MX2019000852A - Un proceso para preparar oxido de propileno. - Google Patents

Un proceso para preparar oxido de propileno.

Info

Publication number
MX2019000852A
MX2019000852A MX2019000852A MX2019000852A MX2019000852A MX 2019000852 A MX2019000852 A MX 2019000852A MX 2019000852 A MX2019000852 A MX 2019000852A MX 2019000852 A MX2019000852 A MX 2019000852A MX 2019000852 A MX2019000852 A MX 2019000852A
Authority
MX
Mexico
Prior art keywords
stream
propylene oxide
propene
effluent stream
distillation
Prior art date
Application number
MX2019000852A
Other languages
English (en)
Inventor
Parvulescu Andrei-Nicolae
Weber Markus
Urbanczyk Daniel
Riedel Dominic
Wegerle Ulrike
Weidenbach Meinolf
Witzl Werner
Henrique Teles Joaquim
Mueller Ulrich
Schelling Heiner
Kramp Marvin
Mueller Christian
Tonio Woerz Nicolai
Metzen Bernd
Keller Tobias
Luecke Karsten
Original Assignee
Basf Se
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Basf Se filed Critical Basf Se
Publication of MX2019000852A publication Critical patent/MX2019000852A/es

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07D—HETEROCYCLIC COMPOUNDS
    • C07D301/00—Preparation of oxiranes
    • C07D301/32—Separation; Purification
    • 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
    • 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
    • B01D3/009—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping in combination with chemical reactions
    • 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
    • B01D3/34—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
    • B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
    • B01D5/0057—Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes
    • B01D5/006—Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes with evaporation or distillation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/70—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65
    • B01J29/7038—MWW-type, e.g. MCM-22, ERB-1, ITQ-1, PSH-3 or SSZ-25
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/86—Borosilicates; Aluminoborosilicates
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/89—Silicates, aluminosilicates or borosilicates of titanium, zirconium or hafnium
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/40—Catalysts, in general, characterised by their form or physical properties characterised by dimensions, e.g. grain size
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/0009—Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
    • B01J37/0027—Powdering
    • B01J37/0045—Drying a slurry, e.g. spray drying
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07D—HETEROCYCLIC COMPOUNDS
    • C07D301/00—Preparation of oxiranes
    • C07D301/02—Synthesis of the oxirane ring
    • C07D301/03—Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds
    • C07D301/12—Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds with hydrogen peroxide or inorganic peroxides or peracids
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07D—HETEROCYCLIC COMPOUNDS
    • C07D303/00—Compounds containing three-membered rings having one oxygen atom as the only ring hetero atom
    • C07D303/02—Compounds containing oxirane rings
    • C07D303/04—Compounds containing oxirane rings containing only hydrogen and carbon atoms in addition to the ring oxygen atoms
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
    • B01J2229/10—After treatment, characterised by the effect to be obtained
    • B01J2229/18—After treatment, characterised by the effect to be obtained to introduce other elements into or onto the molecular sieve itself
    • B01J2229/186—After treatment, characterised by the effect to be obtained to introduce other elements into or onto the molecular sieve itself not in framework positions
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
    • B01J2229/30—After treatment, characterised by the means used
    • B01J2229/42—Addition of matrix or binder particles
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/08—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
    • B01J29/085—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y containing rare earth elements, titanium, zirconium, hafnium, zinc, cadmium, mercury, gallium, indium, thallium, tin or lead
    • 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
    • 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
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Epoxy Compounds (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Heterocyclic Carbon Compounds Containing A Hetero Ring Having Oxygen Or Sulfur (AREA)

Abstract

La presente invención se refiere a un proceso para preparar óxido de propileno, que comprende (i) proporcionar una corriente que comprende propeno, peróxido de hidrógeno o una fuente de peróxido de hidrógeno, agua, y un disolvente orgánico; (ii) hacer pasar la corriente de alimentación de líquido proporcionada en (i) en una zona de epoxidación que comprende un catalizador de epoxidación que comprende una zeolita de titanio, y someter la corriente de alimentación de líquido a condiciones de reacción de epoxidación en la zona de epoxidación, obteniendo una mezcla de reacción que comprende propeno, óxido de propileno, agua, y el disolvente orgánico; (iii) retirar una corriente de eftuente de la zona de epoxidación, la corriente de efluente comprende óxido de propileno, agua, disolvente orgánico, y propeno; (iv) separar propeno de la corriente de efluente por destilación, que comprende (iv.1) someter la corriente de efluente a condiciones de destilación en una unidad de destilación, obteniendo una corriente superior gaseosa S0 enriquecida en propeno en comparación con la corriente de efluente sometida a condiciones de destilación, y una corriente inferior líquida S01 enriquecida en óxido de propileno, agua y disolvente orgánico en comparación con la corriente de efluente sometida a condiciones de destilación; (iv.2) devolver una porción condensada de la corriente S0 a una parte superior de la unidad de destilación.
MX2019000852A 2016-07-20 2017-07-19 Un proceso para preparar oxido de propileno. MX2019000852A (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP16180293 2016-07-20
PCT/EP2017/068223 WO2018015430A1 (en) 2016-07-20 2017-07-19 A process for preparing propylene oxide

Publications (1)

Publication Number Publication Date
MX2019000852A true MX2019000852A (es) 2019-10-04

Family

ID=56497636

Family Applications (1)

Application Number Title Priority Date Filing Date
MX2019000852A MX2019000852A (es) 2016-07-20 2017-07-19 Un proceso para preparar oxido de propileno.

Country Status (14)

Country Link
US (1) US10435381B2 (es)
EP (1) EP3487844B1 (es)
KR (1) KR102451362B1 (es)
CN (1) CN109641861B (es)
BR (1) BR112019000496B1 (es)
ES (1) ES2840052T3 (es)
HU (1) HUE052352T2 (es)
MX (1) MX2019000852A (es)
MY (1) MY190761A (es)
PL (1) PL3487844T3 (es)
RU (1) RU2740395C2 (es)
SG (1) SG11201900013PA (es)
WO (1) WO2018015430A1 (es)
ZA (1) ZA201900949B (es)

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11529618B2 (en) 2016-11-28 2022-12-20 Basf Se Catalyst composite comprising an alkaline earth metal containing CHA zeolite and use thereof in a process for the conversion of oxygenates to olefins
CN109996781A (zh) 2016-11-30 2019-07-09 巴斯夫欧洲公司 使用沸石催化剂将乙二醇转化为乙二胺的方法
CN109996783A (zh) 2016-11-30 2019-07-09 巴斯夫欧洲公司 使用mor骨架结构的铜改性沸石将单乙醇胺转化成乙二胺的方法
US10968152B2 (en) * 2017-03-13 2021-04-06 Basf Se Simplified process for isolating pure 1,3-butadiene
JP2020512325A (ja) 2017-03-21 2020-04-23 ビーエーエスエフ ソシエタス・ヨーロピアＢａｓｆ Ｓｅ 不凍剤用の防食成分の製造方法
JP2020518558A (ja) 2017-05-03 2020-06-25 ビーエーエスエフ ソシエタス・ヨーロピアＢａｓｆ Ｓｅ ゼオライトを用いた、エチレンオキシドのモノエタノールアミンおよびエチレンジアミンへの変換方法
KR102581563B1 (ko) 2017-05-15 2023-09-26 바스프 코포레이션 골격 유형 aei를 갖는 제올라이트 물질을 제조하는 방법
JP7266577B2 (ja) 2017-08-04 2023-04-28 ビーエーエスエフ ソシエタス・ヨーロピア 骨格型ｃｈａを有し、遷移金属、並びにカリウム及びセシウムの１種以上を含むゼオライト材料
MX2022003329A (es) * 2019-09-24 2022-04-07 Nova Chem Int Sa Generacion de vapor en deshidrogenacion oxidativa (odh).
CN114733449A (zh) * 2022-05-09 2022-07-12 上海簇睿低碳能源技术有限公司 一种基于ts-1整构催化剂的丙烯环氧化制环氧丙烷反应装置与工艺
CN115806533B (zh) * 2022-12-20 2024-02-02 江苏嘉宏新材料有限公司 一种环氧丙烷的制备工艺

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US6024840A (en) * 1997-08-08 2000-02-15 Arco Chemical Technology, L.P. Propylene oxide purification
EP1122249A1 (fr) 2000-02-02 2001-08-08 SOLVAY (Société Anonyme) Procédé de fabrication d'un oxiranne
KR20030001023A (ko) * 2001-06-28 2003-01-06 조운수 수배차량의 위치 확인 장치
DE10249378A1 (de) 2002-10-23 2004-05-06 Basf Ag Verfahren zur kontinuierlichen Rückführung des bei der Oxidation von Olefinen mit Hydroperoxiden nicht umgesetzten Olefins mittels Verdichtung und Druckdestillation
EP1558608A1 (en) 2002-10-28 2005-08-03 Warner-Lambert Company LLC Oxindole substituted piperazine derivatives
DE10317519A1 (de) * 2003-04-16 2004-11-04 Basf Ag Verfahren zur Herstellung von Propylenoxid
US7718040B2 (en) 2007-03-23 2010-05-18 Lyondell Chemical Technology, L.P. Propylene oxide recovery process
KR101475976B1 (ko) * 2007-07-10 2014-12-23 스미또모 가가꾸 가부시끼가이샤 프로필렌 옥사이드의 제조 방법
CN101885712B (zh) * 2009-05-13 2013-05-08 中国石油化工股份有限公司 生产环氧丙烷的方法
SG11201600537RA (en) * 2013-07-24 2016-02-26 Basf Se A process for preparing propylene oxide
SG10201608178YA (en) 2013-10-02 2016-11-29 Solvay Process For Manufacturing A Purified Aqueous Hydrogen Peroxide Solution
RU2705993C2 (ru) * 2014-10-27 2019-11-13 Басф Се Перегонка с частичным потоком

Also Published As

Publication number Publication date
US10435381B2 (en) 2019-10-08
SG11201900013PA (en) 2019-02-27
KR20190038849A (ko) 2019-04-09
RU2019104625A (ru) 2020-08-21
PL3487844T3 (pl) 2021-04-06
WO2018015430A1 (en) 2018-01-25
US20190169149A1 (en) 2019-06-06
BR112019000496A2 (pt) 2019-04-24
HUE052352T2 (hu) 2021-04-28
ES2840052T3 (es) 2021-07-06
CN109641861A (zh) 2019-04-16
EP3487844B1 (en) 2020-09-30
RU2740395C2 (ru) 2021-01-13
RU2019104625A3 (es) 2020-10-26
KR102451362B1 (ko) 2022-10-05
ZA201900949B (en) 2021-06-30
EP3487844A1 (en) 2019-05-29
BR112019000496B1 (pt) 2022-12-06
CN109641861B (zh) 2023-05-12
MY190761A (en) 2022-05-12

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