technical committee on fundamentals of combustion …recommended specific language and instructed...

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Technical Committee on Fundamentals of Combustion Systems Hazards Date: March 5, 2010 To: Technical Committee on Fundamentals of Combustion Systems Hazards From: Denise Beach, Staff Liaison/Senior Engineer Re: Agenda Package – March ROC Meeting Enclosed is the agenda package for the March 18-19, 2010 meeting in Tampa, FL for the Report on Comments (ROC) meeting. Please ensure that you have reviewed the comments in advance, not only for technical merit, but also if you believe there are any other committees to which duplicate comments should be sent. The agenda and comments will be posted on the committee webpage. Some items to bring to the meeting include: Agenda packet with comments; your copy of the NFPA 85 Fall 2010 Report on Proposals; your copy of NFPA 85; any previous copies of NFPA 85 you may wish to reference. Optional items that are sometimes useful include previous ROP/ROCs if handy. If you have any questions or comments, please feel free to reach me at (617) 984-7501 or by e-mail at [email protected]. You can reach the Fundamental TC Chair, Dale Evely at (205) 992-6649 or by e-mail at [email protected] . Live Meeting Web Access . TC Members participating via Live Meeting should have received a separate email with instructions on connecting through the web. If you do not have the email, please follow these steps to connect to the meeting: 1. Copy this address and paste into your web browser: https://www.livemeeting.com/cc/nfpa/join 2. Copy and paste the required information: Meeting ID: B2JSGT Entry Code: F]hp;\?7T Location: https://www.livemeeting.com/cc/nfpa 3. Dial the conferencing service directly, and enter the participant code shown below: Toll-free: +1-8773202367 Toll: +1-8773202367 Participant Code: 1959301

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Page 1: Technical Committee on Fundamentals of Combustion …recommended specific language and instructed the BCS-SBB Technical Committee to address the issue and provide input to the BCS-FUN

Technical Committee on Fundamentals of Combustion Systems Hazards

Date: March 5, 2010 To: Technical Committee on Fundamentals of Combustion Systems Hazards From: Denise Beach, Staff Liaison/Senior Engineer Re: Agenda Package – March ROC Meeting Enclosed is the agenda package for the March 18-19, 2010 meeting in Tampa, FL for the Report on Comments (ROC) meeting. Please ensure that you have reviewed the comments in advance, not only for technical merit, but also if you believe there are any other committees to which duplicate comments should be sent. The agenda and comments will be posted on the committee webpage. Some items to bring to the meeting include: Agenda packet with comments; your copy of the NFPA 85 Fall 2010 Report on Proposals; your copy of NFPA 85; any previous copies of NFPA 85 you may wish to reference. Optional items that are sometimes useful include previous ROP/ROCs if handy. If you have any questions or comments, please feel free to reach me at (617) 984-7501 or by e-mail at [email protected]. You can reach the Fundamental TC Chair, Dale Evely at (205) 992-6649 or by e-mail at [email protected]. Live Meeting Web Access. TC Members participating via Live Meeting should have received a separate email with instructions on connecting through the web. If you do not have the email, please follow these steps to connect to the meeting: 1. Copy this address and paste into your web browser: https://www.livemeeting.com/cc/nfpa/join 2. Copy and paste the required information: Meeting ID: B2JSGT Entry Code: F]hp;\?7T Location: https://www.livemeeting.com/cc/nfpa

3. Dial the conferencing service directly, and enter the participant code shown below: Toll-free: +1-8773202367 Toll: +1-8773202367 Participant Code: 1959301

Page 2: Technical Committee on Fundamentals of Combustion …recommended specific language and instructed the BCS-SBB Technical Committee to address the issue and provide input to the BCS-FUN

Technical Committee on Fundamentals of Combustion Systems Hazards

AGENDA

Tampa Electric Company 702 North Franklin Street

Tampa, FL 33602 March 18-19, 2010

1. Chair’s welcome, call to order, and opening remarks at 8:00 a.m. (TECO advises that

attendees should be able to enter security starting at 7:30 a.m. Attendees can enter the lobby and access the cafeteria as early as 7:00 a.m. A continental breakfast will be available in the meeting room.)

2. Self-Introduction of Committee Members and Guests 3. Approval of Minutes from the May 27-28, 2009 ROP Meeting in Atlanta, GA. See E-

Committee web page to view. 4. Staff Liaison Report A. Committee membership update (For the period May 1, 2009 – March 5, 2010)

Name Category Change Date Allan Zadiraka M (Principal) Resignation 12/09/2009 Peter Matthews I (Principal) Resignation 10/06/2009 John Gilbert I (Principal) Appointment 08/05/2009 Dennis Mason I (Principal) Re-Appointment 08/05/2009 Mark Ratcliffe SE (Principal) Appointment 08/05/2009 William Rucki M (Alternate to T.

Jablkowski) Appointment 08/05/2009

Kenneth Hurlburt M (Alternate to B. Basile) Appointment 10/27/2009 Daniel May SE (Alternate to M. Walz) Appointment 10/27/2009 Gail Lance M (Principal) From Alt to P 03/02/2010

(Total Voting Members – 24; M=33%, SE=33%, I=17%, U=17%) B. Revision Cycle Review and timeline (Attachment A) 5. Old Business 6. New Business A. Review of public comments (see enclosed Acrobat file) B. Creation of Committee Comments (See Attachment B for TCC Notes)

i. Interlock System Initiation - The TCC revised the action on Proposal 85-30 (25) to include language accepted in Proposal 85-31 (CP9). The TCC also recommended that the BCS-FUN and BCS-HRS Technical Committees reconsider the language of 85-31 and 85-110(CP105) respectively, in light of the new definition for transmitter.

Page 3: Technical Committee on Fundamentals of Combustion …recommended specific language and instructed the BCS-SBB Technical Committee to address the issue and provide input to the BCS-FUN

ii. Minimum purge rate – The TCC instructed the BCS-FUN Technical Committee to reconsider Proposal 85-49 (43) in light of the use of the term “minimum purge rate” by the BCS-MBB Technical Committee in Proposal 85-69 (CP4) and others.

iii. Continuous Trend Display – The TCC instructed the BCS-SBB Technical Committee to establish a task group to reconsider Proposals 85-51 (20), 85-52 (65), and 85-53 (CP401) for the Report on Comments phase. The TCC recommended specific language and instructed the BCS-SBB Technical Committee to address the issue and provide input to the BCS-FUN Technical Committee prior to the BCS-FUN ROC meeting in March 2010.

iv. Interlock Bypass - The TCC reviewed Proposal 85-56 and requested that the BCS-FUN Technical Committee review the issue of “interlock bypass” for possible expansion of section 4.5.4.

7. BCS-MBB Aluminum Material Task Group (Attachment C) 8. Other Items? 9. Date/Location of Next Meeting. (NFPA 85 is currently on a 4-year revision cycle.) 10. Adjournment.

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ATTACHMENT A: ROP AGENDA

NFPA 85 Revision Cycle Fall 2010

NFPA 85 F2010 (last cycle F06) [BCS-AAC]

Intent to enter cycle January 9, 2009 Proposal Closing May 8, 2009 (May 29 orig date) ROP Published and Posted December 28, 2009 Comment Closing March 5, 2010 ROC Published and Posted August 27, 2010

ROC TC Meetings (between March 5 and April 9, 2010) FUN ROC (Tampa) – 2 days March 18-19, 2010 HRS ROC (Orlando) – 2 days March 25-26, 2010 MBB ROC (Tempe) – 2 days March 30-31, 2010 FBB ROC teleconference/Live Meeting April 5, 2010 PFS ROC teleconference/Live Meeting April 2, 2010 SBB ROC teleconference/Live Meeting April 6, 2010 STO ROC teleconference/Live Meeting April 2, 2010 TCC ROC (Barberton, OH, tentative) June 2-3, 2010 Intent to make motion (ITMAM) closing October 22, 2010 Issuance of standard - NO controversy January 28, 2011 (publ. bit later) NFPA WSCE Meeting with NITMAM June 4-9, 2011

Issuance of Standard – with controversy July 29, 2011 (published bit later)

Page 5: Technical Committee on Fundamentals of Combustion …recommended specific language and instructed the BCS-SBB Technical Committee to address the issue and provide input to the BCS-FUN

Report on Comments – November 2010 NFPA 85_______________________________________________________________________________________________85- Log #CC1 BCS-FUN

_______________________________________________________________________________________________Technical Committee on Fundamentals of Combustion Systems Hazards,

85-7Revise text as follows:

***Insert 85_LCC1_R Here***

References and extracts are updated to conform to the NFPA Regulations Governing CommitteeProjects.

AISC publications are deleted in accordance with proposal 85-103.ANSI K61.1 and ANSI/FCI 70.2 are moved to new groupings reflecting the Standards Developer instead of the ANSI

designation.Extract tags for the following definitions can be updated editorially as no change has been made to the source

definition:3.3.164.4 Check Valve.3.3.57 Explosion Vent.3.3.64 Flame.3.3.73.9 Municipal Solid Waste (MSW).3.3.46 Damper.NFPA 69 has modified the definition for inert gas as follows:3.3.21.1 Inert Gas. A gas that is noncombustible and nonreactive. [69, 2008]In a poll of BCS TC chairmen, the consensus was to retain the current NFPA 85 definition and delete the extract tag

rather than accept the updated definition from NFPA 69.ABMA 202 has been withdrawn replaced with ABMA 203, A Guide to Clean and Efficient Operation of

Coal-Stoker-Fired Boilers. ABMA no longer sells or makes available ABMA 202. Robert Morrow of Detroit StokerCompany and member of the BCS-STO Technical Committee reviewed ABMA 203 and confirmed that it is anacceptable replacement reference for the purpose of Annex F. Annexes F and N are therefore updated editorially toreference the replacement standard.

_______________________________________________________________________________________________85- Log #6 BCS-FUN

_______________________________________________________________________________________________Dale P. Evely, Southern Company Services, Inc.

85-106Revise text to read as follows:

An HRSG, heat exchanger, or emissions control system, alone or incombination, and their associated ductwork All ductwork from the combustion turbine exhaust to the stack inlet. ,including any emission control systems contained within the exhaust flow path.

This definition was proposed to be revised by the BCS-HRS Technical Committee during their ROPmeeting but the proposed wording was a bit ambiguous. The above proposed revision for this definition needs to bereviewed by both the BCS-HRS TC as well as the BCS-FUN TC.

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Report on Comments – November 2010 NFPA 85_______________________________________________________________________________________________85- Log #27 BCS-FUN

_______________________________________________________________________________________________Marcelo M. Hirschler, GBH International

85-12Revise text as follows:The method of interconnecting signals or interlocks to a logic system or between logic systems

using a dedicated interconnection for each individual signal. When the term hardwired is applied to the logic systemitself it is the method of using individual devices and interconnecting wiring to program and perform the logic functionswithout the use of software based logic solvers.

A.3.3.81 When the term hardwired is applied to the logic system itself it is the method of using individual devices andinterconnecting wiring to program and perform the logic functions without the use of software based logic solvers.

NFPA definitions must be in a single sentence. The proposed definition is in two sentences. Thesecond sentence should be located in a different section or, if informational, in Annex A.

I am the chair of the NFPA Advisory Technical Committee on Glossary of Terminology but this comment is notsubmitted on their behalf because we have not had the opportunity to discuss it.

_______________________________________________________________________________________________85- Log #28 BCS-FUN

_______________________________________________________________________________________________Marcelo M. Hirschler, GBH International

85-13Revise text to read as follows:

3.3.94* Logic System. The decision-making and translation elements of the burner management system. A logicsystem provides outputs in a particular sequence in response to external inputs and internal logic. Logic systems arecomprised of the following: (1) hardwired systems wired in direct electric series — individual devices and interconnectingwiring — and (2) microprocessor-based systems — (a) computer hardware, power supplies, I/O devices, and theinterconnections among them; and (b) operating system and logic software.

A.3.3.94 A logic system provides outputs in a particular sequence in response to external inputs and internal logic.Logic systems are comprised of the following: (1) hardwired systems wired in direct electric series — individual devicesand interconnecting wiring — and (2) microprocessor-based systems — (a) computer hardware, power supplies, I/Odevices, and the interconnections among them; and (b) operating system and logic software.

NFPA definitions must be in a single sentence. The definition of logic system is in two sentences. Thesecond sentence should be located in a different section or, if informational, in Annex A.I am the chair of the NFPA Advisory Technical Committee on Glossary of Terminology but this comment is notsubmitted on their behalf because we have not had the opportunity to discuss it.

_______________________________________________________________________________________________85- Log #29 BCS-FUN

_______________________________________________________________________________________________Marcelo M. Hirschler, GBH International

85-8Revise text as follows:

NFPA definitions must be in a single sentence and should not contain requirements associated withthe standard. The proposed definition is in two sentences, with the second sentence containing a requirementassociated with section 8.8.4, which is inappropriate in a definition and, if desired, must be located in a different sectionor, if informational, in Annex A.I am the chair of the NFPA Advisory Technical Committee on Glossary of Terminology but this comment is notsubmitted on their behalf because we have not had the opportunity to discuss it.

2Printed on 3/11/2010

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Report on Comments – November 2010 NFPA 85_______________________________________________________________________________________________85- Log #30 BCS-FUN

_______________________________________________________________________________________________Marcelo M. Hirschler, GBH International

85-9Revise text as follows:

NFPA definitions must be in a single sentence and should not contain requirements associated withthe standard. The proposed definition is in two sentences, with the second sentence containing a requirementassociated with section 8.8.4, which is inappropriate in a definition and, if desired, must be located in a different sectionor, if informational, in Annex A.

I am the chair of the NFPA Advisory Technical Committee on Glossary of Terminology but this comment is notsubmitted on their behalf because we have not had the opportunity to discuss it.

_______________________________________________________________________________________________85- Log #25 BCS-FUN

_______________________________________________________________________________________________John Van Name, URS - Washington Division

85-27Revise text to read as follows:

(6) Where the common component does not contain a possible ignition source, a bypass shall not be required, as longas Open Flow Path requirements and emergency shutdown air flow requirements are met. The common tie point shallnot permit reverse flow in any path under any conditions.

When two or more boiler outlets are tied together, it is possible to pressurize the connection pointeither by design or excursion. Positive pressure at the common component eliminates an open flow path (3.3.104),permits products of combustion from a running unit to enter a starting unit or a unit experiencing an emergencyshutdown with loss of fans, and also prevents the unburned fuel and products of combustion from exiting thecombustion chamber and gas paths via passive means when fans are lost. The most serious emergency condition inNFPA 85 is compromised by the present wording. This comment does not pertain to a specific type of equipment; itpertains to the requirements of any combustion products removal subsystem. Item (6) negates item (5) and this loopholehas been used to design systems that create safety issues for unit purge, emergency shutdowns, inspections andmaintenance, and to flagrantly violate the basic tenet of purge.

Chapter 4 presently quotes 6.6.3.2.2, 6.7.3.2.2 and 6.8.3.2.2, but specific references in the original comment havebeen replaced with definitions and references used throughout the document.

3Printed on 3/11/2010

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Report on Comments – November 2010 NFPA 85_______________________________________________________________________________________________85- Log #4 BCS-FUN

_______________________________________________________________________________________________Dale P. Evely, Southern Company Services, Inc.

85-29

Vents from systems operating at different pressure levels shall not be permitted to be manifolded together.Vents from systems served from different pressure reducing stations shall not be manifolded together.Vents from different boilers or HRSGs shall not be permitted to be manifolded together.Vents from systems using different fuel sources shall not be permitted to be manifolded together.Header vents shall only be permitted to be manifolded together with other header vents and only when

operated and tripped in parallel.Burner vents shall only be permitted to be manifolded together with other burner vents.Igniter vents shall only be permitted to be manifolded together with other igniter vents.Lance vents shall only be permitted to be manifolded together with other lance vents.

The language proposed by the BCS-FUN TC is in conflict due to a liberal use of cut and paste; theabove addresses this.

_______________________________________________________________________________________________85- Log #16 BCS-FUN

_______________________________________________________________________________________________Technical Correlating Committee on Boiler Combustion System Hazards,

85-31The TCC instructs the BCS-FUN Technical Committee to consider changing the terminology

"continuously variable process signals" to "process transmitters" in light of the new definition 3.3.159 for Transmitter.This is a direction from the Technical Correlating Committee on Boiler Combustion System Hazard in

accordance with 3.4.2 and 3.4.3 of the Regulations Governing Committee Projects.

_______________________________________________________________________________________________85- Log #5 BCS-FUN

_______________________________________________________________________________________________Dale P. Evely, Southern Company Services, Inc.

85-45Revise text to read as follows:

Signals and the manually operated devices specified in 4.6.3.2.4(8) that initiate mandatory master fuel tripsshall be hardwired. hard wired.

A 4.6.7 Signals that initiate mandatory master fuel trips originate directly from hardwired interlocks or from signalsdeveloped by the burner management system logic. The required operator initiated trip (e.g. pushbutton or manualswitch) is required to be hardwired directly to the master fuel trip relay and may be wired as an input to the burnermanagement system logic as well.

ROP Sequences 85-41 and 85-45 have slightly different wording for the same paragraph. Bothproposals were generated by the BCS-FUN TC. From the TC statement on 85-45, it looks like they intended to acceptthe language in 85-41, but for some reason they did not make them agree. This comment is meant to resolve the conflictbetween 85-41 and 85-45 at the suggestion of the NFPA liaison.

4Printed on 3/11/2010

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Report on Comments – November 2010 NFPA 85_______________________________________________________________________________________________85- Log #17 BCS-FUN

_______________________________________________________________________________________________Technical Correlating Committee on Boiler Combustion System Hazards,

85-49The TCC instructs the BCS-FUN TC to reconsider this proposal in the ROC phase in light of the

BCS-MBB actions adding terminology "minimum purge rate established by the designer" in accordance with 6.4.2.3.4.4.This is a direction from the Technical Correlating Committee on Boiler Combustion System Hazard in

accordance with 3.4.2 and 3.4.3 of the Regulations Governing Committee Projects.

_______________________________________________________________________________________________85- Log #18 BCS-FUN

_______________________________________________________________________________________________Technical Correlating Committee on Boiler Combustion System Hazards,

85-51The TCC instructs the BCS-FUN and BCS-SBB to reconsider this paragraph, and specifically

consider modifying the language to 4.6.7.1.1 as follows: "For single burner boilers, continuous trend display of operatingparameters critical to operation shall be provided."

The TCC requests that the review is accomplished by a task group of BCS-SBB members for input prior to theBCS-FUN ROC meeting.

This is a direction from the Technical Correlating Committee on Boiler Combustion System Hazard inaccordance with 3.4.2 and 3.4.3 of the Regulations Governing Committee Projects.

_______________________________________________________________________________________________85- Log #19 BCS-FUN

_______________________________________________________________________________________________Technical Correlating Committee on Boiler Combustion System Hazards,

85-52The TCC instructs the BCS-FUN and BCS-SBB to reconsider this paragraph, and specifically

consider modifying the language to 4.6.7.1.1 as follows: "For single burner boilers, continuous trend display of operatingparameters critical to operation shall be provided."

The TCC requests that the review is accomplished by a task group of BCS-SBB members for input prior to theBCS-FUN ROC meeting.

This is a direction from the Technical Correlating Committee on Boiler Combustion System Hazard inaccordance with 3.4.2 and 3.4.3 of the Regulations Governing Committee Projects.

5Printed on 3/11/2010

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Report on Comments – November 2010 NFPA 85_______________________________________________________________________________________________85- Log #7 BCS-FUN

_______________________________________________________________________________________________Dale P. Evely, Southern Company Services, Inc.

85-116New text to read as follows:

Locations at which natural gas, propane, or fuel oil systems are installed in compliance with this code normallyare not considered hazardous locations for electrical equipment as defined in NFPA 70, .

ROP item 85-116 Log #11 was rejected by the BCS-PFS TC but since it was meant to add newChapter 4 material it should have been considered by the BCS-FUN TC but was not; this comment has been filed toallow that to happen. Since the submitter of this comment does not agree with the original proposal the above textreflects the ideas of the comment submitter and is meant to replace what was originally proposed by Mr. Cunningham.NFPA 70 general compliance is currently only mandated in Chapters 5, 8 and 9 of NFPA 85 and these requirementsshould not be generally extended to the other chapters. The general need to properly establish electrical areaclassifications is currently discussed in Annex A as a part of A.4.1 and A.4.6.5 (2) b and the above proposed material ismeant to address Mr. Cunningham’s additional concerns in this regard.

_______________________________________________________________________________________________85- Log #11 BCS-FUN

_______________________________________________________________________________________________Gordon G. Gaetke, The Dow Chemical Company

85-41Revise text: (3) A documented life-cycle system reliability safety analysis that addresses all

requirements of this Code and incorporates the appropriate application-based safety integrity level (SIL) for safetyinstrumented systems (SIS). One methodology for achieving a life-cycle system reliability safety analysis is to use aprocess that includes Safety Integrity Level (SIL) determination and a Safety Instrumented System (SIS) design andimplementation consistent with the ISA 84 standard series.

Safety Integrity Level (SIL) assessments are a safety analysis, not reliability.

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85-20

Report on Proposals F2010 — Copyright, NFPA NFPA 85

_____________________________________________________________85-26 Log #16 BCS-FUN Final Action: Accept (4.6.2.3.2.5(5) and (6))_____________________________________________________________Submitter: Dale P. Evely, Southern Company Services, Inc. Recommendation: Revise text to read as follows: 4.6.2.3.2.5 (5) Boilers that share a common component between the furnace outlet and the stack shall have provisions to bypass the common component for unit purge when the common component contains a possible ignition source. (6) Where the common component does not contain a possible ignition source, a bypass shall not be required.Substantiation: This text had been reworded from a previous edition of the Code to eliminate an exception (section 1.9.2.3.2.e.5 of the 2001 Edition). This resulted in two separate sentences in the same code paragraph and made it unclear that the second sentence was meant to override the first sentence. The rewording here proposed is intended to eliminate any confusion in regards to this requirement. Committee Meeting Action: AcceptNumber Eligible to Vote: 22 Ballot Results: Affirmative: 20 Ballot Not Returned: 2 Bosfield, C., Raney, G. _____________________________________________________________85-27 Log #82 BCS-FUN Final Action: Reject (4.6.2.3.2.5(6))_____________________________________________________________Submitter: John Van Name, URS - Washington Division Recommendation: Revise text as follows: (6) Where the common component does not contain a possible ignition source, a bypass shall not be required, as long as the requirements contained in 6.5.3.2 Open-Flow Air Path and 6.4.2.3.4.3 (C) are met. Substantiation: When two or more boiler outlets are tied together, it is possible to pressurize this connection point either by design or excursion. Positive pressure at the connection point eliminates an open air path and also permits products of combustion from a running unit to enter a starting unit or a unit experiencing an emergency shutdown with loss of fans. A pressurized connection point also creates a safety issue for maintenance and inspection entries into a shutdown unit requiring emergency maintenance. A means of natural draft must always be provided for the emergency condition to slowly purge the remaining products of combustion. Water seals block a natural draft flow path. ID fans with positive discharge pressures keep the connection point pressurized above atmospheric pressure at all times. Committee Meeting Action: RejectCommittee Statement: The proposal is not appropriate for inclusion in chapter 4 as it is specific to one type of equipment covered by the code. It would also not be appropriate for chapter four to refer to requirements in an equipment chapter. The proposal is referred to the MBB TC for inclusion in Chapter 6. Number Eligible to Vote: 22 Ballot Results: Affirmative: 20 Ballot Not Returned: 2 Bosfield, C., Raney, G. _____________________________________________________________85-28 Log #82a BCS-MBB Final Action: Reject (4.6.2.3.2.5(6))_____________________________________________________________Submitter: John Van Name, URS - Washington Division Recommendation: Revise text as follows: (6) Where the common component does not contain a possible ignition source, a bypass shall not be required, as long as the requirements contained in 6.5.3.2 Open-Flow Air Path and 6.4.2.3.4.3 (C) are met. Substantiation: When two or more boiler outlets are tied together, it is possible to pressurize this connection point either by design or excursion. Positive pressure at the connection point eliminates an open air path and also permits products of combustion from a running unit to enter a starting unit or a unit experiencing an emergency shutdown with loss of fans. A pressurized connection point also creates a safety issue for maintenance and inspection entries into a shutdown unit requiring emergency maintenance. A means of natural draft must always be provided for the emergency condition to slowly purge the remaining products of combustion. Water seals block a natural draft flow path. ID fans with positive discharge pressures keep the connection point pressurized above atmospheric pressure at all times. Committee Meeting Action: RejectCommittee Statement: The proposal is not appropriate for inclusion in Chapter 4 as it is specific to one type of equipment covered by the code. It would also not be appropriate for chapter four to refer to requirements in an equipment chapter. The proposal is referred to the MBB TC for inclusion in Chapter 6. MBB TC Statement: The TC feels that the bypass should not be mandated because the proposed purge procedures (6.4.2.3.4.3(C)) as described in Proposal 85-68 (Log #60) address the issues raised by the submitter. Number Eligible to Vote: 30 Ballot Results: Affirmative: 28 Ballot Not Returned: 2 Hrul, B., Raney, G.

_____________________________________________________________85-29 Log #17 BCS-FUN Final Action: Accept in Principle (4.6.2.4.3)_____________________________________________________________Submitter: Dale P. Evely, Southern Company Services, Inc. Recommendation: Revise text to read as follows: 4.6.2.4.3 The vent lines from headers shall be permitted to be manifolded together, the vent lines from individual burners shall be permitted to be manifolded together, and vent lines from individual igniters shall be permitted to be manifolded together with the following restrictions: 4.6.2.4.3.1 (1) Burner vents shall not be manifolded with igniter vents or lance vents in any combination. 4.6.2.4.3.2 (2) Header vents shall be permitted to be manifolded with other header vents only where they are operated and tripped in parallel. 4.6.2.4.3.3 (3) Vents of headers served from different pressure reducing stations shall not be manifolded. 4.6.2.4.3.4 (4) Vent systems of different boilers or HRSGs shall not be manifolded. 4.6.2.4.3.5 (5) Vents of systems operating at different pressure levels shall not be manifolded. 4.6.2.4.3.6 (6) Vents of systems using different fuel sources shall not be manifolded. Substantiation: This text had been reworded from a previous edition of the Code to eliminate multiple exceptions (section 1.9.2.4.2 of the 2001 Edition). This resulted in confusion as to requirements because it was no longer obvious that the sub-sections were meant to override the requirement in the main section. The rewording here proposed is intended to eliminate any confusion in regards to the requirements for manifolding of vent lines. Committee Meeting Action: Accept in PrincipleRevise entire proposal as follows:4.6.2.4.3 Manifolding of Vents4.6.2.4.3.1 Vents from systems operating at different pressure levels shall not be permitted to be manifolded together. 4.6.2.4.3.2 Vents from systems served from different pressure reducing stations shall not be manifolded together. 4.6.2.4.3.3 Vents from different boilers or HRSGs shall not be permitted to be manifolded together. 4.6.2.4.3.4 Vents from systems using different fuel sources shall not be permitted to be manifolded together. 4.6.2.4.3.5 Header vents shall only be permitted to be manifolded together with other header vents and only when operated and tripped in parallel. 4.6.2.4.3.6 Burner vents shall only be permitted to be manifolded together with other burner vents. 4.6.2.4.3.7 Igniter vents shall only be permitted to be manifolded together with other igniter vents. 4.6.2.4.3.8 Lance vents shall only be permitted to be manifolded together with other lance vents. Committee Statement: Agree in principle, however the original proposal as written deleted the requirement for not manifolding headers, burners, igniters, and lance vent lines together. Changed “header” to “systems” in 4.6.2.4.3.2 because individual pressure reducing valves are sometimes used on burners and not just header systems. New language also better conforms to the NFPA manual of style. Number Eligible to Vote: 22 Ballot Results: Affirmative: 20 Ballot Not Returned: 2 Bosfield, C., Raney, G. _____________________________________________________________85-30 Log #25 BCS-FUN Final Action: Accept in Principle (4.6.3.1.3)_____________________________________________________________TCC Action: The TCC revised the action to reflect ACCEPT IN PRINCIPLE and updated the language of subparagraph (1) to reflect the language accepted in 85-31. The TCC instructs the BCS-FUN Technical Committee to consider changing the terminology “continuously variable process signals” to “process transmitters” in light of the new definition 3.3.159 for Transmitter. (1) A switch or transmitter independent of control functions and signalsSubmitter: Dale P. Evely, Southern Company Services, Inc. Recommendation: Add text as follows: 4.6.3.1.3 The burner management system interlock and alarm functions shall be initiated by one or more of the following: (1) Dedicated process switches independent of other control functions and signals(2) One or both of two continuously variable process signals exceeding a preset value(3) The median of three continuously variable process signals exceeding a preset value 4.6.3.1.3.1 When multiple continuously variable process signals are provided to initiate interlock or alarm functions those signals shall be monitored in comparison to each other by divergence or other fault diagnostic alarms. 4.6.3.1.3.2 When multiple continuously variable process signals are provided to initiate interlock or alarm functions the provided signals shall be generated by individual sensing devices connected to separate process taps. Substantiation: This is a refinement of language that currently exists in section 8.7.4.1.6 of the Code but which should also be applicable to all boiler and combustion systems. Continuously variable process signals are preferred

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Report on Proposals F2010 — Copyright, NFPA NFPA 85by many over discrete process switches because they can be monitored to assure that they are continuing to respond to changes in the process. Modern continuously variable devices also are less prone to drift than process switches and thus provide a better indicator of the process parameter they are monitoring. Committee Meeting Action: AcceptNumber Eligible to Vote: 22 Ballot Results: Affirmative: 19 Negative: 1 Ballot Not Returned: 2 Bosfield, C., Raney, G. Explanation of Negative: ZADIRAKA, A.: As written, proposal allows use of single process switch for initiating interlock & alarm functions but requires use of minimum of two continuous variable process signals even though Committee statement says the continuous variable process signal is much more reliable than process switch. _____________________________________________________________85-31 Log #CP9 BCS-MBB Final Action: Accept (4.6.3.1.3 (New) )_____________________________________________________________TCC Action: The TCC instructs the BCS-FUN Technical Committee to consider changing the terminology “continuously variable process signals” to “process transmitters” in light of the new definition 3.3.159 for Transmitter.Submitter: Technical Committee on Multiple Burner Boilers, Recommendation: Add new text to read as follows: 4.6.3.1.3 The burner management system interlock and alarm functions shall be initiated by one or more of the following: (1) A switch or transmitter independent of control functions and signals (2) One or both of two continuously variable process signals exceeding a preset value(3) The median of three continuously variable process signals exceeding a preset value 4.6.3.1.3.1 When multiple continuously variable process signals are provided to initiate interlock or alarm functions those signals shall be monitored in comparison to each other by divergence or other fault diagnostic alarms. 4.6.3.1.3.2 When multiple continuously variable process signals are provided to initiate interlock or alarm functions the provided signals shall be generated by individual sensing devices connected to separate process taps. Substantiation: This is a refinement of language that currently exists in section 8.7.4.1.6 of the Code but which should also be applicable to all boiler and combustion systems. Continuously variable process signals are preferred by many over discrete process switches because they can be monitored to assure that they are continuing to respond to changes in the process. Modern continuously variable devices also are less prone to drift than process switches and thus provide a better indicator of the process parameter they are monitoring. It is the intent of the TC to allow a single transmitter to be used if independent of control functions. Editorially, the terminology was changed to singular to clarify the intent of the provision that a single switch or transmitter is adequate. Committee Meeting Action: AcceptNumber Eligible to Vote: 30 Ballot Results: Affirmative: 28 Ballot Not Returned: 2 Hrul, B., Raney, G. _____________________________________________________________85-32 Log #77 BCS-FUN Final Action: Accept in Principle (4.6.3.2.3(2))_____________________________________________________________Submitter: G. F. Gilman, SIS-Tech Recommendation: New text to read as follows: 4.6.3.2.3 (2) Memory corruption and Losses * Add to Annex: The software for the programmable system shall reside in a form of nonvolatile storage (memory) that retains information on loss of system power. Substantiation: Provide a definition. Committee Meeting Action: Accept in PrincipleAdd new text to read as follows: 4.6.3.2.4(12) Logic shall be maintained either in nonvolatile storage or in other memory that retains information on the loss of system power. Committee Statement: The TC agrees with the submitter that further clarification regarding logic retention is warranted, but feels that it belongs in the mandatory section of the code. The basic text was extracted from section 8.7.5 of the 2007 edition of the code. Number Eligible to Vote: 22 Ballot Results: Affirmative: 20 Ballot Not Returned: 2 Bosfield, C., Raney, G. _____________________________________________________________85-33 Log #92 BCS-FUN Final Action: Reject (4.6.3.2.4)_____________________________________________________________Submitter: Celso G. Schmidt, Forney Corporation Recommendation: New text to read as follows: (12)* The hardware master fuel trip relay shall be of the type that stays tripped until the unit purge system interlock permits it to be reset. Whenever the master fuel trip relay (s) is operated, it shall directly remove all fuel inputs from the furnace in a redundant path with the soft master fuel trip which will trip all outputs to fuel related devices. The master fuel trip relay contacts shall not only

trip the fuel headers but all individual fuel related equipment and shall de-energize all spark igniters and all ignition devices within the unit and flue gas path.

A.4.6.3.2.4 (12) The main hardware master fuel trip relay shall be a fail-safe relay with mechanically linked contacts to prevent the reclosing of the normally closed contact if a normally open contact is welded. Substantiation: The master fuel trip relay is not addressed properly in the Chapter 4, common to all boilers and HRSGs. This proposal intends to make the existing requirements for MBB common to all boilers and HRSGs. The proposal for the Annex A intends to utilize safe relays for the master fuel trip application. These relays meet IEC 947-5-1-I. There are several manufacturers in the market and some relays are tamper resistant. Committee Meeting Action: RejectCommittee Statement: The TC feels that this requirement, which comes from the MBB chapter, is more appropriately to be considered by the TC’s which are responsible for the other boiler sections, i.e. SBB, HRS, and FBB. The language came from 6.4.2.3.1(A) blocks 3-12. It is not appropriate to pull one requirement from the table into chapter 4 without the input from the other TCs. The TC feels that the equipment chapters contain requirements that address some of the submitter’s concerns, and that the proposal should be forwarded to the other TC’s for use in clarifying the applicable coverage. Number Eligible to Vote: 22 Ballot Results: Affirmative: 20 Ballot Not Returned: 2 Bosfield, C., Raney, G. _____________________________________________________________85-34 Log #92a BCS-FBB Final Action: Reject (4.6.3.2.4)_____________________________________________________________Submitter: Celso G. Schmidt, Forney Corporation Recommendation: Add new text to read as follows: (12)* The hardware master fuel trip relay shall be of the type that stays tripped until the unit purge system interlock permits it to be reset. Whenever the master fuel trip relay (s) is operated, it shall directly remove all fuel inputs from the furnace in a redundant path with the soft master fuel trip which will trip all outputs to fuel related devices. The master fuel trip relay contacts shall not only trip the fuel headers but all individual fuel related equipment and shall de-energize all spark igniters and all ignition devices within the unit and flue gas path. A.4.6.3.2.4 (12) The main hardware master fuel trip relay shall be a fail-safe relay with mechanically linked contacts to prevent the reclosing of the normally closed contact if a normally open contact is welded. Substantiation: The master fuel trip relay is not addressed properly in the Chapter 4, common to all boilers and HRSGs. This proposal intends to make the existing requirements for MBB common to all boilers and HRSGs. The proposal for the Annex A intends to utilize safe relays for the master fuel trip application. These relays meet IEC 947-5-1-I. There are several manufacturers in the market and some relays are tamper resistant. Committee Meeting Action: RejectCommittee Statement: The Fundamentals TC feels that this requirement, which comes from the MBB chapter, is more appropriately to be considered by the TC’s which are responsible for the other boiler sections, i.e. SBB, HRS, and FBB. The language came from 6.4.2.3.1(A) blocks 3-12. It is not appropriate to pull one requirement from the table into chapter 4 without the input from the other TC’s. The TC feels that the equipment chapters contain requirements that address some of the submitter’s concerns, and that the proposal should be forwarded to the other TC’s for use in clarifying the applicable coverage. FBB TC Statement: The current language in the FBB chapter, section 7.9.3., adequately addresses the submitter’s concerns. Number Eligible to Vote: 14 Ballot Results: Affirmative: 10 Ballot Not Returned: 4 Chelian, P., Darguzas, J., George, W., Herdman, R.

_____________________________________________________________85-35 Log #92b BCS-HRS Final Action: Reject (4.6.3.2.4)_____________________________________________________________TCC Action: The TCC revised the TC action to REJECT to reflect a lack of consensus for this proposal in other NFPA 85 TCs. The applicable chapters address master fuel trip in different ways, with different requirements. Therefore, the TCC rejects the addition of this section to chapter 4 as it would result in correlating issues with other chapters.Submitter: Celso G. Schmidt, Forney Corporation Recommendation: New text to read as follows:

(12)* The hardware master fuel trip relay shall be of the type that stays tripped until the unit purge system interlock permits it to be reset. Whenever the master fuel trip relay (s) is operated, it shall directly remove all fuel inputs from the furnace in a redundant path with the soft master fuel trip which will trip all outputs to fuel related devices. The master fuel trip relay contacts shall not only trip the fuel headers but all individual fuel related equipment and shall de-energize all spark igniters and all ignition devices within the unit and flue gas path. A.4.6.3.2.4 (12) The main hardware master fuel trip relay shall be a fail-safe relay with mechanically linked contacts to prevent the reclosing of the normally closed contact if a normally open contact is welded.

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Report on Proposals F2010 — Copyright, NFPA NFPA 85the manufacturer may mismark a valve, and furthermore that valve positions may not be indicative of the actual air/fuel ratio due to valve characterization. Number Eligible to Vote: 15 Ballot Results: Affirmative: 13 Ballot Not Returned: 2 Bosfield, C., Raney, G. Comment on Affirmative: GILMAN, G.: I agree that there could be more problems that any benefit. WAGNER, J.: Use in Appendix. _____________________________________________________________85-48 Log #10 BCS-FUN Final Action: Reject (4.6.5.1.5 (New) )_____________________________________________________________Submitter: Michael C. Polagye, FM Global Recommendation: Insert a new 4.6.5.1.5 as follows: 4.6.5.1.5 Valves and dampers used to maintain air/fuel ratio shall have local external visual indication of position. Substantiation: As noted in the Committee’s Substantiation, the submitter’s reason for creating the proposal addresses a valid safety issue that applies to both control valves and dampers and should not be limited to multiple-burner boilers. The new paragraph number for the text in this comment addresses these concerns. Committee Meeting Action: RejectCommittee Statement: Although the committee agrees that the addition of external visual indications is advantageous, it does not warrant being a specific requirement of the fundamentals section of the Code. Committee agrees with the TCC’s position, and this material is not appropriate for the fundamental chapters and should be considered by the individual TCs for their individual chapters.Number Eligible to Vote: 22 Ballot Results: Affirmative: 20 Ballot Not Returned: 2 Bosfield, C., Raney, G. _____________________________________________________________85-49 Log #43 BCS-FUN Final Action: Reject (4.6.5.2.1)_____________________________________________________________TCC Action: The TCC instructs the BCS-FUN TC to reconsider this proposal in the ROC phase in light of the BCS-MBB actions adding terminology “minimum purge rate established by the designer” in accordance with 6.4.2.3.4.4.Submitter: Tom Russell, Honeywell Recommendation: Revise text as follows: Except as noted in 4.6.5.2.2 under no circumstances shall airflow demand be less than the minimum purge rate. Substantiation: The issue of purging needs to be clarified. Does the purge rate need to be fixed or can it be variable, the code is ambiguous on this topic. The code permits a boiler to be purged at various airflow rates, but it implies that whatever airflow rate is used for purging now becomes the minimum value to which airflow can be controlled. These changes permit purging at rates above the minimum and then permit airflow to be reduced to the minimum. Committee Meeting Action: RejectCommittee Statement: The current intent, as described in section A.4.6.5.2.1, is that the purge rate established by the designer/operator becomes the “purge rate” and that is the de facto minimum. Further, the use of the word “minimum” in this section would imply that there is an acceptable range, which is not the case. Number Eligible to Vote: 22 Ballot Results: Affirmative: 19 Negative: 1 Ballot Not Returned: 2 Bosfield, C., Raney, G. Explanation of Negative: YATES, H.: MBB accepted in principal similar proposals that define “mininum purge rate” as’....the minimum purge rate established by the designer....’ rejecting Log 36 would compromise, if not conflict with, actions taken by MBB. _____________________________________________________________85-50 Log #19 BCS-FUN Final Action: Accept (4.6.5.3.3.1)_____________________________________________________________Submitter: Dale P. Evely, Southern Company Services, Inc. Recommendation: Revise text to read as follows:

4.6.5.3.3* Automatic Control. 4.6.5.3.3.1 Except as noted in 4.6.5.3.3.2, automatic Automatic control of the fuel input(s) shall not be permitted unless the airflow is maintained in automatic control. 4.6.5.3.3.2 For HRSGs designed and operated in accordance with Chapter 8, automatic control of fuel inputs shall be permitted without automatic control of airflow. Substantiation: This text had been reworded from a previous edition of the Code to eliminate an exception (section 1.9.5.3.3 of the 2001 Edition). This resulted in two separate subsections in the same code paragraph and made it unclear that the second section was meant to override the first section. The rewording here proposed is intended to eliminate any confusion in regards to this requirement. Committee Meeting Action: AcceptNumber Eligible to Vote: 22 Ballot Results: Affirmative: 20

Ballot Not Returned: 2 Bosfield, C., Raney, G. _____________________________________________________________85-51 Log #20 BCS-FUN Final Action: Accept in Principle (4.6.7.1)_____________________________________________________________TCC Action: The TCC instructs the BCS-FUN and BCS-SBB to reconsider this paragraph, and specifically consider modifying the language to 4.6.7.1.1 as follows: “For single burner boilers, continuous trend display of operating parameters critical to operation shall be provided.” The TCC requests that the review is accomplished by a task group of BCS-SBB members for input prior to the BCS-FUN ROC meeting.Submitter: Dale P. Evely, Southern Company Services, Inc. Recommendation: Revise text to read as follows: 4.6.7.1 As a minimum, except as noted in 4.6.7.1.1, continuous trend display of steam flow, feed water flow rate, total fuel flow rate, and total airflow rate as a percentage of the maximum unit load, drum level, final steam temperature, main steam pressure, and furnace combustion chamber draft shall be simultaneously available at the operating location. 4.6.7.1.1 For single burner package boilers, minimum continuous trend display shall include steam flow, airflow, drum level, steam pressure, and, where applicable, the furnace draft. Substantiation: This text had been reworded from a previous edition of the Code to eliminate an exception (section 1.9.7 of the 2001 Edition). This resulted in two separate subsections in the same code paragraph and made it unclear that the second section was meant to override the first section. The rewording here proposed is intended to eliminate any confusion in regards to this requirement. Committee Meeting Action: Accept in PrincipleRevise proposal as follows: 4.6.7.1 As a minimum, e Except as noted in 4.6.7.1.1, continuous trend display

of steam flow, feed water flow rate, total fuel flow rate, and total airflow rate as a percentage of the maximum unit load, drum level, final steam temperature, main steam pressure, and furnace combustion chamber draft shall be simultaneously available at the operating location. 4.6.7.1.1 For single burner package boilers, minimum continuous trend display shall include steam flow, airflow, drum level, steam pressure, and, where applicable, the furnace draft. Committee Statement: Editorial revisions. The term “as a minimum” is redundant because the code is a minimum. Number Eligible to Vote: 22 Ballot Results: Affirmative: 20 Ballot Not Returned: 2 Bosfield, C., Raney, G. _____________________________________________________________85-52 Log #65 BCS-FUN Final Action: Accept in Principle (4.6.7.1.1)_____________________________________________________________TCC Action: The TCC instructs the BCS-FUN and BCS-SBB to reconsider this paragraph, and specifically consider modifying the language to 4.6.7.1.1 as follows: “For single burner boilers, continuous trend display of operating parameters critical to operation shall be provided.” The TCC requests that the review is accomplished by a task group of BCS-SBB members for input prior to the BCS-FUN ROC meeting.Submitter: Michael C. Polagye, FM Global Recommendation: Revise text as follows:

4.6.7.1.1 For single burner package boilers, minimum continuous trend display shall include steam flow, fuel flow, airflow, drum level, steam pressure, and, where applicable, the furnace draft. Substantiation: Historically, the trending of steam flow and air flow has been used as index of air-fuel ratio and for alerting operators to changes in “locked settings” of the air to fuel ratio control. However, current single-burner boilers operate at low excess air and in the event of a change in a “locked setting” that results in reduced air flow, there will be a nearly corresponding decrease in steam flow coupled with an increase in unburned fuel. Without a fuel flow trend continuously displayed with the other trends required in 4.6.7.1.1 this condition may not be recognized. Committee Meeting Action: Accept in PrincipleRevise text to read as follows: 4.6.7.1.1 For single burner package boilers, minimum continuous trend display shall include steam flow, fuel flow, airflow, drum level, steam pressure, and, where applicable, the furnace draft. Committee Statement: These changes are in addition to the change in Proposal 85-51 (Log #20). The phrase “package boilers” is not used anywhere else in the code and may cause confusion. The TC accepts the submitter’s substantiation for the addition of “fuel flow”. Number Eligible to Vote: 22 Ballot Results: Affirmative: 20 Ballot Not Returned: 2 Bosfield, C., Raney, G.

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Report on Proposals F2010 — Copyright, NFPA NFPA 85_____________________________________________________________85-53 Log #CP401 BCS-SBB Final Action: Accept (4.6.7.1.1)_____________________________________________________________TCC Action: The TCC instructs the BCS-FUN and BCS-SBB to reconsider this paragraph, and specifically consider modifying the language to 4.6.7.1.1 as follows: “For single burner boilers, continuous trend display of operating parameters critical to operation shall be provided.” (Proposed Annex A material would be included unchanged.) The TCC requests that the review is accomplished by a task group of BCS-SBB members for input prior to the BCS-FUN ROC meeting.Submitter: Technical Committee on Single Burner Boilers, Recommendation: Revise as follows: 4.6.7.1.1* Single burner boilers shall not be required to provide continuous trend display of operating information. For single burner package boilers, minimum continuous trend display shall include steam flow, airflow, drum level, steam pressure, and, where applicable, the furnace draft. A.4.6.7.1.1 For single burner boilers, continuous trend display may include

steam flow, fuel flow, drum or water level, steam pressure, and, where measurement is available, the furnace draft and airflow. When the main control for combustion control uses metered air/fuel ratio, the fuel flow and air flow should be available to the operators to ensure proper operation. Substantiation: Single burner boilers are provided with automatic controls to ensure safe operation. Continuous trend display of this information adds complexity without providing additional safety. There are many different designs of single burner boilers and the operating information required by the existing provision is not appropriate for all designs. Therefore, the specific operating information has been moved to the annex material. Committee Meeting Action: AcceptNumber Eligible to Vote: 15 Ballot Results: Affirmative: 12 Negative: 1 Ballot Not Returned: 2 Bosfield, C., Raney, G. Explanation of Negative: GILMAN, G.: It is critical for the operator to have the information available. If there is no trend or visible information the operator can not observe a problem. I was informed of a plant that lost the operator information and the operator was depending on the BMS for protection. Change trend display may include to trend display shall include. Change the fuel flow and air flow shall be available to the operators to ensure proper operation. Certain types of SBB may not have the information available and therefor it is not required. This is in line with a relay BMS does not need to meet the requirements of a logic system. See 4.6.3.2. reference to A4.6.3.2.. Comment on Affirmative: WAGNER, J.: Boiler Operators in schools and colleges using cast iron & steel fire tubes. Do not stay in their respective boiler rooms. _____________________________________________________________85-54 Log #CP402 BCS-SBB Final Action: Accept (5.3.2.6)_____________________________________________________________Submitter: Technical Committee on Single Burner Boilers, Recommendation: Revise as follows: 5.3.2* Fuel Supply — Gas. 5.3.2.6 Gas piping material and system design shall be in accordance with NFPA 54, National Fuel Gas Code (for gas piping inside industrial and institutional buildings), ASME B31.1, Power Piping (for gas piping in power applications), or ASME B31.3, Process Piping (for gas piping in process applications). 5.3.2.6.1 Where a conflict exists between this code and NFPA 54, ASME B31.1 or ASME B31.3, the requirements of 5.3.2.6 shall prevail. 5.3.2.6.2 Aluminum alloy threaded fittings shall be permitted to be used with steel or wrought iron piping. Substantiation: The TC recognizes that NFPA 54 currently prohibits the use of aluminum threaded fittings with steel or wrought iron piping. However, industry experience has shown that these fittings have been used safely and successfully for many years. Therefore, the TC has added language to explicitly permit the use of aluminum threaded fittings with steel or wrought iron piping in fuel gas piping on single burner boilers. Committee Meeting Action: AcceptNumber Eligible to Vote: 15 Ballot Results: Affirmative: 13 Ballot Not Returned: 2 Bosfield, C., Raney, G. Comment on Affirmative: GILMAN, G.: I agree because the use of the fittings over the years have not been a problem. WAGNER, J.: Using different metal fittings have caused problems when tightened.

_____________________________________________________________85-55 Log #50 BCS-SBB Final Action: Accept in Principle (5.3.4.6.3 (New) )_____________________________________________________________Submitter: Gordon G. Gaetke, The Dow Chemical Company Recommendation: Add new text to read as follows:

5.3.4.6.3 * Any permanently installed flue gas analyzers shall not present an ignition source hazard.

Substantiation: In 2005 a flammable hydrocarbon mixture formed in a chemical company’s process furnace that was ignited severely damaging the furnace. A power failure placed the furnace off-line and inadvertently permitted the introduction of hydrocarbon material. The investigation determined an in situ zirconium oxide oxygen probe was the source of ignition. These oxygen probes are very common with fired equipment such as boilers. If excessive unburned fuel accumulates from failed light-offs, or if fuel leaked into boiler or hydrocarbons are ingested through fan, it could be ignited by such an ignition source. If an SBB contains a zirconium oxide or other high temperature analyzer, the analyzer should be designed to protect the sample space from the ignition source. Another option is to have the analyzer powered down prior to startup. Then power up analyzer after boiler successfully started up. However, frequent power cycling of these analyzers degrades analyzer life. Also, it takes several minutes for analyzer to cool down and warm up. Since many Single Burner Boilers are automatic recycling, this option is not feasible. Committee Meeting Action: Accept in Principle

5.3.4.6.3 * Any permanently installed flue gas analyzers shall not present an ignition source hazard to the flue gas stream being sampled. Committee Statement: The TC added language to clarify that the ignition hazard is within the flue gas stream. Number Eligible to Vote: 15 Ballot Results: Affirmative: 11 Negative: 2 Ballot Not Returned: 2 Bosfield, C., Raney, G. Explanation of Negative: EIBL, J.: “Wording should be clarified to address in-situ zirconium oxide analyzers that are internally heated above the AIT of the fuels being burned.” WAGNER, J.: Substantiation uses a fired furnace and not a boiler. Comment on Affirmative: GILMAN, G.: I agree that this is a potential risk. The system must be designed to prevent the hazard.

_____________________________________________________________85-56 Log #55 BCS-SBB Final Action: Reject (5.3.6.4.3)_____________________________________________________________Submitter: Tom Russell, Honeywell Recommendation: Add new text as follows: The design shall not require any deliberate “defeating” of an interlock to start or operate equipment. Whenever a required interlock device is removed temporarily from service, it shall be noted in the log and annunciated. Other means shall be substituted to supervise this interlock function. Substantiation: 1. Paragraph 4.5.4 implies implementing a bypass is permitted, where as presently 5.3.6.4.3 prevents any bypass. Also multiple burner boilers (section 6) permit bypasses. This non-agreement is causing confusion. 2. Without the ability to bypass an interlock, testing and/or maintenance cannot be performed while the equipment is in operation. I believe we should permit the ability to perform testing and maintenance without necessarily removing the unit from operation. Committee Meeting Action: RejectCommittee Statement: The TC rejects the proposal because 5.3.6.4.3.1 covers the acceptable circumstances for bypasses, thereby prohibiting manual bypass during normal operation except for low water cutouts. Number Eligible to Vote: 15 Ballot Results: Affirmative: 12 Negative: 1 Ballot Not Returned: 2 Bosfield, C., Raney, G. Explanation of Negative: CONNOR, J.: The increased maintenance and testing resulting from not incurring the associated downtime could provide a safer shutdown system and would bring NFPA 85 Chapter 5 closer to ANSI/ISA-84.00.01-2004(IEC 61508 modified) the international SIS (Safety Instrumented Shutdown)system standard. Such interlock bypasses should be keyed and supervised as defined in the above referenced standard. The wording of 85-56 (Log #55) should be revisited. Comment on Affirmative: GILMAN, G.: For systems that run for extensive periods of time may require. I agree that by pass testing OK if the if the operator is aware that the component is temporarily out of service. WAGNER, J.: Noted in log book. _____________________________________________________________85-57 Log #23 BCS-SBB Final Action: Accept in Principle (5.3.10)_____________________________________________________________Submitter: Dale P. Evely, Southern Company Services, Inc. Recommendation: Add text as follows:

5.3.10 Proof of Closure Switches. Each safety shutoff valve proof of closure switch shall be a non-field-adjustable switch installed by the valve manufacturer that activates only after the valve is fully closed. Substantiation: The second sentence of the existing definition in Section 3.3.158.5 is a requirement and should not be a part of the definition. This proposal relocates the requirement to Chapter 5 as requested by the Technical Correlating Committee in their June 2006 meeting. A companion proposal has been submitted to remove the requirement portion of the definition from Section 3.3.158.5. Committee Meeting Action: Accept in Principle 5.1.3 All safety shutoff valves, safety interlock devices, valve-proving

systems, and flame detection systems shall be listed or approved. A safety

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Beach, Denise

From: Beach, DeniseSent: Tuesday, February 16, 2010 11:59 AMTo: '[email protected]'Cc: Beach, DeniseSubject: FW: Aluminum Material in Industrial Gas Control equipment

TO: All BCS Technical Committee Members All, Please see the message from Franklin Switzer regarding a joint task group on aluminum. Please reply to Franklin and myself if you are willing to participate. Best Regards, Denise

Denise Beach Senior Engineer NFPA 1 Batterymarch Park Quincy, MA 02169-7471 Phone: 617-984-7501 Fax: 617-984-7110

From: Franklin Switzer Jr. [mailto:[email protected]] Sent: Sunday, February 14, 2010 1:49 PM To: Beach, Denise Subject: Aluminum Material in Industrial Gas Control equipment  Denise, Could you please send this to the combined NFPA 54, 85, 86, 87 Committees. There are a couple of modifications from the one I sent last week. I will also forward this to Geraldo, ASME CSD‐1 secretary for distribution once I talk to him next week. I believe all other Chairman are aware of the correspondence now.  Franklin  

Gentlemen and Ladies, I have been in contact with many various Chairman of NFPA 54, 85, 86 and ASME CSD‐1 regarding the topic of Aluminum valves in Boilers, Ovens, and Furnaces covered in these codes. This has become a very discussed topic with what seems to be a lot of confusion regarding the application. Please see the Reference section below that I sent to several of the manufacturers back in June of 2009 when the topic first came up at the MBB committee of NFPA 85.  As I see it there are 2 fundamental issues that have come to light and need to be resolve: 1/ Aluminum Threaded Fittings including Valves, Strainer, Regulators and Pressure switches in gas trains for NFPA 54, 85, 86, 87 and ASME CSD‐1 standards                 Reasons:              Galvanic reaction,  

Weakness of thread due to heat, 

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Variations in thread engagement because of the thermo changes in thread form versus the more stable steel pipe thread 

Relaxation of thread seal as temperature changes once installed  

2/ Aluminum bodies of construction whether Threaded or Flanged in NFPA 54 as well as NFPA 85, 86, 87 and ASME CSD‐1 standards                 Reasons:              Low melt point of material in the event of a fire  Each of these issues has had more than one reason given for their ban but there seems to be no one clear‐cut reason that everyone I have talked to can agree on. Additionally, our industries seemed to have accepted their use even though these standards have not allowed this for many years.  When I brought this issue up to the individual standards NFPA 85, 86 and ASME CSD‐1, many times the finger merely pointed to NFPA 54 and in the case of Boiler B31.X as the expert and the reason we reference them was because they are the overriding standard and why would the individual standards contradict the National Fuel Gas Code. When I brought the issue to NFPA 54 and ask for clarification as to why they banned Threaded fittings with Steel pipe there were just as many questions raised regarding why this was in the code. Several members volunteered to get input from leading experts in various fields to help clarify. This has resulted in the flurry of activity since the NFPA 54 committee meeting in Fort Lauderdale.  I have been in touch with Dale Evely and Skip Yates from the NFPA 85 committee, Tom Crane of the NFPA 54 committee and we would like to get an assembly of personnel from the different committees and with a cross section of experience to try to bring this matter to a close, hopefully in time for one or more of the committees to take action with their current cycle or be able to issue a TIA with their next release. At this time I have myself, Franklin Switzer (SE, NFPA 54, 85, 86, ASME CSD‐1, and CSA Z21 TAG, S‐afe, Inc), Mike Polagye (I, NFPA 85 Chairmen ACC, Member FUN, MBB, HRS, 86 and CSD‐1, Factory Mutual), Walter Spurko (Non‐Member, Various ASME BPV and B31 series committees, [recommended by Gregg Gress, I, NFPA 54 committee member, ICC]) and John Ible (U, NFPA 85 Chairman SBB, Member ACC, MBB, Dupont Company Inc.).  I would like to request members to volunteer for this task group that have a knowledge of the subject and desire to participate. I am also looking for a somewhat small group, 8‐10 total participants and a cross section of Manufacturers (M), Insurance(I), Users(U) as well as a cross section of the various codes impacted. Remember, even if you do not feel qualified or don’t have the time, someone you know may have a very broad knowledge of the topic and can serve on the committee even if they are not NFPA members or committee members currently.  Also, for those members who serve on several or many of these committees, your input is very valuable for this task group. Once I have volunteers, and have selected the group, I would like to get a teleconference set for early March, probably a Friday AM about 10:00AM EST so that it isn’t too early in the event we pick up some members on the west coast. Please respond ASAP so we can get the group organized and start working on what seems to be a highly controversial issue.  This committees recommendations could have a dramatic impact on the Combustion market that we are all involved with, I would really like to get a very qualified answer to these questions before we go back with recommendations to the individual committees.   

References: NFPA 85-2007 Boiler and Combustion Systems Hazards Code Chapter 4 Fundamentals of Boiler Combustion Systems 4.6 Equipment Requirements.

4.6.2 Functional Requirements of Fuel-Burning System. 4.6.2.5 Fuel Gas Piping Systems. Fuel gas piping material and system design shall be in accordance with NFPA 54, National Fuel Gas Code (for fuel gas piping inside industrial and institutional buildings),

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ASME B31.1, Power Piping (for fuel gas piping in power applications), or ASME B31.3, Process Piping (for fuel gas piping in process applications). 4.6.2.6 Fuel Oil Piping Systems. Fuel oil piping materials and system design shall be in accordance with NFPA 31, Standard for the Installation of Oil-Burning Equipment (for fuel oil piping inside industrial or institutional buildings), ASME B31.1, Power Piping (for fuel oil piping in power applications), or ASME B31.3, Process Piping (for fuel oil piping in process applications).

Chapter 5 Single Burner Boilers 5.3 Equipment Requirements.

5.3.1 Fuel Supply — Oil. 5.3.1.11 Oil piping materials and system design shall be in accordance with NFPA 31, Standard for the Installation of Oil-Burning Equipment (for oil piping inside industrial or institutional buildings), ASME B31.1, Power Piping (for oil piping in power applications), or ASME B31.3, Process Piping (for oil piping in process applications).

5.3.2* Fuel Supply — Gas. 5.3.2.6 Gas piping material and system design shall be in accordance with NFPA 54, National Fuel Gas Code (for gas piping inside industrial and institutional buildings), ASME B31.1, Power Piping (for gas piping in power applications), or ASME B31.3, Process Piping (for gas piping in process applications).

NFPA 86-2007 Standard for Ovens and Furnaces Chapter 6 Furnace Heating Systems 6.2 Fuel Gas–Fired Units.

6.2.5 Equipment Fuel Gas Piping. 6.2.5.2* Piping and Fittings. (A) Fuel gas piping materials shall be in accordance with NFPA 54, National Fuel Gas Code. 

A.6.2.5.2 NFPA 54, National Fuel Gas Code, provides sizing methods for gas piping systems. 6.3 Oil-Fired Units.

6.3.5 Equipment Oil Piping. 6.3.5.2 Piping and Fittings. (A) Fuel oil piping materials shall be in accordance with NFPA 31, Standard for the Installation of Oil-Burning Equipment. 

NFPA 31-2006 Standard for the Installation of Oil-Burning Equipment Chapter 13 Oil-and-Gas Burning Appliances 13.7 Piping, Pumps, and Valves. Piping for fuel oil shall meet all applicable requirements of Chapter 8 of this standard. Piping for fuel gas shall meet all applicable requirements of NFPA 54, National Fuel Gas Code.

NFPA 54-2009 National Fuel Gas Code Chapter 5 Gas Piping System Design, Materials, and Components 5.6* Acceptable Piping Materials and Joining Methods.

5.6.8 Metallic Piping Joints and Fittings. 5.6.8.4 Metallic Fittings (Including Valves, Strainers, Filters). Metallic fittings shall comply with the following:

(1) Threaded fittings in sizes larger than 4 in. (100 mm) shall not be used unless acceptable to the authority having jurisdiction. (2) Fittings used with steel or wrought-iron pipe shall be steel, brass, bronze, malleable iron, or cast iron. (3) Fittings used with copper or brass pipe shall be copper, brass, or bronze. (4) Fittings used with aluminum alloy pipe shall be of aluminum alloy. (5) Cast-Iron Fittings. Cast-iron fittings shall comply with the following:

(a) Flanges shall be permitted. (b) Bushings shall not be used. (c) Fittings shall not be used in systems containing flammable gas–air mixtures. (d) Fittings in sizes 4 in. (100 mm) and larger shall not be used indoors unless approved by the authority having jurisdiction.

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(e) Fittings in sizes 6 in. (150 mm) and larger shall not be used unless approved by the authority having jurisdiction.

(6) Aluminum Alloy Fittings. Threads shall not form the joint seal. (7) Zinc–Aluminum Alloy Fittings. Fittings shall not be used in systems containing flammable gas–air mixtures. (8) Special Fittings. Fittings such as couplings, proprietary-type joints, saddle tees, gland-type compression fittings, and flared, flareless, or compression-type tubing fittings shall be as follows:

(a) Used within the fitting manufacturer’s pressure–temperature recommendations (b) Used within the service conditions anticipated with respect to vibration, fatigue, thermal expansion, or contraction (c) Installed or braced to prevent separation of the joint by gas pressure or external physical damage (d) Acceptable to the authority having jurisdiction 

  

S-afe, Inc. Franklin R. Switzer Jr. President 2405 West Sacramento Drive Muncie, IN 47303-9002 (765) 284-8164 (765) 216-0979 (765) 760-0147

[email protected] www.s-afe.com ************************************************** IMPORTANT NOTICE: This correspondence is not a Formal Interpretation issued pursuant to NFPA regulations. Any opinion expressed is the personal opinion of the author, and does not necessarily represent the official position of the NFPA or it's Technical Committees. This correspondence is not a Formal Interpretation issued pursuant to ASME regulations. Any opinion expressed is the personal opinion of the author, and does not necessarily represent the official position of the ASME or it's Technical Committees. This correspondence is not a Formal Interpretation issued pursuant to ANSI/CSA regulations. Any opinion expressed is the personal opinion of the author, and does not necessarily represent the official position of the ANSI/CSA or THE Z21/CSA JOINT TECHNICAL ADVISORY GROUP ON STANDARDS FOR AUTOMATIC GAS CONTROLS. ************************************************** DISCLAIMER of S-afe, Inc.: This e-mail and any files transmitted with it are confidential and intended solely for the use of the individual or entity to which they are addressed. If you are not the named addressee you should not disseminate, distribute or copy this e-mail. If you have received this message in error please notify [email protected] and delete the message and any attachments accompanying it immediately. Although S-afe, Inc. operates an active anti-virus policy, the company accepts no liability for any damage caused by any virus transmitted by this e-mail. Please note that any views expressed in this e-mail may be those of the originator and do not necessarily reflect those of the organization.