SG189260A1 - Low energy distillation system and method - Google Patents
Low energy distillation system and method Download PDFInfo
- Publication number
- SG189260A1 SG189260A1 SG2013025069A SG2013025069A SG189260A1 SG 189260 A1 SG189260 A1 SG 189260A1 SG 2013025069 A SG2013025069 A SG 2013025069A SG 2013025069 A SG2013025069 A SG 2013025069A SG 189260 A1 SG189260 A1 SG 189260A1
- Authority
- SG
- Singapore
- Prior art keywords
- section
- fluid
- feed
- stripper
- rectifier
- Prior art date
Links
- 238000004821 distillation Methods 0.000 title claims abstract description 55
- 238000000034 method Methods 0.000 title claims description 18
- 239000012530 fluid Substances 0.000 claims abstract description 59
- 238000012546 transfer Methods 0.000 claims abstract description 28
- 238000004891 communication Methods 0.000 claims abstract description 18
- 238000010438 heat treatment Methods 0.000 claims abstract description 7
- 239000012809 cooling fluid Substances 0.000 claims abstract description 6
- 230000005484 gravity Effects 0.000 claims description 6
- 229930195733 hydrocarbon Natural products 0.000 claims description 2
- 150000002430 hydrocarbons Chemical class 0.000 claims description 2
- 239000007788 liquid Substances 0.000 description 15
- 239000000047 product Substances 0.000 description 11
- 238000013461 design Methods 0.000 description 9
- 238000010992 reflux Methods 0.000 description 9
- 230000006835 compression Effects 0.000 description 5
- 238000007906 compression Methods 0.000 description 5
- 238000000926 separation method Methods 0.000 description 5
- 241000196324 Embryophyta Species 0.000 description 4
- 239000007795 chemical reaction product Substances 0.000 description 4
- 238000005192 partition Methods 0.000 description 4
- 238000009835 boiling Methods 0.000 description 3
- 230000010354 integration Effects 0.000 description 3
- 238000007670 refining Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 239000000498 cooling water Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000012263 liquid product Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 241000202755 Areca Species 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000009420 retrofitting Methods 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
- 238000010977 unit operation Methods 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/28—Evaporating with vapour compression
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/007—Energy recuperation; Heat pumps
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
- B01D3/143—Fractional distillation or use of a fractionation or rectification column by two or more of a fractionation, separation or rectification step
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
- B01D3/32—Other features of fractionating columns ; Constructional details of fractionating columns not provided for in groups B01D3/16 - B01D3/30
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US39035810P | 2010-10-06 | 2010-10-06 | |
PCT/US2011/054854 WO2012047953A1 (en) | 2010-10-06 | 2011-10-05 | Low energy distillation system and method |
Publications (1)
Publication Number | Publication Date |
---|---|
SG189260A1 true SG189260A1 (en) | 2013-05-31 |
Family
ID=44802411
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SG10201507750XA SG10201507750XA (en) | 2010-10-06 | 2011-10-05 | Low energy distillation system and method |
SG2013025069A SG189260A1 (en) | 2010-10-06 | 2011-10-05 | Low energy distillation system and method |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SG10201507750XA SG10201507750XA (en) | 2010-10-06 | 2011-10-05 | Low energy distillation system and method |
Country Status (8)
Country | Link |
---|---|
US (1) | US20120085126A1 (zh) |
EP (1) | EP2624928A1 (zh) |
KR (1) | KR20130143577A (zh) |
CN (1) | CN103237580B (zh) |
BR (1) | BR112013008394A2 (zh) |
CA (1) | CA2813892A1 (zh) |
SG (2) | SG10201507750XA (zh) |
WO (1) | WO2012047953A1 (zh) |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20140183027A1 (en) * | 2011-05-09 | 2014-07-03 | Fluor Technologies Corporation | Internal heat exchanger for distillation column |
JP6266876B2 (ja) * | 2012-11-15 | 2018-01-24 | 東洋エンジニアリング株式会社 | 蒸留装置とその制御方法 |
JP6033050B2 (ja) | 2012-11-16 | 2016-11-30 | 東洋エンジニアリング株式会社 | 芳香族炭化水素製造装置 |
US20140262729A1 (en) * | 2013-03-14 | 2014-09-18 | Elwha Llc | Heat transfer between a distillation column and a temperature source |
DE102013214765A1 (de) * | 2013-07-29 | 2015-01-29 | Wacker Chemie Ag | Verfahren und Vorrichtung zur destillativen Trennung eines Drei- oder Mehrkomponentengemisches |
JP6140591B2 (ja) * | 2013-11-21 | 2017-05-31 | 東洋エンジニアリング株式会社 | 蒸留装置 |
JP6289112B2 (ja) * | 2014-01-17 | 2018-03-07 | 東洋エンジニアリング株式会社 | 蒸留塔 |
CN105884103A (zh) * | 2014-09-03 | 2016-08-24 | 中石化洛阳工程有限公司 | 一种酸性水汽提方法 |
DE102014220539A1 (de) | 2014-10-09 | 2016-04-14 | Wacker Chemie Ag | Reinigung von Chlorsilanen mittels Destillation und Adsorption |
CN104524800B (zh) * | 2014-12-31 | 2016-06-22 | 石家庄工大化工设备有限公司 | 一种具有换热塔板的热耦合喷射并流塔 |
US20160216040A1 (en) * | 2015-01-23 | 2016-07-28 | Indigo Power Systems Llc | Heat exchanger |
JP6566876B2 (ja) * | 2016-01-26 | 2019-08-28 | 東洋エンジニアリング株式会社 | 内部熱交換型蒸留塔の熱交換量調節方法 |
CN106693425B (zh) * | 2016-12-13 | 2023-04-07 | 浙江科茂能源科技有限公司 | 一种高效节能板式换热蒸馏装置 |
US10539364B2 (en) * | 2017-03-13 | 2020-01-21 | General Electric Company | Hydrocarbon distillation |
CN113274755B (zh) * | 2021-05-24 | 2022-05-13 | 大连理工大学 | 一种碘硫循环中硫酸相热分解制备氧气的工艺与装置 |
Family Cites Families (26)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2804292A (en) * | 1949-02-02 | 1957-08-27 | Air Prod Inc | Gas-liquid contact apparatus |
GB776154A (en) * | 1952-12-19 | 1957-06-05 | Ruetgerswerke Ag | Improvements in and relating to the fractional distillation of mixtures of liquids |
US3575007A (en) * | 1968-03-26 | 1971-04-13 | Treadwell Corp | Isothermal fractional distillation of materials of differing volatilities |
US3969450A (en) * | 1973-11-14 | 1976-07-13 | Standard Oil Company | Heat-exchanger trays and system using same |
US4234391A (en) * | 1978-10-13 | 1980-11-18 | University Of Utah | Continuous distillation apparatus and method |
US4277268A (en) * | 1979-10-17 | 1981-07-07 | Conoco, Inc. | Heat pump fractionation process |
US4706739A (en) * | 1985-04-26 | 1987-11-17 | Noren Don W | Heat exchanger |
US4961826A (en) * | 1986-02-13 | 1990-10-09 | Trustees Of Dartmouth College | Distillation process for ethanol |
US4737177A (en) * | 1986-08-01 | 1988-04-12 | Erickson Donald C | Air distillation improvements for high purity oxygen |
US5351492A (en) * | 1992-09-23 | 1994-10-04 | Air Products And Chemicals, Inc. | Distillation strategies for the production of carbon monoxide-free nitrogen |
US5435436A (en) * | 1994-01-21 | 1995-07-25 | Manley; David B. | Thermomechanically integrated distillation of close-boiling light hydrocarbons |
DE69529146T2 (de) * | 1994-08-29 | 2003-11-13 | Kansai Chemical Engineering Co., Ltd. | Destillationskolonne mit innerem wärmeaustausch |
US6045660A (en) * | 1996-03-08 | 2000-04-04 | Savage; Kern | Mechanically assisted two-phase contactor and fuel ethanol production system |
US5737940A (en) * | 1996-06-07 | 1998-04-14 | Yao; Jame | Aromatics and/or heavies removal from a methane-based feed by condensation and stripping |
US6605190B1 (en) * | 1997-02-14 | 2003-08-12 | San Diego State University Foundation | Staged optimal externally-controlled systems and method thereof |
AUPO775697A0 (en) * | 1997-07-07 | 1997-07-31 | Inland Oil Refiners (Qld) Pty Ltd | Method and apparatus for fractional distillation |
JP2004033844A (ja) * | 2002-07-01 | 2004-02-05 | Kimura Chem Plants Co Ltd | 内部熱交換型蒸留塔 |
DE102005004948B3 (de) * | 2005-02-02 | 2006-03-02 | Uhde Gmbh | Verfahren zur Erhöhung der Selektivität von physikalisch wirkenden Lösungsmitteln bei einer Absorption von Gaskomponenten aus technischen Gasen |
CN101015747A (zh) * | 2006-09-07 | 2007-08-15 | 浙江大学 | 一种基于内部热交换的精馏节能装置 |
DE102007004788A1 (de) * | 2007-01-31 | 2008-08-07 | Bayer Technology Services Gmbh | Verfahren zur Destillation eines biologisch erzeugten Alkohols |
US8002952B2 (en) * | 2007-11-02 | 2011-08-23 | Uop Llc | Heat pump distillation |
CN101549211B (zh) * | 2009-04-21 | 2011-07-20 | 西安交通大学 | 热泵精馏节能改造方法和装置 |
JP4803470B2 (ja) * | 2009-10-05 | 2011-10-26 | 独立行政法人産業技術総合研究所 | 熱交換型蒸留装置 |
JP5956772B2 (ja) * | 2012-02-20 | 2016-07-27 | 東洋エンジニアリング株式会社 | 熱交換型蒸留装置 |
JP5923335B2 (ja) * | 2012-02-24 | 2016-05-24 | 東洋エンジニアリング株式会社 | 熱交換型蒸留装置 |
JP5923367B2 (ja) * | 2012-03-30 | 2016-05-24 | 東洋エンジニアリング株式会社 | 熱交換型蒸留装置 |
-
2011
- 2011-10-03 US US13/251,624 patent/US20120085126A1/en not_active Abandoned
- 2011-10-05 CA CA2813892A patent/CA2813892A1/en not_active Abandoned
- 2011-10-05 KR KR1020137011371A patent/KR20130143577A/ko not_active Application Discontinuation
- 2011-10-05 CN CN201180058527.4A patent/CN103237580B/zh not_active Expired - Fee Related
- 2011-10-05 BR BR112013008394A patent/BR112013008394A2/pt not_active IP Right Cessation
- 2011-10-05 SG SG10201507750XA patent/SG10201507750XA/en unknown
- 2011-10-05 SG SG2013025069A patent/SG189260A1/en unknown
- 2011-10-05 EP EP11770624.2A patent/EP2624928A1/en not_active Withdrawn
- 2011-10-05 WO PCT/US2011/054854 patent/WO2012047953A1/en active Application Filing
Also Published As
Publication number | Publication date |
---|---|
CN103237580B (zh) | 2015-08-19 |
CN103237580A (zh) | 2013-08-07 |
KR20130143577A (ko) | 2013-12-31 |
US20120085126A1 (en) | 2012-04-12 |
EP2624928A1 (en) | 2013-08-14 |
CA2813892A1 (en) | 2012-04-12 |
SG10201507750XA (en) | 2015-10-29 |
BR112013008394A2 (pt) | 2016-06-21 |
WO2012047953A1 (en) | 2012-04-12 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US20120085126A1 (en) | Low energy distillation system and method | |
TWI632948B (zh) | 使用分隔管柱之分離方法 | |
JP5720669B2 (ja) | 高純度の2−エチルヘキサノール生産のための分離壁型蒸留塔及びこれを利用した分別蒸留方法 | |
US8440056B2 (en) | Heat integrated distillation apparatus | |
EP2555842B1 (en) | Process and equipment for separating 1,2,4 trimethylbenzene (pseudocumene) from a mixture containing aromatic hydrocarbons | |
JP5783491B2 (ja) | 高純度のネオペンチルグリコール生産のための分離壁型蒸留塔及びこれを利用した製造方法 | |
JP5696954B2 (ja) | 高純度の2−エチルヘキシル−アクリレート生産のための分離壁型蒸留塔及びこれを利用した製造方法 | |
RU2500450C2 (ru) | Усовершенствованный тепловой насос для высокочистого кубового продукта | |
US8002952B2 (en) | Heat pump distillation | |
JP6518233B2 (ja) | 三成分または多成分混合物の蒸留による分離のための方法および装置 | |
JP2012520347A (ja) | 高純度のアクリル酸生産のための分離壁型蒸留塔及びこれを利用した分別蒸留方法 | |
JP6140374B2 (ja) | 3成分または多成分の混合物を蒸留により分離するための方法および装置 | |
JP2012515771A (ja) | 高純度のノルマルブタノール生産用分離壁型蒸留塔、及びノルマルブタノール蒸留方法 | |
US7129387B2 (en) | Low capital implementation of distributed distillation in ethylene recovery | |
RU2617506C2 (ru) | Способ и установка для дистилляции метанола с регенерацией тепла | |
KR20140063455A (ko) | 증류 장치와 이를 제어하는 방법 | |
Voinov et al. | A study of diabatic distillation in a column with a low pressure drop | |
Madyshev et al. | Energy saving in distillation by combining vortex contact device and thermal effects | |
JP2023531131A (ja) | 蒸留のための方法および装置 | |
RU2394064C2 (ru) | Способ перегонки нефти | |
US4484985A (en) | Distillation and condensing process | |
CN207085373U (zh) | 一种使用稳定性高的氟苯加工用分离器 | |
KR20240093735A (ko) | N-부탄올의 정제를 위한 방법 | |
RU2188845C1 (ru) | Способ получения газоконденсатных фракций | |
Kharkov | Thermal Distillation Study on Heat and Mass Transfer Improvement of Column Contact Devices |