ImageVerifierCode 换一换
格式:PDF , 页数:119 ,大小:2.93MB ,
资源ID:399869      下载积分:10000 积分
快捷下载
登录下载
邮箱/手机:
温馨提示:
快捷下载时,用户名和密码都是您填写的邮箱或者手机号,方便查询和重复下载(系统自动生成)。 如填写123,账号就是123,密码也是123。
特别说明:
请自助下载,系统不会自动发送文件的哦; 如果您已付费,想二次下载,请登录后访问:我的下载记录
支付方式: 支付宝扫码支付 微信扫码支付   
验证码:   换一换

加入VIP,免费下载
 

温馨提示:由于个人手机设置不同,如果发现不能下载,请复制以下地址【http://www.mydoc123.com/d-399869.html】到电脑端继续下载(重复下载不扣费)。

已注册用户请登录:
账号:
密码:
验证码:   换一换
  忘记密码?
三方登录: 微信登录  

下载须知

1: 本站所有资源如无特殊说明,都需要本地电脑安装OFFICE2007和PDF阅读器。
2: 试题试卷类文档,如果标题没有明确说明有答案则都视为没有答案,请知晓。
3: 文件的所有权益归上传用户所有。
4. 未经权益所有人同意不得将文件中的内容挪作商业或盈利用途。
5. 本站仅提供交流平台,并不能对任何下载内容负责。
6. 下载文件中如有侵权或不适当内容,请与我们联系,我们立即纠正。
7. 本站不保证下载资源的准确性、安全性和完整性, 同时也不承担用户因使用这些下载资源对自己和他人造成任何形式的伤害或损失。

版权提示 | 免责声明

本文(API PUBL 4703-2001 Gas Fired Boiler - Test Report Refinery Site A Characterization of Fine Particulate Emission Factor and Specification Profiles from Stationary Petroleum Industry.pdf)为本站会员(towelfact221)主动上传,麦多课文库仅提供信息存储空间,仅对用户上传内容的表现方式做保护处理,对上载内容本身不做任何修改或编辑。 若此文所含内容侵犯了您的版权或隐私,请立即通知麦多课文库(发送邮件至master@mydoc123.com或直接QQ联系客服),我们立即给予删除!

API PUBL 4703-2001 Gas Fired Boiler - Test Report Refinery Site A Characterization of Fine Particulate Emission Factor and Specification Profiles from Stationary Petroleum Industry.pdf

1、 Gas Fired BoilerTest Report Refinery Site ACharacterization of Fine Particulate Emission Factors and Speciation Profiles from Stationary Petroleum Industry Combustion SourcesRegulatory and Scientific AffairsPUBLICATION NUMBER 4703JULY 2001Gas Fired BoilerTest Report Refinery Site ACharacterization

2、of Fine Particulate Emission Factors and Speciation Profiles from Stationary Petroleum Industry Combustion SourcesRegulatory and Scientific AffairsAPI PUBLICATION NUMBER 4703JULY 2001PREPARED UNDER CONTRACT BY:GE ENERGYANDENVIRONMENTALRESEARCHCORPORATION18 MASONIRVINE, CA 92618FOREWORDAPI PUBLICATIO

3、NS NECESSARILY ADDRESS PROBLEMS OF A GENERAL NATURE.WITH RESPECT TO PARTICULAR CIRCUMSTANCES, LOCAL, STATE, AND FEDERALLAWS AND REGULATIONS SHOULD BE REVIEWED.API IS NOT UNDERTAKING TO MEET THE DUTIES OF EMPLOYERS,MANUFACTURERS, OR SUPPLIERS TO WARN AND PROPERLY TRAIN AND EQUIPTHEIR EMPLOYEES, AND O

4、THERS EXPOSED, CONCERNING HEALTH AND SAFETYRISKS AND PRECAUTIONS, NOR UNDERTAKING THEIR OBLIGATIONS UNDERLOCAL, STATE, OR FEDERAL LAWS.NOTHING CONTAINED IN ANY API PUBLICATION IS TO BE CONSTRUED ASGRANTING ANY RIGHT, BY IMPLICATION OR OTHERWISE, FOR THEMANUFACTURE, SALE, OR USE OF ANY METHOD, APPARA

5、TUS, OR PRODUCTCOVERED BY LETTERS PATENT. NEITHER SHOULD ANYTHING CONTAINED INTHE PUBLICATION BE CONSTRUED AS INSURING ANYONE AGAINST LIABILITYFOR INFRINGEMENT OF LETTERS PATENT.All rights reserved. No part of this work may be reproduced, stored in a retrieval system, or transmitted byany means, ele

6、ctronic, mechanical, photocopying, recording, or otherwise, without prior writtenpermission from the publisher. Contact the publisher, API Publishing Services, 1220 L Street, N.W.,Washington, D.C. 20005.ACKNOWLEDGMENTSThe following people are recognized for their contributions of time and expertise

7、duringthis study and in the preparation of this report:API STAFF CONTACTKarin Ritter, Regulatory and Scientific AffairsMEMBERS OF THE PM SOURCE CHARACTERIZATION WORKGROUPLee Gilmer, Equilon Enterprises LLC, Stationary Source Emissions Research Committee, ChairpersonKarl Loos, Equilon Enterprises LLC

8、Jeff Siegell, ExxonMobil Research and EngineeringGE ENERGY AND ENVIRONMENTAL RESEARCH CORPORATIONPROJECT TEAM MEMBERSGlenn England, Project ManagerStephanie Wien, Project EngineerBob Zimperman, Field Team LeaderBarbara Zielinska, Desert Research InstituteJake McDonald, Desert Research InstituteTABLE

9、 OF CONTENTSSection PageEXECUTIVE SUMMARY ES-11.0 PROJECT DESCRIPTION .1-1PROJECT OVERVIEW 1-1PROJECT OBJECTIVES 1-2Primary Objectives.1-2Secondary Objectives.1-2TEST OVERVIEW .1-2Source Level (In-Stack) Samples1-2Dilution Stack Gas Samples .1-3Process Samples.1-4KEY PERSONNEL.1-52.0 PROCESS DESCRIP

10、TION.2-1SAMPLING LOCATIONS2-13.0 TEST PROCEDURES 3-1STACK GAS FLOW RATE, MOISTURE CONTENT ANDMOLECULAR WEIGHT3-1O2, CO2, CO, NOXAND SO23-1IN-STACK METHOD TESTS 3-6In-Stack Filterable Total PM, PM10 and PM2.5.3-7Condensible Particulate Matter Mass and Chemical Analysis. 3-12DILUTION TUNNEL TESTS. 3-1

11、5PM2.5 Mass. 3-17Elements 3-17Sulfate, Nitrate, Chloride and Ammonium 3-18Organic and Elemental Carbon. 3-19Volatile Organic Compounds . 3-19Semivolatile Organic Compounds 3-204.0 TEST RESULTS.4-1PROCESS OPERATING CONDITIONS 4-1PRELIMINARY TEST RESULTS4-1STACK CONDITIONS AND FLOW RATE.4-5CO, NOXAND

12、SO2EMISSIONS4-6IN-STACK AND IMPINGER METHOD RESULTS 4-7Particulate Mass.4-7OC, EC and SVOCs . 4-12DILUTION TUNNEL RESULTS 4-14Particulate Mass. 4-14Sulfate, Chloride, Nitrate and Ammonium 4-15OC, EC and Organic Species 4-15Elements 4-195.0 EMISSION FACTORS AND SPECIATION PROFILES5-1UNCERTAINTY.5-1EM

13、ISSION FACTORS FOR PRIMARY EMISSIONS .5-1PM2.5 SPECIATION PROFILES5-5Dilution Tunnel5-5Method 201A/202 5-8SPECIATION PROFILES FOR ORGANIC AEROSOLS .5-8Dilution Tunnel Organic Speciation .5-8Method 201A/202 Organic Speciation 5-106.0 QUALITY ASSURANCE.6-1SAMPLE STORAGE AND SHIPPING.6-1DILUTION TUNNEL

14、 FLOWS .6-1GRAVIMETRIC ANALYSIS .6-1ELEMENTAL (XRF) ANALYSIS6-3ORGANIC AND ELEMENTAL CARBON ANALYSIS 6-4SULFATE, NITRATE, CHLORIDE AND AMMONIUMANALYSIS.6-5SVOC ANALYSIS6-6VOC ANALYSIS6-8TABLE OF CONTENTS (CONTINUED)Section PageCEMS ANALYSIS 6-127.0 DISCUSSION AND FINDINGS.7-1PM2.5 MASS MEASUREMENTS7

15、-1CHEMICAL SPECIATION OF PRIMARY PM2.5 EMISSIONS7-5SECONDARY PM2.5 PRECURSOR EMISSIONS 7-11REFERENCES R-1Appendix AGLOSSARY . A-1Appendix BSI CONVERSION FACTORS. B-1LIST OF FIGURESFigure PageE-1 Speciation Profile for Primary Particulate Emissions from Gas-Fired Boiler(Refinery Site A). ES-102-1 Boi

16、ler Process Overview and Sampling/Monitoring Locations .2-23-1 Chronology for Gas-Fired Boiler (Refinery Site A) 3-33-2 CEMS Schematic .3-53-3 PM2.5/PM10 Train Configuration for Method 201A/202 .3-83-4 Method 201A (Modified) Sample Recovery Procedure 3-93-5 Method 201A Modified Sample Analysis Proce

17、dure 3-103-6 Sampling Train Configuration for EPA Method 17.3-113-7 Method 202 Sample Recovery Procedure .3-133-8 Method 202 Sample Modified Analysis Procedure .3-143-9 Dilution Tunnel Sampling System3-165-1 Speciation Profile-Dilution Tunnel PM2.5 Fractions 5-95-2 Speciation Profile-Method 201A/202

18、 .5-115-3 Organic Aerosol Mass Fraction Speciation.5-145-4 In-Stack Organic Aerosol Mass Fraction Speciation.5-177-1 Speciation of Inorganic Impinger Fraction Reanalysis (Refinery Site A) 7-27-2 Results of Laboratory Tests Showing Effect of SO2and Purge onMethod 202 Sulfate Bias 7-47-3 In-Stack and

19、Ambient Species Concentrations (Dilution Tunnel)(Refinery Site A)7-67-4 Comparison of Species Concentrations to Detection Limits (Dilution Tunnel)7-77-5 Mean Species Concentrations and Standard Deviation (Dilution Tunnel) .7-8LIST OF TABLESTable PageE-1 Summary of Primary Particulate Emission Factor

20、s for Gas-Fired RefineryBoiler . ES-4E-2 Summary of Semivolatile Organic Species Emission Factors for Gas-FiredRefinery Boiler ES-5E-3 Summary of Secondary Particulate Precursor Emission Factors for Gas-FiredRefinery Boiler. ES-8E-4 Substances of Interest Not Detected in Stack Emissions from Gas-Fir

21、ed Boiler ES-91-1 Overview of Sampling Scope 1-31-2 Summary of Analytical Targets.1-43-1 Summary of Test Procedures.3-23-2 Description of CEMS Instrumentation Used for Gas-FiredBoiler Test (Refinery Site A).3-64-1 Approximate In-Stack Detection Limits Achieved for Gas-FiredBoiler Tests (Refinery A)

22、4-24-2 Process Data for Gas-Fired Boiler (Refinery Site A)4-34-3 Fuel Gas Analyses for Gas-Fired Boiler (Refinery Site A).4-44-4 Stratification Data for Gas-Fired Boiler (Refinery Site A) .4-54-5 Stack Gas Summary for Gas-Fired Boiler (Refinery Site A) 4-64-6 CEMS Data For Gas-Fired Boiler (Refinery

23、 Site A)4-74-7 Filterable Particulate Matter (Method 201A) for Gas-Fired Boiler(Refinery Site A).4-84-8 Condensible Particulate for Gas-Fired Boiler (Refinery Site A).4-94-9 Method 202 Inorganic Residue Analysis . 4-114-10 In-Stack Organic and Elemental Carbon Results for Gas-Fired Boiler(Refinery S

24、ite A) 4-134-11 In-Stack SVOC Results for Gas-Fired Boiler (Refinery Site A) 4-134-12 Stack Gas PM2.5 Results for Gas-Fired Boiler (Refinery Site A) . 4-144-13 Ambient Air PM2.5 Results for Gas-Fired Boiler (Refinery Site A) 4-14LIST OF TABLES (CONTINUED)Table Page4-14 Dilution Tunnel Sulfate, Nitra

25、te, Chloride and Ammonium Results forGas-Fired Boiler (Refinery Site A) 4-154-15 Dilution Tunnel Organic and Elemental Carbon Results for Gas-FiredBoiler (Refinery Site A) 4-164-16 Dilution Tunnel SVOC Results for Gas-Fired Boiler (Refinery Site A) . 4-174-17 Dilution Tunnel VOC Results for Gas-Fire

26、d Boiler (Refinery Site A) . 4-204-18 Dilution Tunnel Elemental Results for Gas-Fired Boiler (Refinery Site A) 4-215-1 Primary Emissions - Particulate Mass and Elements5-25-2 Primary Emissions - Carbon and Semivolatile Organic Compounds 5-35-3 Emission Factors for Secondary Organic Aerosol Precursor

27、s (VOC).5-65-4 Emission Factors for Secondary Organic Aerosol Precursors - NOxand SO2.5-65-5 Speciation Profile for Dilution Tunnel Primary Emissions for Gas-FiredBoiler (Refinery Site A) 5-75-6 Speciation Profile for PM2.5 for Gas-Fired Boiler (Refinery Site A)(Method 201 A/202) 5-105-7 Organic Aer

28、osol Speciation Profile . 5-125-8 Organic Aerosol Speciation Profile (Method 201A/202) 5-166-1 Pre- and Post- Test Dilution Tunnel Flow Checks for the Gas-Fired Boiler(Refinery Site A).6-26-2 Method 201A/202 Blank Results.6-36-3 Results from Field Blank Acetone Rinses6-36-4 Field Blank for Elements.

29、6-46-5 Organic and Elemental Carbon Blanks and Replicate Sample (mg/dscm) 6-56-6 Ion Blank Results6-66-7 SVOC/PUF/XAD Field Blank Results 6-96-8 SVOC PUF/XAD Replicate Analysis Results 6-10ES-1EXECUTIVE SUMMARYIn 1997, the United States Environmental Protection Agency (EPA) promulgated new ambientai

30、r standards for particulate matter smaller than 2.5 micrometers in diameter (PM2.5). Sourceemissions data are needed to assess the contribution of petroleum industry combustion sources toambient PM2.5 concentrations for receptor modeling and PM2.5 standard attainment strategydevelopment. There are f

31、ew existing data on emissions and characteristics of fine aerosols frompetroleum industry combustion sources, and the limited information that is available isincomplete and outdated. The American Petroleum Institute (API) developed a test protocol toaddress this data gap, specifically to: Develop em

32、ission factors and speciation profiles for emissions of primary fineparticulate matter (i.e., particulate present in the stack flue gas includingcondensible aerosols), especially organic aerosols from gas-fired combustiondevices; and Identify and characterize secondary particulate (i.e., particulate

33、 formed viareaction of stack emissions in the atmosphere) precursor emissions.This report presents results of a pilot project to evaluate the test protocol on 550,000 pounds perhour steam (approximately 650 x 106British thermal units per hour) boiler firing refinery processgas. The tangentially fire

34、d boiler has a waterwall furnace with two rows of burners in eachcorner of the furnace. The unit has no controls for NOxemissions. The boiler operated atapproximately 57 percent of capacity, and flue gas temperature at the stack was approximately345 degrees Fahrenheit during the tests.The particulat

35、e measurements at the stack were made using both a dilution tunnel research testmethod and traditional methods for regulatory enforcement of particulate regulations. Thedilution tunnel method is attractive because the sample collection media and analysis methodsare identical to those used for ambien

36、t air sampling. Thus, the results are directly comparablewith ambient air data. Also, the dilution tunnel method is believed to provide representativeresults for condensible aerosols. Regulatory methods are attractive because they are readilyaccepted by regulatory agencies and have been used extensi

37、vely on a wide variety of sourceES-2types; existing regulatory methods for condensible aerosols may be subject to significant bias,however, and sampling/analytical options are limited.Emission factors for all species measured are extremely low, which is expected for gas-firedsources. Emission factor

38、s for primary particulate, including: total particulate, PM10 (particlessmaller than nominally 10 micrometers), and PM2.5; elements; ionic species; and organic andelemental carbon are presented in Table E-1. Since the boiler was firing refinery process gaswith a heating value different from natural

39、gas, emission factors are expressed in pounds ofpollutant per million British thermal units of gas fired (lb/MMBtu). All tests were performed intriplicate. As a measure of the bias, precision, and variability of the results, the uncertainty and95 percent confidence upper bound also are presented.Emi

40、ssion factors for semivolatile organic species are presented in Table E-2. The sum ofsemivolatile organic species is approximately three percent of the organic carbon. Emissionfactors for secondary particulate precursors (NOx, SO2, and volatile organic species with carbonnumber of 7 or greater) are

41、presented in Table E-3.The preceding tables include only those substances that were detected in at least one of the threetest runs. Substances of interest that were not present above the minimum detection limit forthese tests are listed in Table E-4.A single ambient air sample was collected at the s

42、ite. In some cases, the emission factorsreported in Tables E-1 to E-3 resulted from in-stack concentrations that were near ambient airconcentrations. Those species concentrations that are within a factor of 10 of the ambient airconcentration are indicated on the table by an asterisk (*).The primary

43、particulate results presented in Table E-1 also may be expressed as a PM2.5speciation profile, which is the mass fraction of each species contributing to the total PM2.5mass. The speciation profile is presented in Figure E-1.ES-3The main findings of these tests are: Particulate mass emissions from t

44、he boiler were extremely low, consistent with levelsexpected for gaseous fuel combustion. Two methods for determining the average emission factor for primary PM2.5 massgave results which differed in magnitude by a factor of 27: 0.000358 lb/MMBtu usingthe dilution tunnel; and 0.00974 lb/MMBtu using c

45、onventional in-stack methods forfilterable and condensible particulate. Sampling and analytical artifacts principally caused by gaseous SO2in the stack gaswere shown to produce a relatively large positive bias in condensible particulate asmeasured by conventional in-stack methods. Most of the differ

46、ence between thedilution tunnel and conventional method results can be explained by thesemeasurement artifacts. The results using conventional EPA methods are nominallyconsistent with published EPA emission factors for external combustion of naturalgas (U. S. EPA, 1998). Therefore, the published EPA

47、 emission factors derived fromtests using similar measurement methods also may be positively biased. Chemical species accounting for 74 percent of the measured PM2.5 mass werequantified. Organic and elemental carbon comprise 68 percent of the measured primary PM2.5mass. Sulfates, iron, copper, chlor

48、ide, and smaller amounts of other elements account foranother 6 percent of the measured PM2.5 mass. Less than 26 percent of the measured PM2.5 mass is unspeciated. Most elements are not present at levels significantly above the background levels inthe ambient air or the minimum detection limits of t

49、he test methods. Most organic species are not detected at levels significantly above background levelsin the ambient air or field blanks. All detected organics are present at extremely lowlevels consistent with gaseous fuel combustion. Emissions of secondary particle precursors are low and consistent with levelsexpected for gaseous fuel combustion.ES-4Table E-1. Summary of Primary Particulate Emission Factors for Gas-Fired Refinery Boiler.Substance Emission Uncertainty 95% ConfidenceParticulate Condensible Particulate (inorganic) 9.07E-3 107 1.58E-2Condensible Particulate (or

copyright@ 2008-2019 麦多课文库(www.mydoc123.com)网站版权所有
备案/许可证编号:苏ICP备17064731号-1