ES2077046T3 - Procedimiento continuo y dispositivo de separacion cromatografica de una mezcla de al menos tres constituyentes en tres efluentes purificados por medio de un solo disolvente a dos temperaturas y/o a dos presiones diferentes. - Google Patents
Procedimiento continuo y dispositivo de separacion cromatografica de una mezcla de al menos tres constituyentes en tres efluentes purificados por medio de un solo disolvente a dos temperaturas y/o a dos presiones diferentes.Info
- Publication number
- ES2077046T3 ES2077046T3 ES90402335T ES90402335T ES2077046T3 ES 2077046 T3 ES2077046 T3 ES 2077046T3 ES 90402335 T ES90402335 T ES 90402335T ES 90402335 T ES90402335 T ES 90402335T ES 2077046 T3 ES2077046 T3 ES 2077046T3
- Authority
- ES
- Spain
- Prior art keywords
- solvent
- mixture
- strong
- constituents
- extract
- Prior art date
- Legal status (The legal status 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 status listed.)
- Expired - Lifetime
Links
- 239000002904 solvent Substances 0.000 title abstract 11
- 238000000034 method Methods 0.000 title abstract 3
- 239000000203 mixture Substances 0.000 title abstract 3
- 239000000470 constituent Substances 0.000 title abstract 2
- 238000013375 chromatographic separation Methods 0.000 title 1
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 abstract 3
- 238000000926 separation method Methods 0.000 abstract 3
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 abstract 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 abstract 1
- 230000002745 absorbent Effects 0.000 abstract 1
- 239000002250 absorbent Substances 0.000 abstract 1
- 239000012530 fluid Substances 0.000 abstract 1
- 239000008103 glucose Substances 0.000 abstract 1
- IWDCLRJOBJJRNH-UHFFFAOYSA-N p-cresol Chemical compound CC1=CC=C(O)C=C1 IWDCLRJOBJJRNH-UHFFFAOYSA-N 0.000 abstract 1
- 238000000746 purification Methods 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D15/00—Separating processes involving the treatment of liquids with solid sorbents; Apparatus therefor
- B01D15/02—Separating processes involving the treatment of liquids with solid sorbents; Apparatus therefor with moving adsorbents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D15/00—Separating processes involving the treatment of liquids with solid sorbents; Apparatus therefor
- B01D15/08—Selective adsorption, e.g. chromatography
- B01D15/10—Selective adsorption, e.g. chromatography characterised by constructional or operational features
- B01D15/18—Selective adsorption, e.g. chromatography characterised by constructional or operational features relating to flow patterns
- B01D15/1814—Recycling of the fraction to be distributed
- B01D15/1821—Simulated moving beds
- B01D15/1828—Simulated moving beds characterised by process features
- B01D15/1835—Flushing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D15/00—Separating processes involving the treatment of liquids with solid sorbents; Apparatus therefor
- B01D15/08—Selective adsorption, e.g. chromatography
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D15/00—Separating processes involving the treatment of liquids with solid sorbents; Apparatus therefor
- B01D15/08—Selective adsorption, e.g. chromatography
- B01D15/10—Selective adsorption, e.g. chromatography characterised by constructional or operational features
- B01D15/18—Selective adsorption, e.g. chromatography characterised by constructional or operational features relating to flow patterns
- B01D15/1814—Recycling of the fraction to be distributed
- B01D15/1821—Simulated moving beds
- B01D15/1842—Simulated moving beds characterised by apparatus features
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D15/00—Separating processes involving the treatment of liquids with solid sorbents; Apparatus therefor
- B01D15/08—Selective adsorption, e.g. chromatography
- B01D15/10—Selective adsorption, e.g. chromatography characterised by constructional or operational features
- B01D15/18—Selective adsorption, e.g. chromatography characterised by constructional or operational features relating to flow patterns
- B01D15/1814—Recycling of the fraction to be distributed
- B01D15/1821—Simulated moving beds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D15/00—Separating processes involving the treatment of liquids with solid sorbents; Apparatus therefor
- B01D15/08—Selective adsorption, e.g. chromatography
- B01D15/26—Selective adsorption, e.g. chromatography characterised by the separation mechanism
- B01D15/40—Selective adsorption, e.g. chromatography characterised by the separation mechanism using supercritical fluid as mobile phase or eluent
Landscapes
- Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Treatment Of Liquids With Adsorbents In General (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
SE DESCRIBE UN DISPOSITIVO Y UN PROCEDIMIENTO DE SEPARACION EN CONTINUO Y EN FASE FLUIDA DE UNA MEZCLA DE POR LO MENOS TRES CONSTITUYENTES EN TRES FRACCIONES. SE UTILIZA UNA TECNICA EN CONTRACORRIENTE SIMULADA EN UNA COLUMNA DE SEPARACION LLENA DE UN ABSORBENTE QUE TIENE CINCO ZONAS 6, 5, 4, 3 Y 2 CON DIFERENTES FUNCIONES Y SE REALIZA LA SECUENCIA DE ETAPAS SIGUIENTES: SE INTRODUCE DISOLVENTE FUERTE S2, SE EXTRAE UN EXTRACTO E2 EN EL DISOLVENTE FUERTE, SE INTRODUCE EL MISMO DISOLVENTE PERO A UNA TEMPERATURA Y/O A UNA PRESION MAS DEBIL (DISOLVENTE S1 DEBIL), SE SACA EXTRACTO EN EL DISOLVENTE DEBIL E1, SE INTRODUCE LA MEZCLA A SEPARAR, SE EXTRAE REFINADO EN EL DISOLVENTE DEBIL R, SE RECICLA UNA CORRIENTE RCY ALTERNATIVAMENTE HACIA LA ALIMENTACION DEL DISOLVENTE FUERTE S2 Y DESPUES HACIA LA ALIMENTACION DEL DISOLVENTE DEBIL S1. SE ENVIA UNA CORRIENTE PROCEDENTE DE LA ZONA 6 ALTERNATIVAMENTE HACIA UNA SALIDA DE EXTRACTO EN EL DISOLVENTE FUERTE S2, Y DESPUES HACIA LA ENTRADA DE LA ZONA CINCO. SEHACEN AVANZAR PERIODICAMENTE DE MODO SINCRONO A TRAVES DE LA COLUMNA LAS DIVERSAS ALIMENTACIONES Y SALIDAS. APLICACION ESPECIALMENTE A LA SEPARACION DE GLUCOSA, XILOSA Y ARABINOSA Y A LA DEPURACION DE AGUA QUE CONTIENE FENOL, P-CRESOL Y TOLUENO.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR8911365A FR2651149B1 (fr) | 1989-08-28 | 1989-08-28 | Procede continu et dispositif de separation chromatographique d'un melange d'au moins trois constituants en trois effluents purifies au moyen d'un seul solvant a deux temperatures et/ou a deux pressions differentes. |
Publications (1)
Publication Number | Publication Date |
---|---|
ES2077046T3 true ES2077046T3 (es) | 1995-11-16 |
Family
ID=9384987
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ES90402335T Expired - Lifetime ES2077046T3 (es) | 1989-08-28 | 1990-08-22 | Procedimiento continuo y dispositivo de separacion cromatografica de una mezcla de al menos tres constituyentes en tres efluentes purificados por medio de un solo disolvente a dos temperaturas y/o a dos presiones diferentes. |
Country Status (8)
Country | Link |
---|---|
US (1) | US5114590A (es) |
EP (1) | EP0415822B1 (es) |
JP (1) | JP2964348B2 (es) |
KR (1) | KR0155553B1 (es) |
DE (1) | DE69020825T2 (es) |
ES (1) | ES2077046T3 (es) |
FR (1) | FR2651149B1 (es) |
MY (1) | MY106861A (es) |
Families Citing this family (53)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2962594B2 (ja) * | 1991-06-12 | 1999-10-12 | オルガノ株式会社 | 複数成分の分離方法 |
FR2704158B3 (fr) * | 1993-04-21 | 1995-06-16 | Inst Francais Du Petrole | Procédé et dispositif de fractionnement d'un mélange en lit mobile simulé en présence d'un gaz comprimé. |
FR2690630B1 (fr) * | 1992-04-29 | 1994-07-22 | Separex Sa | Procede et dispositif de fractionnement de melanges de composants par voie chromatographique a l'aide d'un eluant a pression supercritique. |
WO1993022022A1 (fr) * | 1992-04-29 | 1993-11-11 | Institut Français Du Petrole | Procede et dispositif de fractionnement d'un melange en lit mobile simule en presence d'un gaz comprime, d'un fluide supercritique ou d'un liquide subcritique |
FR2694208B1 (fr) * | 1992-07-30 | 1994-09-23 | Separex Sa | Procédé et dispositif industriels de fractionnement de mélanges de composants par chromatographie. |
US5770088A (en) * | 1992-06-30 | 1998-06-23 | Daicel Chemical Industries, Ltd. | Simulated moving bed chromatographic separation process |
JP3070890B2 (ja) * | 1993-02-12 | 2000-07-31 | オルガノ株式会社 | 澱粉糖の製造方法 |
JPH08512336A (ja) * | 1993-04-29 | 1996-12-24 | ノルスク・ヒドロ・アクシェセルスカープ | 脂肪酸およびその誘導体のクロマトグラフィーによる分画方法 |
US5387347A (en) * | 1993-09-15 | 1995-02-07 | Rothchild; Ronald D. | Method and apparatus for continuous chromatographic separation |
FR2719233B1 (fr) * | 1994-04-28 | 1996-07-19 | Inst Francais Du Petrole | Procédé de séparation en lit mobile simulé à débit de recyclage constant. |
EP0687491A1 (en) * | 1994-06-16 | 1995-12-20 | Daicel Chemical Industries, Ltd. | Simulated moving bed chromatographic separation process |
FR2721529B1 (fr) * | 1994-06-22 | 1996-09-06 | Inst Francais Du Petrole | Procédé de séparation par chromatographie en lit mobile simulé avec correction de volume mort par diminution de longueur. |
FR2721527B1 (fr) * | 1994-06-22 | 1996-09-06 | Inst Francais Du Petrole | Procédé de séparation par chromatographie en lit mobile simulé avec correction de volume mort par augmentation de débit. |
FR2721528B1 (fr) * | 1994-06-22 | 1996-09-06 | Inst Francais Du Petrole | Procédé de séparation par chromatographie en lit mobile simulé avec correction de volume mort par desynchronisation des périodes. |
US5635072A (en) * | 1995-01-31 | 1997-06-03 | Uop | Simulated moving bed adsorptive separation process |
US5630943A (en) * | 1995-11-30 | 1997-05-20 | Merck Patent Gesellschaft Mit Beschrankter Haftung | Discontinuous countercurrent chromatographic process and apparatus |
FR2743002B1 (fr) * | 1995-12-27 | 1998-01-30 | Inst Francais Du Petrole | Procede de regulation d'au moins un debit de fluide circulant dans une boucle de separation chromatographique en lit mobile simule |
FR2751888B1 (fr) * | 1996-07-31 | 1998-09-11 | Inst Francais Du Petrole | Dispositif et procede de rincage en lit mobile simule comportant au moins deux lignes de distribution de fluides |
US6063284A (en) * | 1997-05-15 | 2000-05-16 | Em Industries, Inc. | Single column closed-loop recycling with periodic intra-profile injection |
FR2779067B1 (fr) * | 1998-05-29 | 2000-08-18 | Inst Francais Du Petrole | Dispositif de regulation de debit d'au moins un fluide d'unites de separation par lit mobile simule |
US6036865A (en) * | 1998-06-15 | 2000-03-14 | Union Carbide Chemicals & Plastics Technology Corporation | Separation processes |
US6045703A (en) * | 1998-06-15 | 2000-04-04 | Union Carbide Chemicals & Plastics Technology Corporation | Separation processes |
FR2783021B1 (fr) | 1998-09-09 | 2000-10-13 | Inst Francais Du Petrole | Procede et systeme de pompage de fluide utilisant une pompe avec un debit constant a l'aspiration ou au refoulement |
FR2810897B1 (fr) | 2000-06-28 | 2002-10-11 | Novasep | Procede et dispositif de separation en lit mobile simule d'au moins un constituant dans des colonnes ayant un rapport longueur sur diametre approprie |
EP1352235B1 (en) * | 2000-11-21 | 2013-05-08 | Waters Technologies Corporation | Mobile phase dilution scheme for enhanced chromatography |
SE0202188D0 (sv) | 2002-07-11 | 2002-07-11 | Pronova Biocare As | A process for decreasing environmental pollutants in an oil or a fat, a volatile fat or oil environmental pollutants decreasing working fluid, a health supplement, and an animal feed product |
EP2295529B2 (en) | 2002-07-11 | 2022-05-18 | Basf As | Use of a volatile environmental pollutants-decreasing working fluid for decreasing the amount of pollutants in a fat for alimentary or cosmetic use |
FR2856313B1 (fr) * | 2003-06-17 | 2005-07-29 | Inst Francais Du Petrole | Methode de gestion des vannes d'un systeme de separation a lit mobile simule |
US6872314B2 (en) * | 2003-08-29 | 2005-03-29 | Eastman Chemical Company | Dewatering process |
JP5600688B2 (ja) * | 2009-01-06 | 2014-10-01 | クロマコン アーゲー | 多画分精製方法及びそのような方法のための装置 |
JP5872483B2 (ja) | 2009-12-30 | 2016-03-01 | ビーエイエスエフ ファーマ(コーラニッシュ)リミテッド | 擬似移動床式クロマトグラフ分離方法 |
PT3401410T (pt) | 2010-06-26 | 2021-04-05 | Virdia Llc | Métodos para produção de misturas de açúcar |
WO2012137201A1 (en) | 2011-04-07 | 2012-10-11 | Hcl Cleantech Ltd. | Lignocellulose conversion processes and products |
GB201111601D0 (en) | 2011-07-06 | 2011-08-24 | Equateq Ltd | New process |
GB201111595D0 (en) | 2011-07-06 | 2011-08-24 | Equateq Ltd | Improved process |
GB201111589D0 (en) | 2011-07-06 | 2011-08-24 | Equateq Ltd | New modified process |
GB201111591D0 (en) | 2011-07-06 | 2011-08-24 | Equateq Ltd | Further new process |
GB201111594D0 (en) | 2011-07-06 | 2011-08-24 | Equateq Ltd | New improved process |
WO2013055932A1 (en) * | 2011-10-11 | 2013-04-18 | Georgia Tech Research Corporation | Methods and controllers for simulated moving bed chromatography for multicomponent separation |
GB201300354D0 (en) | 2013-01-09 | 2013-02-20 | Basf Pharma Callanish Ltd | Multi-step separation process |
US9428711B2 (en) | 2013-05-07 | 2016-08-30 | Groupe Novasep | Chromatographic process for the production of highly purified polyunsaturated fatty acids |
US8802880B1 (en) | 2013-05-07 | 2014-08-12 | Group Novasep | Chromatographic process for the production of highly purified polyunsaturated fatty acids |
EP2883860B1 (fr) | 2013-12-11 | 2016-08-24 | Novasep Process | Procédé chromatographique de production d'acides gras polyinsaturés |
EP3092218B1 (fr) | 2014-01-07 | 2022-03-09 | Novasep Process Solutions | Procédé de purification d'acides aminés aromatiques |
WO2016036757A1 (en) | 2014-09-02 | 2016-03-10 | INVISTA Technologies S.á.r.l. | Purification of long chain diacids |
WO2016053484A1 (en) | 2014-09-30 | 2016-04-07 | Exxonmobil Chemical Patents Inc. | Adsorptive separation of multi-component fluid mixtures |
EP3280697A1 (en) | 2015-04-08 | 2018-02-14 | INVISTA Textiles (U.K.) Limited | Materials and methods for the selective recovery of monovalent products from aqueous solutions using continuous ion exchange |
US10265642B2 (en) | 2015-04-10 | 2019-04-23 | Invista North America S.A.R.L. | Process for separation of diamines and/or omega-aminoacids from a feed fixture |
US12090420B2 (en) | 2018-09-18 | 2024-09-17 | Inv Nylon Chemicals Americas, Llc | Systems and methods for recovering amines and their derivatives from aqueous mixtures |
CN113567581B (zh) * | 2021-07-19 | 2024-01-05 | 湖北科林博伦新材料有限公司 | 采用高效液相色谱法分析碱水中邻甲酚钠含量的方法 |
US20250050241A1 (en) | 2021-12-17 | 2025-02-13 | Basf Se | Chromatographic separation process for efficient purification of polyunsaturated fatty acids |
US11548864B1 (en) | 2022-06-15 | 2023-01-10 | Zaiput Flow Technologies LLC | Separation of chemical species using multiple liquid phases and related systems |
US12187695B2 (en) | 2022-06-15 | 2025-01-07 | Zaiput Flow Technologies LLC | Separation of chemical species using multiple liquid phases and related systems |
Family Cites Families (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2985589A (en) * | 1957-05-22 | 1961-05-23 | Universal Oil Prod Co | Continuous sorption process employing fixed bed of sorbent and moving inlets and outlets |
GB1326765A (en) * | 1969-10-02 | 1973-08-15 | Magyar Asvanyolaj Es Foeldgaz | Continuous separation of fluid mixtures on a fixed bed of solids |
US3761533A (en) * | 1970-07-23 | 1973-09-25 | Toray Industries | Separation process of components of feed mixture utilizing solid sorbent |
US3706812A (en) * | 1970-12-07 | 1972-12-19 | Universal Oil Prod Co | Fluid-solid contacting apparatus |
US3696107A (en) * | 1971-05-27 | 1972-10-03 | Richard W Neuzil | Improved hydrocarbon separation process |
GB1488616A (en) * | 1974-04-01 | 1977-10-12 | Exxon Research Engineering Co | Dual desorbent composition and temperature separation processes |
US4029717A (en) * | 1974-04-01 | 1977-06-14 | Exxon Research And Engineering Company | Simulated moving bed adsorption-desorption process for paraxylene recovery |
US4031156A (en) * | 1975-03-07 | 1977-06-21 | Exxon Research And Engineering Company | Separation and recovery of ethylbenzene by dual desorbent composition and temperature separation processes |
JPS6055162B2 (ja) * | 1977-05-26 | 1985-12-04 | 参松工業株式会社 | カラムクロマト分離法 |
US4306107A (en) * | 1980-02-07 | 1981-12-15 | Uop Inc. | Production of pure M-xylene and pure ethyl benzene from a mixture of C8 aromatic isomers |
US4402832A (en) * | 1982-08-12 | 1983-09-06 | Uop Inc. | High efficiency continuous separation process |
US4498991A (en) * | 1984-06-18 | 1985-02-12 | Uop Inc. | Serial flow continuous separation process |
EP0290684A1 (en) * | 1987-05-08 | 1988-11-17 | Uop Inc. | Process for separating arabinose |
US4664718A (en) * | 1985-03-18 | 1987-05-12 | Uop Inc. | Process for separating arabinose from a pentose/hexose mixture |
US4724081A (en) * | 1986-04-28 | 1988-02-09 | Soken Kagaku Kabushiki Kaisha | Process and apparatus for separation by liquid chromatography |
JPH0669521B2 (ja) * | 1986-12-23 | 1994-09-07 | 三菱化成エンジニアリング株式会社 | クロマト分離法 |
US4990259A (en) * | 1988-12-16 | 1991-02-05 | The Amalgamated Sugar Company | Chromatographic separator sorbent bed preparation |
-
1989
- 1989-08-28 FR FR8911365A patent/FR2651149B1/fr not_active Expired - Lifetime
-
1990
- 1990-08-22 DE DE69020825T patent/DE69020825T2/de not_active Expired - Lifetime
- 1990-08-22 ES ES90402335T patent/ES2077046T3/es not_active Expired - Lifetime
- 1990-08-22 EP EP90402335A patent/EP0415822B1/fr not_active Expired - Lifetime
- 1990-08-28 KR KR1019900013499A patent/KR0155553B1/ko not_active IP Right Cessation
- 1990-08-28 JP JP2227857A patent/JP2964348B2/ja not_active Expired - Lifetime
- 1990-08-28 US US07/573,564 patent/US5114590A/en not_active Expired - Lifetime
- 1990-08-28 MY MYPI90001466A patent/MY106861A/en unknown
Also Published As
Publication number | Publication date |
---|---|
FR2651149A1 (fr) | 1991-03-01 |
KR0155553B1 (ko) | 1998-11-16 |
JP2964348B2 (ja) | 1999-10-18 |
DE69020825T2 (de) | 1996-03-28 |
US5114590A (en) | 1992-05-19 |
JPH03207403A (ja) | 1991-09-10 |
EP0415822A1 (fr) | 1991-03-06 |
DE69020825D1 (de) | 1995-08-17 |
KR910004231A (ko) | 1991-03-28 |
FR2651149B1 (fr) | 1992-06-05 |
EP0415822B1 (fr) | 1995-07-12 |
MY106861A (en) | 1995-08-30 |
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