MY169293A - A method for recovering hexane - Google Patents

A method for recovering hexane

Info

Publication number
MY169293A
MY169293A MYPI2012004750A MYPI2012004750A MY169293A MY 169293 A MY169293 A MY 169293A MY PI2012004750 A MYPI2012004750 A MY PI2012004750A MY PI2012004750 A MYPI2012004750 A MY PI2012004750A MY 169293 A MY169293 A MY 169293A
Authority
MY
Malaysia
Prior art keywords
flow
heat
hexane
exchange
zone
Prior art date
Application number
MYPI2012004750A
Inventor
Bin Zhang
Yu Sha
Deqin Xu
Chunxia Cui
Biya Gao
Shunqiang Kuang
Kun He
Shijun Lu
Original Assignee
China Petroleum & Chem Corp
Sinopec Shanghai Eng Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by China Petroleum & Chem Corp, Sinopec Shanghai Eng Co Ltd filed Critical China Petroleum & Chem Corp
Publication of MY169293A publication Critical patent/MY169293A/en

Links

Landscapes

  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The present invention provides a method for recovering hexane, comprising the following steps, a flow (8) comprising water. oligomers and hexane is evaporated in an evaporation zone. to obtain a gas-phase flow (10) comprising water and hexane: the gas-phase flow (10) is subjected to heat-exchange in a heat exchange zone, to obtain a post-heat-exchange flow (12) with a reduced temperature: the post-heat-exchange flow (12) is distilled in a dehydration zone in an azeotropic manner. to obtain a hexane flow (14) and a gas-phase mixture flow (13) comprising hexane and water: wherein the post-heat-exchange flow (12) has a temperature of T1, temperature enough to make the post-heat-exchange flow (12) form the gas-phase mixture flow (13) comprising hexane and water in the dehydration zone is T1. conditions of the heat exchange in the heat exchange zone ensure that T2>T1. and the difference value between T2 and T1 is greater than 0 and not greater than 20?C. The method of the present invention makes full use of the heat carried by the gas-phase flow (10) obtained by the evaporation zone and lowers the consumption of low-pressure steam and circulated water for cooling: further reduces the heat load of the dehydration zone.
MYPI2012004750A 2012-03-28 2012-10-25 A method for recovering hexane MY169293A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN201210084778 2012-03-28
CN201210389932.0A CN103360194B (en) 2012-03-28 2012-10-15 A kind of Hexane recovery method

Publications (1)

Publication Number Publication Date
MY169293A true MY169293A (en) 2019-03-21

Family

ID=49362553

Family Applications (1)

Application Number Title Priority Date Filing Date
MYPI2012004750A MY169293A (en) 2012-03-28 2012-10-25 A method for recovering hexane

Country Status (2)

Country Link
CN (1) CN103360194B (en)
MY (1) MY169293A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109013126A (en) * 2018-08-03 2018-12-18 诚亿电子(嘉兴)有限公司 Diluent recovery unit and its recovery method
KR102552143B1 (en) * 2019-09-27 2023-07-05 주식회사 엘지화학 METHOD AND APPARATUS FOR PREPARING n-HEXANE
CN111925269B (en) * 2020-07-30 2023-06-27 陕西延长石油延安能源化工有限责任公司 Hexane refining system and method based on production of high-density polyethylene

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2592814A (en) * 1947-12-20 1952-04-15 Du Pont Isolation of chlorosulfonated polymers of ethylene from solution
US7550065B2 (en) * 2005-04-21 2009-06-23 Lyondell Chemical Technology, L.P. Method for recovering solvents
CN202164246U (en) * 2011-08-12 2012-03-14 中国石油天然气股份有限公司 Refining system producing high-density polyvinyl cyclohexene by adopting slurry method

Also Published As

Publication number Publication date
CN103360194A (en) 2013-10-23
CN103360194B (en) 2015-10-21

Similar Documents

Publication Publication Date Title
EA201790918A1 (en) REFRIGERATOR IN WHICH THE MATERIAL WITH A PHASE TRANSITION IS USED AS A HEAT BATTERY
AR097109A1 (en) METHOD FOR PRODUCING A HYDROLYZED QUERATIN MATERIAL
GB2519028A (en) Improvements to refrigeration systems
MY169293A (en) A method for recovering hexane
WO2013060633A3 (en) Refrigeration device having an evaporation pan
WO2012123268A3 (en) Refrigerator comprising a heat accumulator
EA201690040A1 (en) METHOD FOR OBTAINING SEMI-AROMATIC SEMI-CRYSTALLINE POLYAMIDE
CN103254876B (en) A kind of transformation temperature is the phase change material of-15 DEG C
Yan et al. The spatio temporal evolution characteristics and response of regional climate change of NDVI at Jiangsu coastal areas
CN204445405U (en) A kind of drinker hot guard system utilizing heat of compressor
GR20140100409A (en) High-erformance heat pump with absorption of plural solutions
ES2542783T3 (en) Procedure for the manufacture of tea products
CN103589842A (en) Method for improving cast iron hardness
CN204939339U (en) A kind of crude benzol extraction element
MX2012011246A (en) Interconversion between isomeric p-menthane-3-carboxylic acids.
Shevtsov Thermal power loss compensation in the production of cooked and dried grains with heat pumps using
Rubio The Hygroscopic cycle for CSP
CN106801119A (en) A kind of water system heat treatment solution
CN106755816A (en) A kind of cooling agent for the quenching of band large-scale metal part
CN102899596A (en) Technology for processing zinc alloy
UA75925U (en) PASTERIZATION INSTALLATION
MX2015001770A (en) Refrigeration and chilling system by vapor compression with independent cycles.
TH165126A (en)
MX2012000635A (en) Cooling system based on a static condenser for commercial refrigeration.
UA77776U (en) Ecofriendly low pressure heat pump