470 CCR Platformer Heater – NCRA, McPhearson, KS 207.52 MMBtu/ hr

The convection section contained two (2) process preheat coils as well as the Boiler and BFW coils.

474 Double Fired Coker Charge Heater with Selective Catalytic Reducer unit

and Air Preheat - Ultramar, Wilmington, CA – 86.3 MMBtu/ hr 479-480 Two Double Fired Coker Charge Heaters – 111.76 MMBtu/ hr each. Our

best Double Fired Unit in terms on run times between decoking. 481-485 Heavy Crude Heaters for Venezuela - 105.00 MMBtu/ hr each 487 HDA Reactor Feed Heater/ Double Fired Unit – 10.630 MMBtu/ hr Lucky Petrochemical, Yeochun, Korea 491-493 Two (2) Hydrotreater Charge Heaters and one Reboiler plus steam Coil Total Duty – 74 MMBtu/ hr NCRA at McPhearson, KS 498 Double Fired Coker Charge Heater – Sun Ref and Marketing, Tulsa, OK Total Duty – 52.90 MMBtu/ hr 513-520 Eight Ketene (Acetic Anhydride Cracking Heaters) 4 to South Caroline

and 4 to Virginia, Hoeschst Celanese Chemical by Rust Engineering, Birmingham Alabama. Double Fired design with multiple rows of wall type burners and tubes of Special design 317 SS formula. Total Duty 92.0 MMBu/ hr

Page No. 1

Notes: He - Helical1. Air Preheat Project Ho - Horizontal2. Waste Heat Boiler V - Vertical3. Steam Superheater W - Wicket4. SCR5. Turbine Heat Recovery

JOB #.NO. OF DWG CUSTOMER P.O. DATE CUSTOMER P.O.# JOBSITE

REF. NOTE

HEATER MM/Btu COILS

32 1 3/6/73 HIDALGO CO., NM 3 37.30 Ho

33 *** 4/9/73 HIDALGO CO., NM 3 37.30 Ho

41 2 1/2/75 TUSCALOOSA, AL 2 96.59 Ho

49 1 12/16/73 BATON ROUGE, LA 1 53.00 V

50 *** 12/16/73 BATON ROUGE, LA 1 53.00 V

51 *** 12/16/73 BATON ROUGE, LA 1,3 36.90 V

52 10 12/26/76 MEMPHIS, TN 12.76 V

53 *** 12/26/76 MEMPHIS, TN 12.54 V

54 *** 12/26/76 MEMPHIS, TN 13.00 V

55 *** 12/26/76 MEMPHIS, TN 24.90 V

56 *** 12/26/76 MEMPHIS, TN 22.90 V

57 *** 12/26/76 MEMPHIS. TN 8.90 V

72 1 4/8/74 PRUDHOE BAY, AK 1 14.725 He

88 1 10/16/74 WHITING, IN 1 215.00 Ho

89 *** 10/16/74 WHITING, IN 1 215.00 Ho

92 15 11/4/77 BAKERSFIELD, CA 9.15 V

93 *** 11/4/77 BAKERSFIELD, CA 9.55 V

94 *** 11/4/77 BAKERSFIELD, CA 2,3 50.00 V

95 *** 11/6/77 BAKERSFIELD, CA 14.70 V

96 *** 11/7/77 BAKERSFIELD, CA 7.70 V

97 *** 11/8/77 BAKERSFIELD, CA 4.28 V

98 *** 11/9/77 BAKERSFIELD, CA 7.58 V

100 1 N/A PRUDHOE BAY, AK 1 14.725 Ho

FOSTER WHEELER CORP

FOSTER WHEELER CORP

FOSTER WHEELER CORP

FOSTER WHEELER CORP

FOSTER WHEELER CORP.


BROWN & ROOT, INC

EXXON

EXXON

WALK HAYDEL & ASSOC.

BROWN & ROOT, INC

EXXON



AMOCO OIL CO

FOSTER WHEELER CORP

FOSTER WHEELER CORP

ATLANTIC RICHFIELD CO.

AMOCO OIL CO

FOSTER WHEELER CORP


FOSTER WHEELER CORP

ATLANTIC RICHFIELD CO

EQUIPMENT

COPPER SMELTER53-0085-2037

53-1185-2037

74996

COPPER SMELTER

ATMOSPHERIC/CRUDE UNIT

PH-2214-1350

PLATFORMER CHARGE HEATER

PLATFORMER #2 INTERHEATER

PH-2214-1350

PH-2214-1350

PH-2214-1350 HDS/ STRIPPER REBOILER

ME-50454-K-53612

PH-2214-1350 HDS/ REACTOR CHARGE HEATER

ME-50454-K-53612

ATMOSPHERIC CRUDE HEATER

HDS/ STABILIZER REBOILER

ME-50454-K-53612 ATMOSPHERIC CRUDE HEATER

VACUUM HEATER

PLATFORMER #1 INTERHEATER

PH-2214-1350

CRUDE HEATER/AIR PREHEATER40403-7203

PH-11-114-2120 PLATFORMER#1 INTERHEATER

PH-11-114-2120

PH-11-114-2120

801-2-2779

HOT GAS OIL HEATER

HOT GAS OIL HEATER

PLATFORMER CHARGE HEATER

PH-11-114-2120 REFORMER

HYDROTREATER CHARGE HEATER

PH-11-114-2120 STRIPPER REBOILER HEATER

801-2-2779

CRUDE HEATER

PH-11-114-2120 PLATFORMER#2 INTERHEATER

PH-11-114-2120 DEPROPANIZER REBOILER HEATER

50114-7206

Page No. 2



REF. NOTE

HEATER MM/Btu COILSEQUIPMENT

123 12 8/6/76 CORPUS CHRISTI, TX 30.00 V

124 *** 8/6/76 CORPUS CHRISTI, TX 2 86.95 V


126 *** 8/7/76 CORPUS CHRISTI, TX 40.50 V



132 6 9/26/76 WOOD RIVER, IL 125.00 Ho

133 12 10/8/76 THREE RIVERS, TX 1 13.50 V

134 *** 10/8/76 THREE RIVERS, TX 17.40 V

135 *** 10/8/76 THREE RIVERS, TX 9.00 V

136 *** 10/8/76 THREE RIVERS, TX 26.60 V

137 *** 10/8/76 THREE RIVERS, TX 19.70 V

138 *** 10/8/76 THREE RIVERS, TX 9.80 V

139 *** 10/8/76 THREE RIVERS, TX 7.00 V

143 2 2/22/78 SHREVEPORT, LA 3 71.776 V

144 9 6/15/78 THREE RIVERS,TX 40.00 V

145 *** 3/7/78 THREE RIVERS,TX 3 8.00 V

146 *** 3/7/78 THREE RIVERS,TX 3.5754 V

178 5 9/6/78 MEMPHIS, TN 17.25 V

179 *** 9/6/78 MEMPHIS, TN 25.62 V



SOUTHERN ENGINEERING


HOWE-BAKER ENGINEERS


AMOCO OIL CO




ATLAS PROCESSING CO




QUINTANA-HOWELL CORP




140-0742-00-001



BA-201 CATALYTIC REFORMER/CHARGE HEATER/C

HDS FEED HEATER

REFORMER CHARGE HEATER

4039

H-110202552

BA-202 & 204 CATALYTIC REFORMER/#1 INTERHEATER

L-10

CRUDE HEATER

802-2-4268 CRUDE HEATER (NO. 5 PIPE STILL)

L-101

140-0742-00-001

HDU REACTOR CHARGE HEATER (NAPTHA)

HDU SPLITTER REBOILER (NAPTHA)

BA-203

L-102 HDA RECYCLE TOWER FEED HEATER

DEOCTANIZER REBOILER

CATALYTIC REFORMER/#2 INTERHEATER

HDU STRIPPER REBOILER

REFORMER INTERHEATER #1

140-0742-00-001

140-0742-00-001

REFORMER INTERHEATER #2

140-0742-00-001 STABILIZER REBOILER

140-0742-00-001

140-0742-00-001

6-114-2180

CRUDE TOWER CHARGE/LUBE UNIT

HDS REACTOR6-114-2180

HDS/REBOILER HEATER

VACUUM TOWER CHARGE HTR/LUBE UNIT

H-1001 78252-6

H-1002 78252-6

CRUDE PREFLASH REBOILER

Page No. 3



REF. NOTE


180 1 9/6/78 FARMINGTON, NM 14.19 Ho

181 *** 9/6/78 ABILENE, TX 42.885 Ho

182 *** 10/3/78 ABILENE, TX 40.482 Ho

183 9/28/78 EL DORADO, AR 25.00 Ho

184 9/28/78 EL DORADO, AR 40.00 Ho

189 3/5/79 WESTWEGO, LA 2 86.90 Ho

192 12 4/9/79 NEDERLAND, TX 2 83.48 V

193 *** 4/9/79 NEDERLAND, TX 2 85.46 V

194 *** 4/9/79 NEDERLAND, TX 2 97.72 V

195 *** 4/9/79 NEDERLAND, TX 2 34.04 V

196 9 4/3/79 WILMINGTON, CA 9.64 V

197 *** 4/9/79 WILMINGTON, CA 14.83 V

198 *** 5/30/79 WILMINGTON, CA 14.90 V

199 3 5/30/79 SUPERIOR, WI 1 20.00 V

201 4 6/14/79 THREE RIVERS, TX 80.00 Ho

202 4 6/30/79 PASADENA, TX 113.20 V

224 7 7/9/80 OAHU, HI 2 28.06 V

225 *** 7/9/80 OAHU, HI 2 55.94 Ho

228 7 11/5/79 KENAI, AK 45.745 V

229 *** 11/5/79 KENAI, AK 24.01 V

237 8 1/17/80 PRINCETON, LA 1 10.80 HoSTONE & WEBSTER

FOSTER WHEELER CORP

LITWIN ENGINEERS

FOSTER WHEELER

LITWIN ENGINEERS

FLOUR DANIEL

FLOUR DANIEL

MURPHY OIL


GIANT REFINING CO.

PRIDE REFINING CO.

PRIDE REFINING CO.

EDCO (LION OIL CO)

EDCO (LION OIL CO)

LITWIN ENGINEERS

FLUOR DANIEL

PCI ENGINEERS

PHILLIPS PETRO. CO

LITWIN ENGINEERS

LITWIN ENGINEERS

LITWIN ENGINEERS

PH-4-114-2420

H-102 12956

4173-12-8-

9-693781-PX

AGO, VGO, DAGO & STACK

M-13966

M-13966

13686

13686

CRUDE CHARGE HEATER

20306

CRUDE CHARGE HEATER

PREFLASH CRUDE BOTTOM HEATER

CRUDE HEATER

HDS STRIPPER REBOILER

ATMOSPHERIC CRUDE/CDU-4

4135-12-6-

4135-12-6- ATMOSPHERIC CRUDE/CDU-2

4135-12-6-

140-0851-00-063

2204

465924-4-0501

4135-12-6-

CRUDE OIL HEATER

HDS CHARGE HEATER

ATMOSPHERIC CRUDE/CDU-2

DEPROPANIZER REBOILER

VACUUM CHARGE HEATER

ATMOSPHERIC CRUDE

VACUUM CHARGE HEATER

57770

465924-4-0501

465924-4-0501

ETHLENE GLYCOL HTR (70% H20/30% GLYCOL)

HYDROCRACKER FRACTIONATOR REBOILERPH-4-114-2420

HYDROCRACKER CHARGE HEATER

#1 REHEAT/POWERFORMER4173-12-8-

#2 REHEAT/POWERFORMER

CHARGE HEATER/FLASH CRUDE

Page No. 4



REF. NOTE


238 *** 8/13/80 PRINCETON, LA 1 5.35 Ho

244 5 1/12/81 OAHU, HI 1 63.00 Ho

250 30 11/30/81 TEXAS CITY, TX 1 434.20 Ho

255 9 5/21/81 TUSCALOOSA, AL 44.35 Ho

256 *** 5/21/81 TUSCALOOSA, AL 64.00 Ho

257 *** 3/4/81 TUSCALOOSA, AL 18.00 Ho

258 8 4/12/80 SHREVEPORT, LA 39.64 Ho

259 *** 8/14/80 SHREVEPORT, LA 21.12 Ho

260 *** 9/24/80 SHREVEPORT, LA 17.20 Ho

280 10 2/10/81 WILMINTON, CA 2 52.77 V

282 5 9/17/81 PORT ARTHUR, TX 73.00 V

285 15 FLUOR ENGINEERS 1/12/82 INDONESIA 93.00 V

286 *** 1/12/82 INDONESIA 29.07 V

287 *** 1/12/82 INDONESIA 23.32 V

288 11 C.F. BRAUN & CO. 7/24/81 TEXAS CITY, TX 21.64 Ho

289 *** C.F. BRAUN & CO. 7/24/81 TEXAS CITY, TX 21.64 Ho

306 16 C.F. BRAUN & CO. 5/13/82 TEXAS CITY, TX 27.50 V

307 *** 5/13/82 TEXAS CITY, TX 27.50 V

308 *** 5/13/82 TEXAS CITY, TX 27.50 Ho

309 *** 5/13/82 TEXAS CITY, TX 27.50 Ho

310 *** 5/13/82 TEXAS CITY, TX 27.50 Ho

SUNTECH

FLUOR ENGINEERS

FLUOR ENGINEERS

FLUOR ENGINEERS

LITWIN ENGINEERS

C.F. BRAUN & CO.

C.F. BRAUN & CO.

C.F. BRAUN & CO.

C.F. BRAUN & CO.

STONE & WEBSTER

FOSTER WHEELER

C.E. LUMMUS

C.E. LUMMUS

C.E. LUMMUS

SUNTECH

AMOCO OIL CO

SUNTECH

5687

1000-H-05-02

589-11-141-1

475224-4-0503

5894-120-141-1

5894-120-141-1

2-000-003-

1000-H-03-01

FEED HEATER/VACUUM

COKER HEATER/DELAYED

2-000-003-

CRUDE HEATER W/ REMOTE CONVECTION

REDUCED CRUDE HEATER

PJ48-114-2420

H-102 12956

FCC POWER RECOVERY BOILER

FEED PREHEATER/DELAYED

VACUUM CHARGE HEATER/LUBE

2-000-003

1000-H-03-01

VACUUM HEATER/CRUDE UNIT4184-1241.1

CHARGE HEATER/NAPTHA HYDROHEATER477804-4-0503-01

SOFT WAX MIX HEATER

OIL PREHEATER/DELAYED/COKER

WAX FREE OIL MIX HEATER

5894-120-141-1 L-C FINING/OIL HEATER

L-C FINING/OIL HEATER

L-C FINING/HYDROGEN HEATER

DEBUTANIZER REBOILER/PLATFORMER

477804-4-0503-01 STRIPPER REBOILER/NAPTHA HYDROHEATER

477804-4-0503-01

CAT. FEED HYDROHEATER FEED HEATER

589-11-141-1 CAT. FEED HYDROHEATER FEED HEATER

5894-120-141-1

5894-120-141-1

L-C FINING/HYDROGEN HEATER

L-C FINING/ OIL HEATER

Page No. 5



REF. NOTE


311 *** 5/13/82 TEXAS CITY, TX 27.50 Ho


315 4 8/1/83 OAHU, HI 47.268 Ho

318 1/12/82 TEXAS CITY, TX 142.50 Ho

324 *** 5/13/82 TEXAS CITY, TX 340.00 Ho

336 13 10/12/83 TEXAS CITY, TX 40.70 Ho

339 13 2/00/88 PASADENA, TX 110.00 Ho

341 *** 4/18/85 NORTH POLE, AK 193.88 Ho

344 10/1/84 CORPUS CHRISTI, TX 1 97.18 V

361 1/13/86 TEXAS CITY, TX 180.00 Ho

363 4/29/86 WYOMING 28.14 Ho

364 4/29/86 WYOMING 28.14 Ho

365 4/29/86 WYOMING 28.14 Ho

366 4/29/86 WYOMING 5.985 Ho

367 4/29/86 WYOMING 5.985 Ho

368 27 3/20/87 DENVER, CO 29.00 V

369 *** 3/20/87 DENVER, CO 29.00 V

370 *** 3/20/87 DENVER, CO 14.00 V

CONOCO INC

CONOCO INC

AMOCO OIL CO.

BEACON/AMOCO PROD.

CONOCO INC

BEACON/AMOCO PROD.

BEACON/AMOCO PROD.

BEACON/AMOCO PROD.

BEACON/AMOCO PROD.

C.F. BRAUN & CO.

QUINTANNA PETROCHEMICAL

MAPCO INC

AMOCO OIL CO

KOCH REFINING CO.

FOSTER WHEELER CORP

AMOCO OIL CO

ARCO PETROLEUM PROD.

C.F. BRAUN & CO

5894-150-141-1

PH-25-114-3441

ULTRAFORMERC-42203-R2

HEAT MEDIUM HEATER (50% GLYCOL/50% H2O)16362F1000HAC0007

830-3-12325 COKER CHARGE HEATER

830-313828 VACUUM HEATER/PIPESTILL 3A

1451 CRUDE HEATER

14805

AIR PREHEAT SYSTEM

CRUDE HEATER

HRE-1927

8894-151-141-1 HYDROGEN REFORMER CONVECTION SECTION

5894-120-141-1 L-C FINING/HYDROGEN HEATER

AMMONIA REFORMER CONVECTION SECTION

HTDRO CRACKER

REFORMER EXPANSION/CHARGE HEATER

RESIDUE GAS HEATER

HEAT MEDIUM HEATER (50% GLYCOL/50% H2O)

HEAT MEDIUM HEATER (50% GLYCOL/50% H2O)

16362F1000HAC0007

042-396875-6

RESIDUE GAS HEATER

16362F1000HAC0007

16362F1000HAC0007

16362F1000HAC0007

042-396875-6

REFORMER EXPANSION/#2 INTERHEATER

REFORMER EXPANSION/#1 INTERHEATER

042-396875-6

Page No. 6



REF. NOTE


372 19 8/4/86 WHITING, IN 1 182.00 Ho

380 3 2/24/87 BAYTOWN 25.00 Ho

381 *** 2/24/87 BAYTOWN 25.00 Ho

387 11 11/00/87 BEAUMONT, TX 65.00 V

390 13 1/12/88 SAUDI ARABIA 31.195 Ho

391 *** 1/12/88 SAUDI ARABIA 31.195 Ho

392 *** 1/12/88 SAUDI ARABIA 31.195 Ho

393 *** 1/12/88 SAUDI ARABIA 31.195 Ho

394 *** 1/12/88 SAUDI ARABIA 31.195 Ho

395 *** 1/12/88 SAUDI ARABIA 31.195 Ho

396 *** 1/12/88 SAUDI ARABIA 14.17 Ho

406 55 11/16/88 TUSCOLA, IL 1 79.91 V

407 *** 11/16/88 TUSCOLA, IL 1 79.91 V

408 *** 11/16/88 TUSCOLA, IL 1 79.91 V

409 *** 11/16/88 TUSCOLA, IL 1 79.91 V

413 29 3/7/89 WYNNEWOOD, OK 98.71 V

414 *** 3/7/89 WYNNEWOOD, OK 98.71 V

415 *** 3/7/89 WYNNEWOOD, OK 98.71 V

426 26 8/11/89 KOREA 3.97 V

427 *** 8/11/89 KOREA 15.24 V

428 *** 8/11/89 KOREA 45.24 VSAMSUNG

QUANTUM USI

QUANTUM USI

SAMSUNG




SAMSUNG




QUANTUM USI

QUANTUM USI

AMOCO OIL CO



EXXON

EXXON


UNOCAL


FC 00015901

140-132-6-00-01

CCR PLATFORMER/#2 INTERHEATER

140-1275-00-01

CRUDE HEATER

ETHYLENE CRACKING HEATER(FUTURE)

140-132-6-00-01 CCR PLATFORMER CHARGE HEATER

801-3-13749

B-8783

COKER CHARGE HEATER

04TT08061671399

VACUUM TOWER HEATER

VACUUM TOWER HEATER

04TT08061671399

FCC REACTOR PREHEAT

CRUDE HEATER140-1275-00-01

CRUDE HEATER

CRUDE HEATER

57068

57068

57068

57068

ETHYLENE CRACKING HEATER

ETHYLENE CRACKING HEATER(FUTURE)

ETHYLENE CRACKING HEATER

140-132-6-00-01

CCR PLATFORMER/#1 INTERHEATER

140-1275-00-01

140-1275-00-01

CRUDE HEATER

140-1275-00-01 CRUDE HEATER

140-1275-00-01

140-1275-00-01

CRUDE HEATER

FC 00015901 C8/C9

CAT. REGENERATION

HYDROGENERATIONFC 00015901

Page No. 7



REF. NOTE


429 *** 8/11/89 KOREA 8.91 V

430 *** 8/11/89 KOREA 32.94 V

436 19 11/17/89 YORKTOWN, VA 56.84 Ho

445 43 2/1/90 ARTESIA, NM 134.90 Ho

446 *** 2/1/90 ARTESIA, NM 14.90 V






453 *** 3/27/90 CORPUS CHRISTI, TX 2 300.00 W

466 TAZCA 5/25/90 TAZ-2066 VENEZUELA ISOSTRIPPER REBOILER 34.50 V

467 16 8/24/90 ANACORTES, WA 62.21 V

468 *** 8/24/90 ANACORTES, WA 68.54 V

470 *** 6/22/90 MCPHERSON, KS 207.52 W

474 309 8/27/90 WILMINGTON, CA 1, 4 86.300 Ho

475 19 10/25/90 SANTA MARIE, CA 1 44.600 V

476 *** 10/25/90 SANTA MARIE, CA 1 44.600 V

479 11/16/90 PORT ARTHUR, TX 1 111.760 Ho

FLUOR DANIEL

FLUOR DANIEL

FLUOR DANIEL

LITWIN ENGINEERS

C.F. BRAUM & CO.

C.F. BRAUM & CO.

TEXACO

TEXACO

ULTRAMAR

BECHTEL

SAMSUNG

SAMSUNG

AMOCO OIL CO.

FLUOR DANIEL

FLUOR DANIEL

FLUOR DANIEL

FLUOR DANIEL

FLUOR DANIEL

CCR PLAT HEATER

2C-100249

PSP-MW-1352 HYDROTREATER REACTOR CHARGE HEATER

PSP-MW-1352 HYDROTREATER CHG FRACTIONATOR FD/REBOILER

20858-100-F-001HA COKER HEATER

1574-12-141-1-13 CRUDE HEATER/ AIR PREHEAT

COKER CHARGE HEATER WITH SERVICE

1574-12-141-1-13 CRUDE HEATER/ AIR PREHEAT

4497-12-003

623813-4-0503-01

813-3-17240

RECYCLE FEED

FC 00015901

FC 00015901

COKER CHARGE HEATER

HDA RX FEED HEATER

623813-4-0503-01

212175-40501-0

HYDROCRACKER-REACTOR CHARGE HEATER #1

623813-4-0503-01

623813-4-0503-01

623813-4-0503-02

DEBUTANIZER REBOILER HEATER

3 CELL CCR PLATFORMER HEATER

FRACTIONATOR REBOILER

NAPTHA HYDROTREATER CHARGE HEATER

HYDROCRACKER-REACTOR CHARGE HEATER #2

212175-40501-0 DEPROPANIZER REBOILER

4CELL-CCR PLATFORMER HEATER

623813-4-0503-01

Page No. 8



REF. NOTE


480 11/16/90 PORT ARTHUR, TX 1 111.760 Ho

481 35 1/14/91 VENEZULA 105.000 Ho

482 *** 1/14/91 VENEZULA 105.000 Ho

483 *** 1/14/91 VENEZULA 105.000 Ho

484 *** 1/14/91 VENEZULA 105.000 Ho

485 *** 1/14/91 VENEZULA 105.000 Ho

487 14 4/19/91 YEOCHUN, KOREA 10.630 V

491 1 6/13/91 MCPHEARSON, KS 21.000 He

492 *** 6/13/91 MCPHEARSON, KS 21.000 He

493 *** 6/13/91 MCPHEARSON, KS 32.000 V

498 12 9/25/91 TULSA, OK 52.900 Ho

513 84 6/1/92 NARROWS, VA 1 11.50 Ho

514 *** 6/1/92 NARROWS, VA 1 11.50 Ho

515 *** 6/1/92 NARROWS, VA 1 11.50 Ho

516 *** 6/1/92 NARROWS, VA 1 11.50 Ho

517 *** 6/1/92 ROCK HILL, SC 1 11.50 Ho

518 *** 6/1/92 ROCK HILL, SC 1 11.50 Ho

519 *** 6/1/92 ROCK HILL, SC 1 11.50 Ho

520 *** 6/1/92 ROCK HILL, SC 1 11.50 Ho

RUST INTERNATIONAL

RUST INTERNATIONAL

RUST INTERNATIONAL

RUST INTERNATIONAL

RUST INTERNATIONAL

RUST INTERNATIONAL

RUST INTERNATIONAL

RUST INTERNATIONAL

SUN REFINING & MKT'G CO.

LUCKY PETROCHEMICAL

LITWIN ENGINEERS

LITWIN ENGINEERS

LITWIN ENGINEERS

BECHTEL

TAZCA

TAZCA

TAZCA

TAZCA

TAZCA

023-04011N

0013-

L/I NO:LALO-BA-00

4805-200-12-005

T16360

KETENE HEATERS WITH AIR PREHEAT


022-01019N KETENE HEATERS WITH AIR PREHEAT

023-04011N




023-04011N



DOUBLE FIRED COKER HEATER

4805-200-12-005

0013-

20858-100-F-001HA

0013-

HYDROTREATER/ CHARGE HEATER

0013-

4805-200-12-005 HYDROTREATER/ CHARGE HEATER

COKER HEATER

REBOILIER/ PLUS STEAM COIL

HEAVY CRUDE HEATER

HDA REACTOR FEED HEATER/DOUBLE FIRED UNIT

HEAVY CRUDE HEATER

HEAVY CRUDE HEATER

HEAVY CRUDE HEATER

0013-

HEAVY CRUDE HEATER

Item 5

ThermaTran’s Quality Assurance & Project Management

18 Pages

THERMATRAN, INC.

QUALITY ASSURANCE &

PROJECT MANAGEMENT

AUGUST 31, 2016 MANUAL 500

CONTENTS

Foreword ................................................................................................ Page 1

Section I ................................................................................................... Quality Assurance Manual

Section II ................................................................................................. Codes and Specifications

Section III ................................................................................................ Sales/Thermal Design

Section IV ................................................................................................ Project Manager

Section V ................................................................................................. Data Processing and CAD

Section VI ................................................................................................ Engineering

Section VII .............................................................................................. Production

Section VIII ............................................................................................. Procurement

Section IX ................................................................................................ Inspection

Section X ................................................................................................. Non-conformance

Section XI ................................................................................................ THERMATRAN Specifications

ii

INTRODUCTION

THERMATRAN, INC. (THERMATRAN) utilizes a computer-based project management system. This system complies inputs from each department to provide a comprehensive accumulation of information. This allows THERMATRAN to detect and correct problem areas well before they jeopardize the ship date.

The Master Job Schedule is the nucleus of this system. It contains the scheduled dates for completion of each task, as well as the dates actually completed. The tasks range from drawings, weld procedures, steel and coil fabrication, through data books. Periodic status checks of each task are requested of each department manager by the system. Since the system has automatic prompts, the possibility of an item being overlooked are greatly reduced.

The Engineering Drawing Report helps assure that all the fabricators involved in a project are working from the latest revised drawings. Since this list is generated and distributed weekly, and contains all the drawings for a given project, there is little chance that our fabricators will build equipment per outdated drawings. Couple this with our Inspection Department check against this list, giving THERMATRAN an as-built drawing for issue at the time of shipment.

The Production Schedule is the agenda for the weekly production meetings. It contains a brief job description as well as a weekly update of fabrication and critical path items. These weekly meetings play an important role in the project management team's ability to recognize potential delays in the project schedule and take the necessary steps to maintain the project completion date as outlined in the Master Job Schedule.

THERMATRAN QUALITY ASSURANCE & PROJECT MANAGEMENT MANUAL

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FOREWORD

THERMATRAN, Inc. (THERMATRAN) designs and, through the use of sub-contractors, fabricates and installs direct fired heaters, incinerators, heat recovery equipment and control systems, and related equipment for the petroleum and petrochemical industries.

It is the policy of THERMATRAN, Inc. to maintain a high quality of design, materials and workmanship relative to fired heaters and incineration systems fabrication. This manual sets forth the policies utilized by THERMATRAN, Inc. to ensure this quality.

It is the collective responsibility of the department managers to ensure compliance with the requirements of this manual. All managers have a responsibility to implement these requirements and to ensure a continuing compliance by active participation of all employees.

The purpose of this manual is to outline a corporate program by which the corporation will function. This program is intended to be a guide for normal activities, but special situations may require deviation from this manual. This deviation must, however, be an intentional and planned event that is closely monitored by the responsible managers.


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SECTION I - CONTROL AND REVISION OF THE MANUAL The control of this manual will rest with the Engineering Department. Engineering will issue controlled copies which will be serialized and recorded in a log as a minimum. Controlled copies will be issued to all department managers and THERMATRAN, Inc. inspection personnel.

Uncontrolled copies will be issued to THERMATRAN, Inc. sub-contractors and to customers upon request. While the uncontrolled copies will be current when they are issued, they may or may not be updated to include later revisions.

Revisions to this manual may range from one page to the entire manual. Suggested revisions may be submitted to Engineering by the departmental managers or the Manager of Quality Assurance, but must have the final approval of the corporate management.

SECTION II - CODES AND SPECIFICATIONS

THERMATRAN, Inc. will design and fabricate to the latest versions of the following codes and specifications unless otherwise stated.

ITEM CODE

Coil American Petroleum Institute (API) STD-530 American National Standards Institute (ANSI) B31.3 American Society of Mechanical Engineers (ASME) Sec. I, Sec. VIII, Div. 1 or Div. 2 when specified on the API Data Sheet.

Materials American Society of Testing & Materials (ASTM) ASME Sec. II THERMATRAN Specifications (See Section XI)

Structural Steel American Institute of Steel Construction, Inc. (AISC) American Welding Society (AWS) THERMATRAN Specifications (Section XI)

Wind & Earth Quake Loads ANSI A58.1 or Uniform Building Code (UBC)

Tube Supports THERMATRAN Specifications (See Section XI)

Paint THERMATRAN Specifications (See Section XI)

Steel Fabrication THERMATRAN Specifications (See Section XI)

Crating THERMATRAN Specifications (See Section XI)

Castable THERMATRAN Specifications (See Section XI)

General API Standard 560 - Process Fired Heaters * API RP-533 - Air Preheat System *

* Except as modified by THERMATRAN Standards

All of the above specifications shall be adhered to as a minimum.


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Customer specifications and/or local codes and laws, when more severe, shall govern.

SECTION III - THERMAL DESIGN

1.It is the responsibility of the Thermal Design Department to originate the data sheets and related documents, to accurately describe each job and, in general, furnish sufficient information to the Operations Manager, Engineering, Procurement, Production and Quality Assurance to enable them to provide a final product in compliance with the purchase order, THERMATRAN Standards, National or International Codes and Specifications, and all governing laws.

2.Thermal Design is also responsible for the thermal and initial mechanical design of the coil, geometry of the heater and preliminary scheduling. It is the responsibility of Thermal Design to stay in communication with the Project Manager and Engineering to ensure realistic projections of project schedules.

3.Thermal Design will maintain a master file for each job that will include but not be limited to the following:

a. Sales Summary

b. Purchase order and job specification including data sheets.

c. Correspondence relative to the job.

d. Inquiry

e. Proposal

f. Process, thermal and coil mechanical calculations.

g. Job Estimate

h. Record of job activity that effects final job cost changes.

4. Thermal Design will initiate all information for the master files.

SECTION IV - PROJECT MANAGER

1. The Project Manager will act as a continuing liaison between the Customer, Sales, Thermal Design,Engineering, Production, Operations, Procurement, Quality Assurance and Accounting.

2. Additional responsibilities of the project manager will be as follows:

a. Ensure a complete understanding of job requirements is attained by all departments.

b. Provide necessary data to Production to ensure that proper provisions for shipping are made.


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c. Review all requisitions originated by Engineering for specification and budget compliance.

d. Chair a weekly production meeting with representatives from Engineering, Production,Procurement, Quality Assurance and Accounting. The purpose of this meeting is to review jobprogress versus job schedules on a consistent and timely basis and to forecast and plan forpotential delays in order to maintain project completion.

e. Coordinate job changes during the period between job initiation and shipment.

f. Coordinate any field modifications that may be necessary.

SECTION V - DATA PROCESSING

1. Data Processing, working with the other departments, will generate and maintain computerprograms. These programs will include, but not be limited to:

a. Process, thermal and mechanical design

b. Estimating

c. Drawing List

d. Scheduling

e. Cost Control

f. Procurement

g. Expediting

h. Shipping

2. Data Processing will maintain adequate documentation of the computer programs.

3. Computer Aided Drafting (CAD) will be maintained by Engineering, interfaced with Data Processing.These departments will be responsible for generating the various patterns. The patterns will include,but not be limited to:

a. Drawing Standards

b. Forms

c. General Arrangement Drawings

d. Detail Drawings

e. Proposal Drawings

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SECTION VI - ENGINEERING

1. It is the responsibility of Engineering to provide mechanical designs, drawings, standards and requisitions to meet the applicable job specifications as designated by Thermal Design.

2. Additional responsibilities of the Engineering Department are as follows:

a. Review customer specifications and itemize the points that deviate from THERMATRAN

standards. Distribute the specifications to the appropriate departments for compliance using RFS 1-1.

b. Specify all production testing and post-weld heat treatment requirements. This data will be

shown on the General Arrangement drawings.

c. Issue all drawings and revisions as required, to Production, Procurement, Inspection and to the customer.

d. Review final data booklets for accuracy and completeness.

e. Furnish shipping clearance data, overall size and weight of major pieces to Production to enable

them to arrange for shipment.

f. Furnish erection and start-up data to field.

g. Maintain engineering files and keep accurate records of transactions throughout a job that effect design and final cost.

h. Initiate and maintain design and fabrication standards.

i. Design and maintain drawings for tube supports.

j. Maintain the latest editions with addenda of codes and standards for use by all departments.

k. Resolve any questions regarding fabrication and design versus project specifications.

l. Review any areas of non-conformance that are submitted by inspection.

m. Review and approve vendor drawings and data.

SECTION VII - PRODUCTION

1. Production is responsible for meeting the job schedule.

2. Production will generate actual project schedule dates considering material availability, shop space, Engineering load, etc., making every effort to meet the initial schedule generated by the Project Manager. Any conflict with the initial schedule will be brought to the attention of the Project Manager immediately and resolved. Production will issue a listing of status and ship date for each


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job weekly to Sales, Thermal Design, Engineering, Procurement, Accounting and Quality Assurance prior to the production meeting.

3. When specifically required by the customer, Production will issue progress reports to the customer in the form and frequency they require.

4. It is the ultimate responsibility of Production to expedite as required to maintain job schedules.

5. Production will arrange for shipment to the field. It is Production's responsibility to be aware ofspecial requirements that may be required by the customer relative to shipping and to documentsame in writing, including all necessary special shipping.

6. Production will maintain a constant line of communication between all parties engaged in a givenproject. This includes not only those engaged in fabrication, but also with the field during the erection phase of the project.

7. Production will attend pre-inspection meetings with THERMATRAN sub-contractors and thecustomer.

8. Production will arrange for competitive bidding of the shipment and compliance with the shipmentbudget.

9. Work with sales/estimating to maintain an up to date estimating system.

SECTION VIII - PROCUREMENT

1. It is the responsibility of Procurement to issue purchase orders for all fabrication and services forprojects to meet the job schedule and customer specifications. Procurement will purchase allmaterials as requisitioned by Engineering.

2. Procurement must maintain all material records required, including mill test reports, receiving tickets,bills of lading and any Material Safety Data Sheets (MSDS).

3. Additional responsibilities of procurement are as follows:

a. Maintain an accurate listing of any excess materials and incorporate them into active projects assoon as possible.

b. Maintain a listing of all tube support patterns owned by THERMATRAN, Inc. and which foundryis in possession of them.

c. Perform shop surveys along with Quality Control of potential future sub-contractors.

d. Transmit material data reports when received to Quality Control for compliance to the purchaseorders and applicable standards and codes.

e. Maintain a record for other departments of all qualified vendors.


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f. Prepare quarterly unit cost report.

SECTION IX - QUALITY CONTROL

1.0 SCOPE

1.1 The requirements of this section apply to the fabrication of all equipment designed and purchased by THERMATRAN, Inc., and shall be used in conjunction with the applicable codes, specifications and standards that pertain to each order.

2.0 GENERAL

2.1 Quality Control shall arrange for and chair all necessary pre-fabrication meetings for any fabricators THERMATRAN is working with on the particular project.

Quality Control shall provide a written agenda to all attending parties one week in advance of the meeting.

Quality Control shall be responsible for generating an attendance list and for keeping detailed notes of the meeting. The attendance list and typed notes should be distributed to all parties. This should also include the project Quality Control plan.

As a minimum those in attendance should include:

· THERMATRAN - Quality Control Manager· THERMATRAN - Project Manager· Fabricator - Quality Control Manager/Chief Inspector· Fabricator - Project Manager· Customer - Quality Control Representative

It is recommended, but not mandatory, that the THERMATRAN Engineering Manager and customer's Project representative attend the meeting.

The primary burden of inspection rests with the fabricator and THERMATRAN's role is to assure that he has all necessary specifications, data sheets, drawings or other necessary documents to properly fabricate and complete the required work.

THERMATRAN will from time to time perform random spot inspections to help establish the level and detail of inspection expected of the fabricator.

2.2 Each item of equipment shall be spot inspected during fabrication and after completion by authorized THERMATRAN, Inc. Quality Control personnel.

2.3 The responsibility and authority of the inspection for all equipment shall be a shown in the attached THERMATRAN, Inc. "QUALITY ASSURANCE AND QUALITY CONTROL PLAN".

2.4 Review all necessary MTR's PMI's and other documentation to certify materials used in


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fabrication and supply are in compliance with the customer purchase order and applicable standards and codes. When this is not the case Quality Control must immediately notify the THERMATRAN Project Manager and Engineering Director.

3.0 ACCESS

3.1 THERMATRAN, Inc. Quality Control personnel shall be given access to all necessary facilities and accommodations by the vendor to perform or monitor the required inspections and tests. This access shall include all relevant inspection and testing records, reports, radiographs and charts.

4.0 PERSONNEL QUALIFICATIONS

4.1 All THERMATRAN, Inc. Quality Control personnel who shall perform non-destructive tests and/or shall evaluate for acceptance the non-destructive Test Method results, shall be qualified and certified in accordance with the requirements of the THERMATRAN, Inc. "NON-DESTRUCTIVE TESTING-PERSONNEL QUALIFICATION AND CERTIFICATION PROGRAM."

4.2 All THERMATRAN, Inc. Quality Control personnel who shall interpret and evaluate radiographic film, shall be qualified and certified in accordance with the requirements of the THERMATRAN, Inc. "RADIOGRAPHIC FILM INTERPRETATION AND EVALUATION: SNT-TC-1A PROGRAM".

5.0 EXTENT OF QUALITY CONTROL

5.1 The amount and type of inspection and testing required, shall be shown in the Fabricator Quality Assurance and Quality Control Plan, and its attachments, and shall be determined by the requirements of the applicable codes and specifications.


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QUALITY ASSURANCE AND QUALITY CONTROL PLAN

1.0 SCOPE

This plan has been established to ensure that the material used in and the fabrication of, all fired heaters and incineration systems designed by THERMATRAN and sub-contracted for fabrication, are built in accordance with the applicable codes, THERMATRAN standards, and customer specifications.

2.0 AUTHORITY AND RESPONSIBILITY

THERMATRAN assumes responsibility for the quality assurance and control related to the fabrication of Fired Heaters and Incineration systems and their design. This responsibility includes verifying that all sub-vendors have acceptable quality control and inspection plans and that these plans are being adhered to.

The Quality Assurance Department has the authority to identify quality control problems, initiate and recommend solutions and, when necessary, stop work in process or shipment when there is reasonable doubt concerning the quality of products. It is the responsibility of the Manager of Quality Assurance to ensure that only products meeting THERMATRAN and their customer's standards are fabricated by the sub-suppliers.

3.0 SPECIFICATIONS AND REQUIREMENTS

The Engineering Department has complete authority and responsibility for in-process and finished product specifications for all products designed by THERMATRAN. The THERMATRAN "Bill of Material" for each item required on the specific customer order will be completed and distributed to ensure that each department has through understanding of what is required on each customer order.

3.1 Company, Customer and Code Specifications

THERMATRAN specifications are produced, maintained, and distributed by the Engineering Department.

Customer specifications are reviewed by the Engineering and Quality Assurance Departments to ensure their compliance to the specific project. The applicable specifications are then distributed to the Purchasing Department to be issued with the inquiries to the sub-vendors.

The applicable codes will be shown on the THERMATRAN data sheets and the Engineering Department will be responsible for ensuring that the codes are shown on the drawings and necessary "Bills of Material".

3.2 Material Specifications

The Engineering Department is responsible for initialing and dating the "Bill of Material


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Checklist" (Form E-18 attached) as each bill of material is completed and issued to the Purchasing Department. Each bill of material will contain the ASME/ASTM material specification and/or applicable Customer specification.

4.0 DRAWINGS AND ENGINEERING CHANGE NOTICES

The Engineering Department will design, authorize, and issue the General Arrangement drawings and the steel design drawings on all projects. Dimensions and tolerances specified on the drawings are the complete responsibility of the Engineering Department and cannot be changed, altered, or modified except by Engineering. It is the responsibility of the Engineering Supervisor or Project Manager to notify the Project Designer of any changes required as a result of customer revisions, material substitutions, fabrication conflicts encountered or other reasons requiring a change to be made. The Engineering Department will issue the revised drawings to the customer for their review and/or approval, and to the Purchasing Department for transmittal to the sub-supplier. Only the Engineering Department maintains a detail drawing file to ensure that only the most current drawings reach the sub-supplier.

5.0 SUB-SUPPLIER QUALIFICATION AND SURVEILLANCE

5.1 It is the responsibility of the Engineering and Quality Assurance Departments to directly assist Purchasing in developing a listing of approved vendors for items that will be used.

5.2 At the request of Purchasing, source inspections will be conducted at a sub-suppliers plant. Such inspections will verify that the vendor, as standard practice, is producing a product that meets both the technical specifications and the quality level required. A re-inspection of an approved vendor may be scheduled based on actual performance of the purchased items.

5.3 Using the Acceptance and Rejection Report, a record of deficiencies will be kept for each purchased item. When, in the opinion of Quality Assurance the number of deficiencies becomes too great, the Purchasing Department will be notified, who in turn will notify the sub-supplier. The sub-supplier must then submit proof of corrective action or the Quality Assurance Department will recommend that he be removed from the approved vendor list.

6.0 QUALITY CONTROL PROCEDURES

6.1 Organization

The project inspector will report directly to the Manager of Quality Assurance, who in turn is responsible to the Director of Engineering. The Quality Assurance Manager will interface with the Managers of Production and Procurement concerning the delivery and quality of THERMATRAN purchased materials.

All managers of responsibility will receive information concerning the status of material and fabrication, as well as quality control information. This information will be reported during


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the weekly THERMATRAN production meetings, unless more immediate attention is required, in which case, the line of responsibility will be immediately notified in writing.

6.2 Pre-Fabrication Meeting

During the pre-meeting to be held with the client, THERMATRAN, and sub-suppliers prior to the start of fabrication, the quality control procedures applicable to the specific project shall be reviewed. These shall include, but not be limited to, the following:

a. Review the purchase order to insure that all inspection requirements are properlyspecified.

b. Verify that the sub-vendor(s) has a Quality Assurance Manual that is acceptable toTHERMATRAN and the client, and that the contents of the manual are being followed.

c. Introduce THERMATRAN "Inspection Checklist" and establish the applicableinspection, witness, and hold points, as well as, the required vendor data documents.

d. Establish the amount of inspection to be conducted by the customer, and establish amethod for contacting the customer for the purpose of conducting joint inspection visits.

6.3 Inspection and Testing

It is the policy of THERMATRAN to inspect and test all of the equipment designed by THERMATRAN and sub-contracted for fabrication, to the applicable codes and specifications.

The type and amount of inspection to be performed for each sub-supplied item will be shown on the THERMATRAN "Vendor Source Inspection Requirements" form. (Copy Attached).

Inspection and testing will include, but not be limited to, the following:

a. Review mill test reports for conformance to the applicable ASTM specification.

b. Review actual received material against mill test reports and purchase specifications.

c. Review the weld procedures, qualifications and welder qualifications.

d. Witness the required non-destructive examinations, to the extent shown on the"Inspection Checklist". Occasionally conduct sample audit tests to verify accuracy ofvendor tests, particularly Brinell Hardness Tests.

e. Witness required pressure testing.

f. Perform the visual and dimensional inspections to the extent specified by theTHERMATRAN quality Assurance Manual, unless stricter inspections are required bythe client specifications. Upon completion of each inspection visit issue a "Punch List"itemizing any fabrication errors, omissions, or other discontinuities encountered.


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g. Perform inspection of shipping preparation.

h. Perform final inspection and issue an "Inspection Release". (Note: An inspectionrejection is to be issued if fabrication errors are not corrected promptly as requested.)

i. Request and receive all required vendor data documents from the sub-vendors.Thereafter transmit these to the Job Manual and data book preparation person(s) withinthe job schedule.

6.4 Documentation

Upon completion of the final inspection, and all required inspection, the project inspector shall prepare the following documents (if applicable) and issue them to the THERMATRAN "Vendor Data Document" department.

a. Dimensional Inspection Certification

b. Visual Inspection Certification

c. NDE Certifications

d. Hydrotest Certification

e. Heat Treatment Charts

f. Hardness Records

g. Radiograph Reader Sheets

h. Manufacturer's Data Report

i. Nameplate Rubbings

j. Material Test Reports

k. Accurate Weld Maps

* Inspection from time to time will conduct audits of these documents to assure that they agree withthe actual and specific number of inspection/test points. For example: Does the stress relief chart account for all welds that were stress relieved?


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SECTION X - NON-CONFORMANCE 1.0 SCOPE 1.1 This section defines the system for controlling and correcting non-conforming material and

fabrication. Non-conformance shall be defined as any material and/or fabrication that does not meet the requirements of the applicable code, specification, standard or drawing.

2.0 RESPONSIBILITY 2.1 The THERMATRAN Quality Control Department shall have the primary responsibility of

identifying non-conformance, but it may be identified by any THERMATRAN, Inc. employee.

3.0 MATERIAL NON-CONFORMANCE 3.1 When the THERMATRAN, Inc. inspector finds any materials which do not conform to the

requirements of the applicable code, specification, or standard, it shall be immediately reported to the Engineering and Procurement departments.

3.2 All non-conforming materials shall be so tagged, segregated from acceptable material, and

withheld from use, immediately upon discovery. 3.3 Action to correct or replace non-conforming material shall begin immediately. 3.4 The Procurement Department shall have the option of replacing the material with

conforming material or requesting the Engineering Department to approve a recommended method of correcting the non-conformance.

3.5 The Engineering Department shall review and approve all recommended methods for

upgrading non-conforming material to an acceptable level. 3.6 The quality Control Department shall witness all corrective action and required testing for

the upgrading of non-conforming material, and give final approval, in writing, of the corrective action.

3.7 Any material that has not been, or cannot be upgraded to an acceptable level shall be rejected,

in writing, by Quality Control. 4.0 FABRICATION NON-CONFORMANCE 4.1 Any fabrication that does not conform to the requirements of the drawings, codes, or

specifications, and is considered by the Inspector to be minor, shall be itemized on a "punch list" and issued to the fabricator for correction.

4.2 Any non-conforming fabrication, that is considered major by the inspector, shall be brought

to the attention of the Project Manager for resolution.


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4.3 Any non-conforming fabrication that is disputed by the fabricator and/or the customer inspector shall be brought to the attention of the THERMATRAN, Inc. Engineering Department for resolution.

4.4 In the event the fabricator cannot or will not correct a fabrication non-conformance, the

THERMATRAN, Inc. inspector shall issue a "Rejection". 4.5 Any storage of materials that does not conform. 5.0 SHIPMENT 5.1 All non-conforming materials and fabrication shall be corrected to the satisfaction of the

THERMATRAN, Inc. Quality Control Department before a release for shipment will be issued.

Item 6

Photos of Typical ThermaTran Fired Heaters – 8 Items – 26 Pages

thermatran information booklet 2017€¦ · thermatran information booklet . 2017 . table of...

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