SG11201604668WA - Extraction column and method for extracting a component from a fluid - Google Patents
Extraction column and method for extracting a component from a fluidInfo
- Publication number
- SG11201604668WA SG11201604668WA SG11201604668WA SG11201604668WA SG11201604668WA SG 11201604668W A SG11201604668W A SG 11201604668WA SG 11201604668W A SG11201604668W A SG 11201604668WA SG 11201604668W A SG11201604668W A SG 11201604668WA SG 11201604668W A SG11201604668W A SG 11201604668WA
- Authority
- SG
- Singapore
- Prior art keywords
- extracting
- fluid
- component
- extraction column
- extraction
- Prior art date
Links
- 238000000605 extraction Methods 0.000 title 1
- 239000012530 fluid Substances 0.000 title 1
- 238000000034 method Methods 0.000 title 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/42—Separation; Purification; Stabilisation; Use of additives
- C07C51/48—Separation; Purification; Stabilisation; Use of additives by liquid-liquid treatment
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/04—Solvent extraction of solutions which are liquid
- B01D11/0426—Counter-current multistage extraction towers in a vertical or sloping position
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/04—Solvent extraction of solutions which are liquid
- B01D11/0426—Counter-current multistage extraction towers in a vertical or sloping position
- B01D11/043—Counter-current multistage extraction towers in a vertical or sloping position with stationary contacting elements, sieve plates or loose contacting elements
-
- 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
- B01D3/141—Fractional distillation or use of a fractionation or rectification column where at least one distillation column contains at least one dividing wall
-
- 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
- B01D3/34—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping with one or more auxiliary substances
- B01D3/40—Extractive distillation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D2011/002—Counter-current extraction
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Extraction Or Liquid Replacement (AREA)
- Treatment Of Liquids With Adsorbents In General (AREA)
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US201361917368P | 2013-12-18 | 2013-12-18 | |
DE102013226428.3A DE102013226428A1 (en) | 2013-12-18 | 2013-12-18 | Extraction column and method of extracting a component from a fluid |
PCT/EP2014/078193 WO2015091628A1 (en) | 2013-12-18 | 2014-12-17 | Extraction column and method for extracting a component from a fluid |
Publications (1)
Publication Number | Publication Date |
---|---|
SG11201604668WA true SG11201604668WA (en) | 2016-07-28 |
Family
ID=53192468
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SG11201604668WA SG11201604668WA (en) | 2013-12-18 | 2014-12-17 | Extraction column and method for extracting a component from a fluid |
Country Status (12)
Country | Link |
---|---|
US (1) | US9643910B2 (en) |
EP (1) | EP3082988B1 (en) |
JP (1) | JP6611721B2 (en) |
KR (1) | KR102300068B1 (en) |
CN (1) | CN106029196B (en) |
BR (1) | BR112016013864B1 (en) |
DE (1) | DE102013226428A1 (en) |
MY (1) | MY177728A (en) |
RU (1) | RU2676072C1 (en) |
SG (1) | SG11201604668WA (en) |
TW (1) | TWI632945B (en) |
WO (1) | WO2015091628A1 (en) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102011117588A1 (en) * | 2011-11-03 | 2013-05-08 | Linde Aktiengesellschaft | Device for producing a phase contact between a liquid and a gaseous phase, in particular a mass transfer column |
WO2015162097A1 (en) | 2014-04-22 | 2015-10-29 | Basf Se | Process for preparing cyclohexane from benzene and methylcyclopentane with upstream benzene hydrogenation |
DE102014108272A1 (en) | 2014-06-12 | 2015-12-17 | Basf Se | Plant and method for carrying out heterogeneously catalyzed gas-phase reactions |
DE102014114193A1 (en) | 2014-09-30 | 2015-08-13 | Basf Se | Process and plant for the recovery of acrylic acid |
KR101777228B1 (en) * | 2016-08-05 | 2017-09-26 | 한전원자력연료 주식회사 | Module type extraction column |
EP3733637A1 (en) | 2020-02-25 | 2020-11-04 | Basf Se | Method for recovering acrylic acid |
CN112451993B (en) * | 2020-11-25 | 2022-02-01 | 中国石油化工股份有限公司 | Spray extraction equipment and solvent extraction method |
Family Cites Families (39)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
IL28565A (en) * | 1967-08-25 | 1971-12-29 | Hydro Chem & Mineral Corp | Apparatus and process for providing direct contact between a liquid and one or more other fluids |
JPS55162307A (en) * | 1979-06-05 | 1980-12-17 | Steiner Ladislav | Liquiddliquid extracting tower |
JPS6235602U (en) * | 1985-04-23 | 1987-03-03 | ||
US4662995A (en) * | 1985-06-25 | 1987-05-05 | Exxon Research And Engineering Company | Distillation process |
DE4328424A1 (en) | 1993-08-24 | 1995-03-02 | Basf Ag | Distillation column for separating a liquid mixture into several pure fractions |
US5758819A (en) | 1996-10-07 | 1998-06-02 | Sniegocki; James | Secured waste container assembly |
DE19838845A1 (en) | 1998-08-26 | 2000-03-02 | Basf Ag | Purification of acrylic acid, used e.g. in polymer production, involves crystallization from mixture with solvent of higher boiling solvent, preferably used as absorbent for gas from catalytic oxidation |
US6498272B1 (en) | 1999-03-06 | 2002-12-24 | Basf Aktiengesellschaft | Method for producing acrylic acid |
DE19924532A1 (en) | 1999-05-28 | 2000-11-30 | Basf Ag | Novel separating column used in fractional condensation of acrylic acid-containing partial oxidation gas mixtures contains both dual-flow- and hydraulically-sealed crossflow-plates |
MY122671A (en) | 1999-03-06 | 2006-04-29 | Basf Ag | Fractional condensation of a product gas mixture containing acrylic acid |
DE19924533A1 (en) | 1999-05-28 | 2000-11-30 | Basf Ag | Fractional condensation of acrylic acid-containing oxidation gas with acrylic acid oligomer drawn off and cracked to give acrylic acid which is fed to the quenching liquid circuit |
DE19947246A1 (en) * | 1999-09-30 | 2001-04-05 | Montz Gmbh Julius | Column partition |
DE10002806A1 (en) * | 2000-01-24 | 2001-07-26 | Basf Ag | Chemical column stripper inlet feed separated by gap from strengthened inlet chamber adjacent to stripper chamber |
AU2001246528A1 (en) | 2000-04-11 | 2001-10-23 | Basf Aktiengesellschaft | Method for the purification of a crude acrylic acid melt |
DE10115277A1 (en) * | 2001-03-28 | 2002-06-13 | Basf Ag | Continuous recovery of (meth)acrylic acid from oxidation reaction gas comprises absorbing in high boiling solvent and rectifying obtained solution at high temperature to reduce product loss as di(meth)acrylic acid |
DE10135585C1 (en) * | 2001-07-20 | 2002-09-12 | Krupp Uhde Gmbh | Process for recovering a pure aromatic fraction containing benzene, toluene and xylenes from refinery streams by extractive distillation, comprises processing solvent and process mixtures |
DE10223058A1 (en) | 2002-05-24 | 2003-12-11 | Basf Ag | Separation of crystals, e.g. (meth)acrylic acid, xylene or N-vinyl pyrrolidone, from suspension in mother liquor comprises addition of the suspension to a wash column having a heated metal wall enveloping a process chamber |
DE10156016A1 (en) | 2001-11-15 | 2003-06-05 | Basf Ag | Device for the cleaning separation of crystals from their suspension in contaminated crystal melt |
JP2004041857A (en) * | 2002-07-09 | 2004-02-12 | Sumitomo Heavy Ind Ltd | Filler |
DE10235847A1 (en) | 2002-08-05 | 2003-08-28 | Basf Ag | A process used to recover acrylic acid obtained in the gas phase oxidation of e.g. propene, involves removal of high-boilers via a side exit in the column to prevent process-stopping polymer formation |
DE10243625A1 (en) | 2002-09-19 | 2004-04-01 | Basf Ag | Hydraulically sealed cross-flow mass transfer tray |
DE10247240A1 (en) | 2002-10-10 | 2004-04-22 | Basf Ag | Process for the production of acrylic acid |
DE10332758A1 (en) | 2003-07-17 | 2004-05-27 | Basf Ag | Thermal separation process for the separation of at least one (meth)acrylic monomer enriched material stream comprises use of a device having separate volume elements and defined residence time |
WO2005007609A1 (en) | 2003-07-11 | 2005-01-27 | Basf Aktiengesellschaft | Thermal separation method for separating at least one (meth)acrylmonomer-enriched material flow |
JP5006507B2 (en) | 2004-01-30 | 2012-08-22 | 株式会社日本触媒 | Acrylic acid production method |
US7169213B2 (en) * | 2004-10-29 | 2007-01-30 | Corning Incorporated | Multi-channel cross-flow porous device |
TWI438187B (en) | 2005-02-28 | 2014-05-21 | Evonik Degussa Gmbh | Acrylic and water-absorbing polymer structures based upon renewable raw materials and process for their preparation |
DE102005015637A1 (en) | 2005-04-05 | 2006-10-12 | Basf Ag | Removing methacrolein from liquid phase (comprising acrylic acid and methacrolein) by crystallization, where acrylic acid is accumulated in crystals formed and methacrolein in remaining mother liquor |
US7601866B2 (en) | 2005-03-01 | 2009-10-13 | Basf Aktiengesellschaft | Process for removing methacrolein from liquid phase comprising acrylic acid as a main constituent and target product, and methacrolein as a secondary component |
FR2884818B1 (en) | 2005-04-25 | 2007-07-13 | Arkema Sa | PROCESS FOR THE PREPARATION OF ACRYLIC ACID FROM GLYCEROL |
DE102007004960A1 (en) | 2007-01-26 | 2008-07-31 | Basf Se | Production of acrylic acid by partial gas phase oxidation, for use e.g. as monomer, includes extracting acrylic acid with organic solvent from acidic stream obtained in purification column |
DE102007055086A1 (en) | 2007-11-16 | 2009-05-20 | Basf Se | Manufacture of acrylic acid involves subjecting precursor to heterogeneously catalyzed gas phase partial oxidation with oxygen in catalyst, reducing gas mixture, and subjecting crude acrylic acid to thermal separation process |
EP2114852B1 (en) | 2007-01-26 | 2015-09-23 | Basf Se | Method for the production of acrylic acid |
CN101589015B (en) * | 2007-01-26 | 2013-11-13 | 巴斯夫欧洲公司 | Method for the production of acrylic acid |
RU2525305C2 (en) * | 2010-08-02 | 2014-08-10 | Александр Михайлович Аниканов | Device for gas-fluid extraction and method of gas-fluid extraction |
DE102011076931A1 (en) * | 2011-06-03 | 2012-12-06 | Basf Se | Aqueous solution containing acrylic acid and its conjugate base |
DE102012204436A1 (en) | 2012-03-20 | 2012-10-04 | Basf Se | Thermal separation between at least a gas ascending- and a liquid containing at least a (meth)acrylic-monomer descending respectively in separating column, accomplished in a separation effective installation containing separating columns |
DE102012204438A1 (en) | 2012-03-20 | 2013-09-26 | Robert Bosch Gmbh | Acceleration sensor with at least one micromechanical sensor element for an occupant protection system in a vehicle |
CN102847341B (en) * | 2012-09-04 | 2014-12-24 | 四川大学 | Wheel disk type liquid-liquid extraction tower |
-
2013
- 2013-12-18 DE DE102013226428.3A patent/DE102013226428A1/en not_active Withdrawn
-
2014
- 2014-12-17 RU RU2016129039A patent/RU2676072C1/en active
- 2014-12-17 SG SG11201604668WA patent/SG11201604668WA/en unknown
- 2014-12-17 JP JP2016541409A patent/JP6611721B2/en active Active
- 2014-12-17 EP EP14821589.0A patent/EP3082988B1/en active Active
- 2014-12-17 US US14/573,313 patent/US9643910B2/en active Active
- 2014-12-17 WO PCT/EP2014/078193 patent/WO2015091628A1/en active Application Filing
- 2014-12-17 BR BR112016013864-3A patent/BR112016013864B1/en active IP Right Grant
- 2014-12-17 KR KR1020167019056A patent/KR102300068B1/en active IP Right Grant
- 2014-12-17 CN CN201480075760.7A patent/CN106029196B/en active Active
- 2014-12-17 MY MYPI2016001090A patent/MY177728A/en unknown
- 2014-12-18 TW TW103144352A patent/TWI632945B/en active
Also Published As
Publication number | Publication date |
---|---|
CN106029196B (en) | 2018-11-13 |
JP2017508600A (en) | 2017-03-30 |
JP6611721B2 (en) | 2019-11-27 |
MY177728A (en) | 2020-09-23 |
KR102300068B1 (en) | 2021-09-09 |
BR112016013864A2 (en) | 2017-08-08 |
DE102013226428A1 (en) | 2015-06-18 |
US9643910B2 (en) | 2017-05-09 |
RU2676072C1 (en) | 2018-12-25 |
EP3082988A1 (en) | 2016-10-26 |
US20150166455A1 (en) | 2015-06-18 |
BR112016013864B1 (en) | 2021-11-30 |
EP3082988B1 (en) | 2019-03-27 |
WO2015091628A1 (en) | 2015-06-25 |
TW201538221A (en) | 2015-10-16 |
KR20160098442A (en) | 2016-08-18 |
CN106029196A (en) | 2016-10-12 |
TWI632945B (en) | 2018-08-21 |
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