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本文(API MPMS 19.1-2012 Manual of Petroleum Measurement Standards Chapter 19.1 Evaporative Loss From Fixed-Roof Tanks (Fourth Edition)《石油计量标准手册.第19.1章 固定罐顶蒸发损失.第4版》.pdf)为本站会员(roleaisle130)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 MPMS 19.1-2012 Manual of Petroleum Measurement Standards Chapter 19.1 Evaporative Loss From Fixed-Roof Tanks (Fourth Edition)《石油计量标准手册.第19.1章 固定罐顶蒸发损失.第4版》.pdf

1、Manual of Petroleum Measurement StandardsChapter 19.1Evaporative Loss From Fixed-Roof TanksFOURTH EDITION, OCTOBER 2012Manual of Petroleum Measurement StandardsChapter 19.1Evaporative Loss From Fixed-Roof TanksMeasurement CoordinationFOURTH EDITION, OCTOBER 2012Special NotesAPI publications necessar

2、ily address problems of a general nature. With respect to particular circumstances, local,state, and federal laws and regulations should be reviewed.Neither API nor any of APIs employees, subcontractors, consultants, committees, or other assignees make anywarranty or representation, either express o

3、r implied, with respect to the accuracy, completeness, or usefulness of theinformation contained herein, or assume any liability or responsibility for any use, or the results of such use, of anyinformation or process disclosed in this publication. Neither API nor any of APIs employees, subcontractor

4、s,consultants, or other assignees represent that use of this publication would not infringe upon privately owned rights.API publications may be used by anyone desiring to do so. Every effort has been made by the Institute to assure theaccuracy and reliability of the data contained in them; however,

5、the Institute makes no representation, warranty, orguarantee in connection with this publication and hereby expressly disclaims any liability or responsibility for loss ordamage resulting from its use or for the violation of any authorities having jurisdiction with which this publication mayconflict

6、.API publications are published to facilitate the broad availability of proven, sound engineering and operatingpractices. These publications are not intended to obviate the need for applying sound engineering judgmentregarding when and where these publications should be utilized. The formulation and

7、 publication of API publicationsis not intended in any way to inhibit anyone from using any other practices.Any manufacturer marking equipment or materials in conformance with the marking requirements of an API standardis solely responsible for complying with all the applicable requirements of that

8、standard. API does not represent,warrant, or guarantee that such products do in fact conform to the applicable API standard.Users of this standard should not rely exclusively on the information contained in this document. Sound business,scientific, engineering, and safety judgment should be used in

9、employing the information contained herein.All rights reserved. No part of this work may be reproduced, translated, stored in a retrieval system, or transmitted by any means, electronic, mechanical, photocopying, recording, or otherwise, without prior written permission from the publisher. Contact t

10、he Publisher, API Publishing Services, 1220 L Street, NW, Washington, DC 20005.Copyright 2012 American Petroleum InstituteForewordNothing contained in any API publication is to be construed as granting any right, by implication or otherwise, for themanufacture, sale, or use of any method, apparatus,

11、 or product covered by letters patent. Neither should anythingcontained in the publication be construed as insuring anyone against liability for infringement of letters patent.Shall: As used in a standard, “shall” denotes a minimum requirement in order to conform to the specification.Should: As used

12、 in a standard, “should” denotes a recommendation or that which is advised but not required in orderto conform to the specification.This document was produced under API standardization procedures that ensure appropriate notification andparticipation in the developmental process and is designated as

13、an API standard. Questions concerning theinterpretation of the content of this publication or comments and questions concerning the procedures under whichthis publication was developed should be directed in writing to the Director of Standards, American PetroleumInstitute, 1220 L Street, NW, Washing

14、ton, DC 20005. Requests for permission to reproduce or translate all or any partof the material published herein should also be addressed to the director.Generally, API standards are reviewed and revised, reaffirmed, or withdrawn at least every five years. A one-timeextension of up to two years may

15、be added to this review cycle. Status of the publication can be ascertained from theAPI Standards Department, telephone (202) 682-8000. A catalog of API publications and materials is publishedannually by API, 1220 L Street, NW, Washington, DC 20005.Suggested revisions are invited and should be submi

16、tted to the Standards Department, API, 1220 L Street, NW,Washington, DC 20005, standardsapi.org.iiiSummary of Changes to API MPMS Chapters 19.1, 19.2 and 19.4The third edition of API Manual of Petroleum Measurement Standards (MPMS) Chapter 19.4 was published followinga revision that was carried out

17、concurrently with revisions to Chapter 19.1, published as the fourth edition, andChapter 19.2, published as the third edition. Primary changes are:1) Consolidation of common material in Chapter 19.4. Material that had previously been included in both Chapters19.1 and 19.2 has been moved to Chapter 1

18、9.4. Chapter 19.4, which was previously Recommended Practice forSpeciation of Evaporative Losses, now has the title Evaporative Loss Reference Information and SpeciationMethodology. This Chapter had already contained reference information on the properties of chemicals andtypical petroleum liquids,

19、and this information has now been removed from Chapters 19.1 and 19.2. In addition,meteorological data have been moved from Chapters 19.1 and 19.2 to Chapter 19.4. In the revised documents:a) Meteorological data are found in Chapter 19.4,b) Calculation of storage tank temperatures is found in Chapte

20、rs 19.1 and 19.2 (in that fixed-roof tanks involvecalculation of the vapor space temperature in order to determine vapor density, whereas this step is notinvolved in estimating emissions from floating-roof tanks), andc) Calculation of true vapor pressure is found in Chapter 19.4 (in that this is now

21、 calculated in the same mannerfor both fixed- and floating-roof tanks).2) Reconciliation of nomenclature. Chapters 19.1 and 19.2 previously had different nomenclature for the samevariables. These revisions adopt a common set of symbols for both chapters.3) Reorganization of the formats. In addition

22、to common material having been removed from Chapters 19.1 and 19.2,the remaining text has been edited to remove unnecessarily verbose or repetitive language. The summary tableswere deemed redundant, and have been deleted.4) Appendices. Appendices have been redesignated as annexes. 5) SI units. An an

23、nex has been added to each chapter to address SI units.Chapter 19.1, fourth editionIn addition to common reference material being deleted from Chapter 19.1, the following changes have been made:1) Reference to API Technical Reports. References to API TR 2568 (cleaning storage tanks) and API TR 2569(

24、closed vent IFRTs) have been added.2) Terminology. The following terminology has been revised:a) “Standing storage loss” has been changed to “standing loss.”b) “Solar insolation” has been changed to “insolation.”3) Effective Throughput. An expression has been added for the sum of changes in liquid l

25、evel, designated HQ, forcalculating effective throughput.4) Normal operating pressure. An expression has been added for calculating the normal operating pressure, as theaverage of the maximum and minimum vent settings.5) Vapor density from vapor space temperature. The temperature used in the calcula

26、tion of vapor density has beenchanged from the liquid surface temperature to the vapor space temperature, and an equation has been added fordetermining the vapor space temperature.vContentsPage1 Scope . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .

27、 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 12 Normative References. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 13 Symbols . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .

28、 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 24 Procedure for Estimating Loss . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 34.1 General . . . . . . . . . . . . . . . . . .

29、 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 34.2 Standing Loss LS. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 34.3 W

30、orking Loss LW. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 95 Example . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .

31、 . . . . . . . . . . . . . . 115.1 Parameters . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 115.2 Solution. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .

32、. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 116 Equipment Descriptions . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 136.1 General . . . . . . . . . . . . . . . . . . . . . . . . . . .

33、 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 136.2 Fixed-Roof Tanks. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 146.3 Roof Fittings. . . .

34、. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 146.4 Insulation . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .

35、 . . . . . . . . 156.5 Outside Surfaces of the Tank. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 167 Loss Mechanisms . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .

36、 . . . . . . . . . . . . . . . . . . 167.1 General . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 167.2 Standing Loss . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .

37、 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 167.3 Working Loss. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 178 Development of Estimation Methods . . . . . . . .

38、 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 188.1 General . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 188.2 Standing Loss . . . . . .

39、 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 198.3 Working Loss. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .

40、 . . 23Annex A (informative) SI units . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 25Bibliography . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .

41、 . . . . . . . . . . . . . . . . . . . . . . 26Figures1 Fixed-Roof Tank Geometry. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 52 Typical Fixed-Roof Tank . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .

42、 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14vii1 Chapter 19.1Evaporative Loss From Fixed-Roof Tanks 1 Scope This standard contains methodologies for estimating the total evaporative losses of hydrocarbons from fixed-roof tanks. The methodologies provide loss estimates for

43、general equipment types based on laboratory, test-tank and field-tank data. Types of fixed-roof tanks and roof fittings described are for information only. The equations estimate average annual losses from uninsulated fixed-roof tanks for various liquid stocks, stock vapor pressures, tank sizes, met

44、eorological conditions, and operating conditions. The following special cases are addressed: a) Horizontal tanks. b) Higher volatility stocks (true vapor pressure greater than 0.1 psia). c) Vent settings higher than 0.03 psia (0.5 oz/in2). The estimation may be improved by using detailed field infor

45、mation, including climatic data and operational data for the appropriate time period. The equations are not intended to be used in the following applications: a) To estimate losses from unstable or boiling stocks or from petroleum liquids or petrochemicals for which the vapor pressure is not known o

46、r cannot readily be predicted (to calculate emissions from tanks that contain material at or above their boiling point or the point at which material starts to flash, the API model E LW(lb/yr) is determined in 4.3. 4.2 Standing Loss LS4.2.1 Aboveground and Underground Tanks a) For aboveground tanks,

47、 the standing loss LS(lb/yr) is: LS= 365(D2/4) HVOKSKEWV(2) where D, HVO, KS, KE, and WVare determined in 4.2.2 through 4.2.6, respectively; The constant 365 has units of days/yr. b) For underground tanks, assume no standing loss occurs (LS= 0) because the insulating nature of the earth limits the d

48、iurnal temperature change. 4.2.2 Tank Diameter D The tank diameter D (ft) is: a) For vertical tanks, D = DV (3a) where DVis the cylindrical diameter of a vertical tank (ft). 4 API MPMS CHAPTER 19.1 b) For horizontal tanks, D =HHDL4(3b) where LHis the end-to-end length of a horizontal tank (ft); DHis

49、 the cylindrical diameter of a horizontal tank (ft). 4.2.3 Vapor Space Outage HVOThe vapor space outage HVO(ft), the height of a cylinder of diameter D whose volume equals the vapor space volume of a fixed-roof tank, is: a) For vertical tanks (see Figure 1): HVO= HS HL+ HRO(4a) where HSis the tank shell height (ft); HLis the average liquid height (ft); If HLis unknown, use HL= (HLX+ HLN)/2 (5a) where HLXis maximum liquid height (ft); HLNis minimum liquid height (ft) (height of remaining heel when emptied). If HLXor HLNis unknown, use HL= HS/2 (5b)HROis the roof outage (ft), the shell

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