ES8701704A1 - Un proceso para la recuperacion de glicerina de una corrien-te de alimentacion acuosa salina que contiene glicerina - Google Patents
Un proceso para la recuperacion de glicerina de una corrien-te de alimentacion acuosa salina que contiene glicerinaInfo
- Publication number
- ES8701704A1 ES8701704A1 ES549714A ES549714A ES8701704A1 ES 8701704 A1 ES8701704 A1 ES 8701704A1 ES 549714 A ES549714 A ES 549714A ES 549714 A ES549714 A ES 549714A ES 8701704 A1 ES8701704 A1 ES 8701704A1
- Authority
- ES
- Spain
- Prior art keywords
- glycerine
- recovery
- pentanol
- saline waters
- flashing
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/74—Separation; Purification; Use of additives, e.g. for stabilisation
- C07C29/76—Separation; Purification; Use of additives, e.g. for stabilisation by physical treatment
- C07C29/80—Separation; Purification; Use of additives, e.g. for stabilisation by physical treatment by distillation
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
- Detergent Compositions (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
METODO DE RECUPERACION DE GLICERINA DE CORRIENTES DE ALIMENTACION ACUOSAS SALINAS. COMPRENDE LA EVAPORACION DE AL MENOS EL 90% DEL AGUA EXISTENTE EN LA CORRIENTE DE ALIMENTACION; PONER EN CONTACTO LA CORRIENTE CONCENTRADA RESULTANTE CON 1-PENTANOL O UNA MEZCLA DE PENTANOLES, EN UNA PROPORCION DE 1:1 A 5:1 DE PENTANOL A ALIMENTACION, A UNA TEMPERATURA COMPRENDIDA ENTRE 115JC Y 160JC; SEPARACION DE LA FASE LIQUIDA DE LA SAL PRECIPITADA; EVAPORACION DE LA FASE LIQUIDA CON FORMACION DE UNA FRACCION SUPERIOR Y OTRA INFERIOR; Y DESTILACION FRACCIONADA DE LA FRACCION INFERIOR PARA OBTENER GLICERINA. AL MENOS UNA PARTE DE LA FRACCION SUPERIOR SE SOMETE A UN PROCESO DE ELIMINACION DE AGUA Y SE RECICLA A LA ETAPA DE CONTACTO DE LA CORRIENTE CON PENTANOL. TIENE APLICACIONES PARA LA RECUPERACION DE GLICERINA DE AGUAS DE DESECHO RESULTANTES DE LA FABRICACION DE RESINAS EPOXIDICAS.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US06/679,773 US4560812A (en) | 1984-12-10 | 1984-12-10 | Recovery of glycerine from saline waters |
Publications (2)
Publication Number | Publication Date |
---|---|
ES8701704A1 true ES8701704A1 (es) | 1986-12-01 |
ES549714A0 ES549714A0 (es) | 1986-12-01 |
Family
ID=24728310
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ES549714A Expired ES8701704A1 (es) | 1984-12-10 | 1985-12-09 | Un proceso para la recuperacion de glicerina de una corrien-te de alimentacion acuosa salina que contiene glicerina |
Country Status (9)
Country | Link |
---|---|
US (1) | US4560812A (es) |
EP (1) | EP0184880B1 (es) |
JP (1) | JPS61140532A (es) |
CN (1) | CN1004695B (es) |
AT (1) | ATE37020T1 (es) |
CA (1) | CA1248971A (es) |
DE (1) | DE3564801D1 (es) |
ES (1) | ES8701704A1 (es) |
ZA (1) | ZA859394B (es) |
Families Citing this family (38)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4784673A (en) * | 1987-07-17 | 1988-11-15 | Shell Oil Company | Desiccant composition for supercritical CO2 |
US5190622A (en) * | 1991-11-14 | 1993-03-02 | Lloyd Berg | Recovery of glycerine from sorbitol by azeotropic distillation |
US5198077A (en) * | 1991-11-19 | 1993-03-30 | Lloyd Berg | Recovery of glycerine from mannitol, lactose or lactitol by azeotropic distillation |
US5286882A (en) * | 1992-10-13 | 1994-02-15 | Shell Oil Company | Polyethercyclicpolyols from epihalohydrins, polyhydric alcohols and metal hydroxides or epoxy alcohol and optionally polyhydric alcohols with addition of epoxy resins |
US5436227A (en) * | 1993-05-27 | 1995-07-25 | Shell Oil Company | Soluble/insoluble alcohol in drilling fluid |
US5361841A (en) * | 1993-05-27 | 1994-11-08 | Shell Oil Company | Drilling and cementing with blast furnace slag/polyalcohol fluid |
US5361842A (en) * | 1993-05-27 | 1994-11-08 | Shell Oil Company | Drilling and cementing with blast furnace slag/silicate fluid |
US5358044A (en) * | 1993-05-27 | 1994-10-25 | Shell Oil Company | Drilling and cementing with blast furnace slag/soluble/insoluble alcohol |
US5439056A (en) * | 1993-06-28 | 1995-08-08 | Shell Oil Company | Coal slag solidification of drilling fluid |
US5363918A (en) * | 1993-08-04 | 1994-11-15 | Shell Oil Company | Wellbore sealing with unsaturated monomer system |
JP3712903B2 (ja) | 2000-01-28 | 2005-11-02 | 花王株式会社 | グリセリンの製造方法 |
CA2598667C (en) | 2003-11-20 | 2012-04-03 | Solvay (Societe Anonyme) | Process for producing a chlorinated organic compound |
US7235183B2 (en) * | 2004-06-22 | 2007-06-26 | Crown Iron Works Company | Glycerine foots salt separation system |
EP2275417A3 (en) * | 2005-05-20 | 2011-03-09 | SOLVAY (Société Anonyme) | Process for producing dichloropropanol |
KR20080019005A (ko) | 2005-05-20 | 2008-02-29 | 솔베이(소시에떼아노님) | 폴리히드록실화 지방족 탄화수소에서 출발하여클로로히드린을 제조하는 방법 |
CN100347104C (zh) * | 2005-12-05 | 2007-11-07 | 江苏三木集团有限公司 | 环氧树脂含盐废水的处理及盐的回收方法 |
FR2913684B1 (fr) * | 2007-03-14 | 2012-09-14 | Solvay | Procede de fabrication de dichloropropanol |
TW200911773A (en) | 2007-06-12 | 2009-03-16 | Solvay | Epichlorohydrin, manufacturing process and use |
FR2918058A1 (fr) * | 2007-06-28 | 2009-01-02 | Solvay | Produit a base de glycerol, procede pour sa purification et son utilisation dans la fabrication de dichloropropanol |
JP2011502032A (ja) | 2007-10-02 | 2011-01-20 | ソルヴェイ(ソシエテ アノニム) | 容器の耐腐食性を向上させるためのケイ素を含有する組成物の使用 |
TWI478875B (zh) | 2008-01-31 | 2015-04-01 | Solvay | 使水性組成物中之有機物質降解之方法 |
US8084651B2 (en) * | 2008-03-10 | 2011-12-27 | Tate & Lyle Ingredients Americas Llc | Process for purification of glycerol |
CA2718315A1 (en) * | 2008-04-03 | 2009-10-08 | Solvay (Societe Anonyme) | Composition comprising glycerol, process for obtaining same and use thereof in the manufacture of dichloropropanol |
FR2935968B1 (fr) * | 2008-09-12 | 2010-09-10 | Solvay | Procede pour la purification de chlorure d'hydrogene |
US9662594B2 (en) * | 2009-06-22 | 2017-05-30 | Ng Innovations, Inc. | Systems and methods for treating fractionated water |
US8409442B2 (en) * | 2009-08-20 | 2013-04-02 | Ng Innovations, Inc. | Water separation method and apparatus |
US8470139B2 (en) * | 2009-12-11 | 2013-06-25 | Nginnovations, Inc. | Systems and method for low temperature recovery of fractionated water |
FR2964657B1 (fr) * | 2010-09-15 | 2013-01-18 | Rhodia Operations | Procede de purification du glycerol brut |
CN103261181A (zh) | 2010-09-30 | 2013-08-21 | 索尔维公司 | 天然来源的环氧氯丙烷的衍生物 |
CN102557164B (zh) * | 2010-12-15 | 2013-12-11 | 益海嘉里(连云港)化工有限公司 | 一种含甘油的高盐工业废水的回收利用方法 |
CN102503014B (zh) * | 2011-11-22 | 2013-06-05 | 浙江大学 | 一种含盐甘油废水的处理方法 |
JP2016529259A (ja) * | 2013-08-19 | 2016-09-23 | アールイージー ライフ サイエンシズ リミテッド ライアビリティ カンパニー | 部分精製された廃グリセロールの製造 |
US9469586B2 (en) | 2013-08-19 | 2016-10-18 | REG Life Sciences, LLC | Production of partially refined waste glycerol |
PT108590A (pt) * | 2015-06-29 | 2016-12-29 | Univ Aveiro | Processo de purificação de crude glicerol |
CN106397124B (zh) * | 2016-09-13 | 2019-05-28 | 西南石油大学 | 一种含盐乙二醇溶液的除盐方法 |
CN106542965B (zh) * | 2016-11-07 | 2019-07-16 | 青岛科技大学 | 低碳混合醇塔釜闪蒸分离甲醇的方法 |
TWI636967B (zh) | 2017-06-30 | 2018-10-01 | 國立清華大學 | 含鹽甘油廢水處理系統與方法 |
CN110229046B (zh) * | 2018-03-05 | 2023-07-28 | 南通星辰合成材料有限公司 | 一种从环氧废水蒸发母液中提取甘油及类甘油醇的装置及方法 |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1078580A (en) * | 1912-09-07 | 1913-11-11 | Gaston Philippe Guignard | Process of extracting glycerin from vinasses. |
US2444296A (en) * | 1943-04-24 | 1948-06-29 | Colgate Palmolive Pect Company | Recovery of glycerol |
US2436209A (en) * | 1943-09-18 | 1948-02-17 | Colgate Palmolive Peet Co | Extraction of polyhydric alcohols |
US2479041A (en) * | 1943-09-18 | 1949-08-16 | Colgate Palmolive Peet Co | Glycerine extraction process |
US3483264A (en) * | 1966-07-08 | 1969-12-09 | Union Starch & Refining Co Inc | Purification of polyhydric alcohols |
JPS51136607A (en) * | 1975-05-22 | 1976-11-26 | Kao Corp | Process for purification of aqueous glycerine solution |
US4164507A (en) * | 1978-07-13 | 1979-08-14 | Shell Oil Company | Process for separation of salt from heavy ends wastes of glycerine manufacture |
-
1984
- 1984-12-10 US US06/679,773 patent/US4560812A/en not_active Expired - Fee Related
-
1985
- 1985-11-20 EP EP85201923A patent/EP0184880B1/en not_active Expired
- 1985-11-20 DE DE8585201923T patent/DE3564801D1/de not_active Expired
- 1985-11-20 AT AT85201923T patent/ATE37020T1/de not_active IP Right Cessation
- 1985-11-21 CA CA000495851A patent/CA1248971A/en not_active Expired
- 1985-12-07 CN CN85109000.1A patent/CN1004695B/zh not_active Expired
- 1985-12-09 ES ES549714A patent/ES8701704A1/es not_active Expired
- 1985-12-09 ZA ZA859394A patent/ZA859394B/xx unknown
- 1985-12-09 JP JP60276656A patent/JPS61140532A/ja active Granted
Also Published As
Publication number | Publication date |
---|---|
ATE37020T1 (de) | 1988-09-15 |
JPH0558610B2 (es) | 1993-08-27 |
CA1248971A (en) | 1989-01-17 |
ZA859394B (en) | 1986-08-27 |
EP0184880A1 (en) | 1986-06-18 |
CN85109000A (zh) | 1986-07-09 |
US4560812A (en) | 1985-12-24 |
DE3564801D1 (en) | 1988-10-13 |
JPS61140532A (ja) | 1986-06-27 |
EP0184880B1 (en) | 1988-09-07 |
ES549714A0 (es) | 1986-12-01 |
CN1004695B (zh) | 1989-07-05 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
FD1A | Patent lapsed |
Effective date: 19970303 |