BR112022003587A2 - Processo e sistema para a produção de carbonato de etileno e/ou etileno glicol - Google Patents
Processo e sistema para a produção de carbonato de etileno e/ou etileno glicolInfo
- Publication number
- BR112022003587A2 BR112022003587A2 BR112022003587A BR112022003587A BR112022003587A2 BR 112022003587 A2 BR112022003587 A2 BR 112022003587A2 BR 112022003587 A BR112022003587 A BR 112022003587A BR 112022003587 A BR112022003587 A BR 112022003587A BR 112022003587 A2 BR112022003587 A2 BR 112022003587A2
- Authority
- BR
- Brazil
- Prior art keywords
- stream
- aqueous
- ethylene glycol
- distillation apparatus
- ethylene carbonate
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D317/00—Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms
- C07D317/08—Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms having the hetero atoms in positions 1 and 3
- C07D317/10—Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms having the hetero atoms in positions 1 and 3 not condensed with other rings
- C07D317/32—Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms having the hetero atoms in positions 1 and 3 not condensed with other rings with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
- C07D317/34—Oxygen atoms
- C07D317/36—Alkylene carbonates; Substituted alkylene carbonates
- C07D317/38—Ethylene carbonate
-
- 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
- B01D3/148—Fractional distillation or use of a fractionation or rectification column by two or more of a fractionation, separation or rectification step in combination with at least one evaporator
-
- 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
- B01D3/42—Regulation; Control
- B01D3/4205—Reflux ratio control splitter
-
- 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
- C07C29/09—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by hydrolysis
- C07C29/10—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by hydrolysis of ethers, including cyclic ethers, e.g. oxiranes
- C07C29/103—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by hydrolysis of ethers, including cyclic ethers, e.g. oxiranes of cyclic ethers
- C07C29/106—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by hydrolysis of ethers, including cyclic ethers, e.g. oxiranes of cyclic ethers of oxiranes
-
- 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
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C31/00—Saturated compounds having hydroxy or O-metal groups bound to acyclic carbon atoms
- C07C31/18—Polyhydroxylic acyclic alcohols
- C07C31/20—Dihydroxylic alcohols
- C07C31/202—Ethylene glycol
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C317/00—Sulfones; Sulfoxides
- C07C317/26—Sulfones; Sulfoxides having sulfone or sulfoxide groups and nitrogen atoms, not being part of nitro or nitroso groups, bound to the same carbon skeleton
- C07C317/32—Sulfones; Sulfoxides having sulfone or sulfoxide groups and nitrogen atoms, not being part of nitro or nitroso groups, bound to the same carbon skeleton with sulfone or sulfoxide groups bound to carbon atoms of six-membered aromatic rings of the carbon skeleton
- C07C317/34—Sulfones; Sulfoxides having sulfone or sulfoxide groups and nitrogen atoms, not being part of nitro or nitroso groups, bound to the same carbon skeleton with sulfone or sulfoxide groups bound to carbon atoms of six-membered aromatic rings of the carbon skeleton having sulfone or sulfoxide groups and amino groups bound to carbon atoms of six-membered aromatic rings being part of the same non-condensed ring or of a condensed ring system containing that ring
- C07C317/38—Sulfones; Sulfoxides having sulfone or sulfoxide groups and nitrogen atoms, not being part of nitro or nitroso groups, bound to the same carbon skeleton with sulfone or sulfoxide groups bound to carbon atoms of six-membered aromatic rings of the carbon skeleton having sulfone or sulfoxide groups and amino groups bound to carbon atoms of six-membered aromatic rings being part of the same non-condensed ring or of a condensed ring system containing that ring with the nitrogen atom of at least one amino group being part of any of the groups, X being a hetero atom, Y being any atom, e.g. N-acylaminosulfones
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Epoxy Compounds (AREA)
Abstract
processo e sistema para a produção de carbonato de etileno e/ou etileno glicol. a invenção se refere a um processo para produzir carbonato de etileno e/ou etileno glicol, que compreende as seguintes etapas: a) fornecer uma corrente de absorvedor aérea retirada de um absorvedor para um separador vapor-líquido para produzir uma corrente de fundo aquosa e uma corrente de gás de reciclo; b) fornecer uma corrente de processo aquosa compreendendo uma ou mais impurezas a um aparelho de destilação para produzir uma corrente de impurezas aérea e uma corrente de processo aquosa purificada, em que a corrente de processo aquosa fornecida ao aparelho de destilação compreende pelo menos uma porção da corrente de fundo aquosa retirada do separador vapor-líquido, em que a corrente de impurezas aérea é fornecida a um condensador e é resfriada até uma temperatura na faixa de 5 a 95°c, em que a corrente de impurezas aérea resfriada é dividida em uma corrente de refluxo que é reciclada para o aparelho de destilação e uma corrente de impurezas aérea; e etapas adicionais c) e d).
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP19195653 | 2019-09-05 | ||
PCT/EP2020/074293 WO2021043743A1 (en) | 2019-09-05 | 2020-09-01 | Process and system for the production of ethylene carbonate and/or ethylene glycol |
Publications (1)
Publication Number | Publication Date |
---|---|
BR112022003587A2 true BR112022003587A2 (pt) | 2022-05-24 |
Family
ID=67874359
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
BR112022003587A BR112022003587A2 (pt) | 2019-09-05 | 2020-09-01 | Processo e sistema para a produção de carbonato de etileno e/ou etileno glicol |
Country Status (7)
Country | Link |
---|---|
US (1) | US12006299B2 (pt) |
EP (1) | EP4025315B1 (pt) |
KR (1) | KR20220055464A (pt) |
CN (1) | CN114341123B (pt) |
BR (1) | BR112022003587A2 (pt) |
TW (1) | TW202114974A (pt) |
WO (1) | WO2021043743A1 (pt) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR102383931B1 (ko) * | 2021-04-08 | 2022-04-08 | 아사히 가세이 가부시키가이샤 | 환상 알킬렌카보네이트의 공업적 제조 방법 |
Family Cites Families (33)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB772145A (en) | 1954-01-11 | 1957-04-10 | Bataafsche Petroleum | A process for purifying ethylene oxide |
US3702886A (en) | 1969-10-10 | 1972-11-14 | Mobil Oil Corp | Crystalline zeolite zsm-5 and method of preparing the same |
DE3237138C2 (de) | 1981-10-16 | 1984-05-17 | Ppg Industries, Inc., Pittsburgh, Pa. | Verfahren zur Herstellung von Ethylencarbonat oder von Gemischen aus Ethylencarbonat und Ethylenglykol |
US4899011A (en) | 1986-01-15 | 1990-02-06 | Mobil Oil Corporation | Xylene isomerization process to exhaustively convert ethylbenzene and non-aromatics |
FR2700715B1 (fr) | 1993-01-28 | 1995-03-31 | Inst Francais Du Petrole | Catalyseur à base de zéolithe MFI modifiée, et son utilisation en isomérisation d'une coupe C8 aromatique. |
JP3860631B2 (ja) | 1995-11-30 | 2006-12-20 | 三菱化学株式会社 | エチレングリコールの製造方法 |
US5763691A (en) | 1995-11-30 | 1998-06-09 | Mitsubishi Chemical Corporation | Ethylene glycol process |
AR016018A1 (es) | 1998-02-03 | 2001-05-30 | Gen Electric | Metodo para preparar diarilcarbonatos con selectividad mejorada |
AU749910B2 (en) | 1998-03-19 | 2002-07-04 | Mitsubishi Chemical Corporation | Method for producing monoethylene glycol |
CN1069605C (zh) | 1998-08-20 | 2001-08-15 | 南亚塑胶工业股份有限公司 | 从乙二醇制程水中去除甲酸、乙酸的方法和装置 |
RU2186053C2 (ru) | 2000-06-15 | 2002-07-27 | Открытое акционерное общество "Нижнекамскнефтехим" | Способ получения моноэтиленгликоля волоконной чистоты |
GC0000169A (en) | 2000-09-28 | 2005-06-29 | Shell Int Research | Catalytic process for producing an alkylene glycolwith reactor-output recycle. |
JP2005224793A (ja) | 2003-07-08 | 2005-08-25 | Toray Ind Inc | エチルベンゼン含有キシレン類の変換触媒およびその触媒を用いたエチルベンゼン含有キシレン類の変換方法 |
US7105710B2 (en) | 2003-09-26 | 2006-09-12 | Shell Oil Company | Process of preparing an alkylene glycol |
WO2005032687A2 (en) | 2003-09-30 | 2005-04-14 | Clark Arthur F | Method for separating volatile components by dilutive distillation |
US7411103B2 (en) | 2003-11-06 | 2008-08-12 | Haldor Topsoe A/S | Process for the catalytic isomerisation of aromatic compounds |
EP2027917A1 (en) | 2007-07-31 | 2009-02-25 | Shell Internationale Researchmaatschappij B.V. | Catalyst composition, its preparation and use |
JP2010535833A (ja) | 2007-08-14 | 2010-11-25 | シエル・インターナシヨナル・リサーチ・マートスハツペイ・ベー・ヴエー | アルキレングリコールの調製方法 |
US8574542B2 (en) | 2007-09-10 | 2013-11-05 | Shell Oil Company | ZSM-5, its preparation and use in ethylbenzene dealkylation |
TWI423946B (zh) | 2007-11-14 | 2014-01-21 | Shell Int Research | 伸烷基二醇的製造方法 |
CA2723988A1 (en) | 2008-05-15 | 2009-11-19 | Shell Internationale Research Maatschappij B.V. | Process for the preparation of alkylene carbonate and/or alkylene glycol |
WO2009140318A1 (en) | 2008-05-15 | 2009-11-19 | Shell Oil Company | Process for the preparation of an alkylene carbonate and an alkylene glycol |
SG2014014088A (en) | 2010-04-21 | 2014-04-28 | Exxonmobil Chem Patents Inc | Xylene isomerization process and catalyst therefor |
CN102309978B (zh) | 2010-07-07 | 2013-08-28 | 中国石油化工股份有限公司 | 一种乙苯脱烷基催化剂及其制备方法和应用 |
US8242321B2 (en) | 2010-09-30 | 2012-08-14 | Uop Llc | Processes for transalkylating aromatic hydrocarbons |
CN104245584A (zh) | 2012-03-26 | 2014-12-24 | 东曹株式会社 | 具有均匀的中孔的mfi型沸石和用于制造其的方法 |
EP3197854B1 (en) | 2014-09-24 | 2019-10-30 | Shell International Research Maatschappij B.V. | Process and apparatus for the preparation of alkylene glycol |
WO2017102701A1 (en) | 2015-12-15 | 2017-06-22 | Shell Internationale Research Maatschappij B.V. | Processes and systems for removing a vinyl iodide impurity from a recycle gas stream in the production of ethylene oxide |
KR102656134B1 (ko) | 2015-12-15 | 2024-04-11 | 쉘 인터내셔날 리써취 마트샤피지 비.브이. | 가드층 시스템 및 공정 |
RU2733849C2 (ru) | 2015-12-15 | 2020-10-07 | Шелл Интернэшнл Рисерч Маатсхаппий Б.В. | Способ и система удаления иодидных примесей из потока оборотного газа в производстве этиленоксида |
TWI723100B (zh) | 2015-12-15 | 2021-04-01 | 荷蘭商蜆殼國際研究所 | 從環氧乙烷製造中的循環氣體流移除烷基碘雜質之方法及系統 |
WO2017178418A1 (en) * | 2016-04-12 | 2017-10-19 | Shell Internationale Research Maatschappij B.V. | Processes and systems for the recycle of process water in the production of ethylene glycol |
KR102613266B1 (ko) * | 2017-05-19 | 2023-12-14 | 쉘 인터내셔날 리써취 마트샤피지 비.브이. | 에틸렌 카르보네이트 및 에틸렌 글리콜의 제조 방법에서의 열 통합 |
-
2020
- 2020-09-01 KR KR1020227006523A patent/KR20220055464A/ko unknown
- 2020-09-01 EP EP20761611.1A patent/EP4025315B1/en active Active
- 2020-09-01 CN CN202080061786.1A patent/CN114341123B/zh active Active
- 2020-09-01 BR BR112022003587A patent/BR112022003587A2/pt unknown
- 2020-09-01 WO PCT/EP2020/074293 patent/WO2021043743A1/en unknown
- 2020-09-01 US US17/637,197 patent/US12006299B2/en active Active
- 2020-09-02 TW TW109129996A patent/TW202114974A/zh unknown
Also Published As
Publication number | Publication date |
---|---|
CN114341123B (zh) | 2024-02-06 |
WO2021043743A1 (en) | 2021-03-11 |
EP4025315B1 (en) | 2023-08-02 |
US12006299B2 (en) | 2024-06-11 |
TW202114974A (zh) | 2021-04-16 |
EP4025315C0 (en) | 2023-08-02 |
KR20220055464A (ko) | 2022-05-03 |
EP4025315A1 (en) | 2022-07-13 |
CN114341123A (zh) | 2022-04-12 |
US20220298132A1 (en) | 2022-09-22 |
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