[1]周元欣,梁 勇,信 鹏,等.丁烷低温常压储罐蒸发气泄放量计算[J].石油化工设备,2020,(06):31-38.[doi:10.3969/j.issn.1000-7466.2020.06.007]
 ZHOU Yuan-xin,LIANG Yong,XIN Peng,et al.Calculation of Boiled Off Gas Relief Quantity for Butane Cryogenic Atmospheric Storage Tank[J].Petro-Chemical Equipment,2020,(06):31-38.[doi:10.3969/j.issn.1000-7466.2020.06.007]
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丁烷低温常压储罐蒸发气泄放量计算()
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石油化工设备[ISSN:1000-7466/CN:62-1078/TQ]

卷:
期数:
2020年06期
页码:
31-38
栏目:
设计计算
出版日期:
2020-12-30

文章信息/Info

Title:
Calculation of Boiled Off Gas Relief Quantity for Butane Cryogenic Atmospheric Storage Tank
作者:
周元欣梁 勇信 鹏远双杰
中国石油天然气管道工程有限公司,河北 廊坊 065000
Author(s):
ZHOU Yuan-xinLIANG YongXIN PengYUAN Shuang-jie
China Petroleum Pipeline Engineering Corporation,Langfang 065000,China
关键词:
低温常压储罐丁烷蒸发气泄放量
Keywords:
cryogenic atmospheric storage tankbutaneboiled off gasrelief quantity
分类号:
TQ053.2
DOI:
10.3969/j.issn.1000-7466.2020.06.007
文献标志码:
A
摘要:
简要介绍了丁烷组分及其低温储存系统的工艺流程。分析了导致丁烷低温常压储罐超压的各工况,分别计算了各工况下的丁烷蒸发气泄放量,根据可能组合工况下的超压排放量,选择最大排放量来确定储罐系统的最大超压泄放量,提出了丁烷低温常压储罐安全泄放系统蒸发气泄放量计算的基本方法,确定了丁烷低温常压储罐安全阀和真空安全阀选型的设计质量流量。
Abstract:
The butane components and process flow of butane cryogenic storage system were briefly introduced. Various conditions leading to overpressure of cryogenic atmospheric tank for butane storage were analyzed and the boiled off gas quantity under each condition was calculated respectively. According to the possible combination of conditions,the maximum overpressure gas flow rate was selected for the design of the relief system of the cryogenic atmospheric tank for butane storage and the design flow rate of safety valve and vacuum relief valve were determined for the butane cryogenic atmospheric tank.

参考文献/References:

[1] 王海波,吴殊斌,王海,等.液化轻烃低温储罐安全排放去向的探讨[J].化肥设计,2018,56(2):34-37.WANG H B,WU S B,WANG H,et al. Exploration on the safe discharging of liquefied light hydrocarbon cryogenic tank[J]. Chemical fertilizer design,2018,56(2):34-37.[2] 胡春生.浅谈大型全冷冻式液化烃储罐安全技术应用[J].化工管理,2018(27):146-147.HU C S. Talking about the safety technology application of large-scale refrigerated liquefied hydrocarbon storage tank[J].Chemical enterprise management,2018(27):146-147.[3] 赵琦.浅谈大型低温液化石油气储罐设计方案的选择[J].化肥设计,2003,41(3):32-33,43.ZHAO Q. Briefly discussing design scheme selection for bigsized and low temperature LPG storage tank[J]. Chemi- cal fertilizer design,2003,41(3):32-33,43.[4] 朱阳明,赵保林,张广营,等.浅析低温丙烷罐区的安全设计[J].化肥设计,2014,52(1):27-30.ZHU Y M,ZHAO B L,ZHANG G Y,et al. Analyzing safety design in low temperature propane tank area[J]. Chemical fertilizer design,2014,52(1):27-30.[5] 王海波,高孜孜,郝黎霞,等.LPG低温常压储罐内物料翻滚的原因及措施[J].化肥设计,2019,57(1):27-29.WANG H B,GAO Z Z,HAO L X,et al. Causes and cou- ntermeasures of material tumbling in LPG cryogenic storage tank with atmospheric pressure[J]. Chemical fertilizer design,2019,57(1):27-29.[6] 李向欣,张浩.不同储存条件下LPG储罐泄漏事故危害范围的对比分析[J].安全,2019,40(3):30-34.LI X X,ZHANG H. Contrastive analysis on hazard range of leakage accident of liquefied petroleum gas tank under different storage conditions[J]. Safety,2019,40(3):30-34.[7] 周元欣,孟凡鹏,梁勇,等.丙烷低温常压双金属全容储罐安全保护系统的定量分析计算[J].化工自动化及仪表,2020,47(4):322-328.ZHOU Y X,MENG F P,LIANG Y,et al. Quantitative analysis and calculation of safety protection system for propane low-temperature atmospheric bimetal storage tank[J]. Control and instruments in chemical industry,2020,47(4):322-328.[8] 陈健,马政足,季龙剑,等.大型LNG低温常压储罐设计[J].广东化工,2015,42(19):143-144.CHEN J,MA Z Z,JI L J,et al. Design of large,low temperature,atmospheric pressure LNG storage tanks[J]. Guangdong chemical industry,2015,42(19):143-144.[9] 张国宾,刘红兵.常压低温储罐的类型及建造技术[J].石油工程建设,2000,26(2):25-28.ZHANG G B,LIU H B. Types and erection techniques for atmospheric pressure low temperature storage tank[J]. Petroleum engineering construction,2000,26(2):25-28.[10] 王冰.常压低温乙烯储罐的安全仪表系统设计[J].石油化工自动化,2014,50(3):9-13.WANG B. Design of safety instrumented system for the atmospheric pressure and cryogenic ethylene storage tank[J]. Automation in petro-chemical industry,2014,50(3):9-13.[11] 刘岩,邹强.液化天然气低温常压储罐结构[J].油气田地面工程,2002,21(3):55,60.LIU Y,ZOU Q. Low temperature & atmospheric storage structure of liquefied petroleum gas (LPG)[J].Oil-gasfield surface engineering,2002,21(3):55,60.[12] 邢献军,杨必应,周晓清,等.大型低温常压液化石油气 储罐的设计[J].压力容器,2001,18(1):48-50.XING X J,YANG B Y,ZHOU X Q,et al. The design development of the low-temperature normal pressure and large LPG storage tank[J]. Pressure vessel techology,2001,18(1):48-50.[13] Venting atmospheric and low-pressure storage tanks:API 2000—2014[S].[14] 祁超忠.LNG船舶与全冷式LPG船舶运输管理的异同[J].航海技术,2009(4):3-6.QI C Z. The similarities and differences between LNG ship and fully cooled LPG ship transportation management[J]. Marine technology,2009(4):3-6.[15] H T Hashemi,H R Wesson. Cut LNG storage costs[J]. Hydrocarbon processing,1971,50(8):117-120.[16] Installation and equipment for liquefied natural gas— Design of onshore installations:BS EN 1473—2016[S].

更新日期/Last Update: 1900-01-01