CL2020002701A1 - Método para operar una instalación de reactor - Google Patents

Método para operar una instalación de reactor

Info

Publication number
CL2020002701A1
CL2020002701A1 CL2020002701A CL2020002701A CL2020002701A1 CL 2020002701 A1 CL2020002701 A1 CL 2020002701A1 CL 2020002701 A CL2020002701 A CL 2020002701A CL 2020002701 A CL2020002701 A CL 2020002701A CL 2020002701 A1 CL2020002701 A1 CL 2020002701A1
Authority
CL
Chile
Prior art keywords
pressure
absorbent
starting materials
liquid
gaseous
Prior art date
Application number
CL2020002701A
Other languages
English (en)
Inventor
Manfred Baldauf
Alexander Tremel
Katharina Meltzer
Lukas Glöser
Original Assignee
Siemens Ag
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 Siemens Ag filed Critical Siemens Ag
Publication of CL2020002701A1 publication Critical patent/CL2020002701A1/es

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1418—Recovery of products
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/002—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by condensation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1425—Regeneration of liquid absorbents
    • 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
    • B01J12/00—Chemical processes in general for reacting gaseous media with gaseous media; Apparatus specially adapted therefor
    • 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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/26—Nozzle-type reactors, i.e. the distribution of the initial reactants within the reactor is effected by their introduction or injection through nozzles
    • 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
    • B01J4/00—Feed or outlet devices; Feed or outlet control devices
    • B01J4/001—Feed or outlet devices as such, e.g. feeding tubes
    • B01J4/002—Nozzle-type elements
    • 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
    • C07C29/15—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively
    • C07C29/151—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases
    • C07C29/1512—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases characterised by reaction conditions
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2252/00—Absorbents, i.e. solvents and liquid materials for gas absorption
    • B01D2252/30—Ionic liquids and zwitter-ions
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/70—Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
    • B01D2257/704—Solvents not covered by groups B01D2257/702 - B01D2257/7027

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Gas Separation By Absorption (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

La invención se refiere a un método para operar una instalación de reactor (2) en la cual se implementan reacciones limitadas por equilibrio, que comprende los pasos de: -convertir los materiales de inicio (4) en un producto (6) en una cámara de reacción (8) bajo una presión p1, en donde un absorbente (10) se carga con el producto (6) y también absorbe los materiales de inicio (4) en el proceso; (a) descargar el absorbente cargado (10') de la cámara de reacción (8); (b) reducir la presión del absorbente (10) a una presión p2, en donde la presión p2 es más baja que la presión p1 y el producto (6) y los materiales de inicio (4) se descargan en el estado gaseoso del absorbente líquido (10); (c) separar los productos gaseosos (6) por condensación de los materiales de inicio gaseosos (4) al mismo tiempo que (d) una presión p3 se aplica al absorbente líquido, la presión p3 que es más alta que la presión p1; (e) conducir el absorbente líquido (10) bajo la presión p3 en un compresor de gas con chorro de líquido (12) en el que los materiales de inicio gaseosos (4) separados de los productos (6) se aspiran y disuelven en el absorbente líquido (10); y entonces (f) se introducen bajo la presión p4, que es más baja que la presión p3, en la cámara de reacción (8).
CL2020002701A 2018-04-20 2020-10-19 Método para operar una instalación de reactor CL2020002701A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP18168534.8A EP3556451B1 (de) 2018-04-20 2018-04-20 Verfahren zum betreiben einer reaktoranlage

Publications (1)

Publication Number Publication Date
CL2020002701A1 true CL2020002701A1 (es) 2021-04-05

Family

ID=62044584

Family Applications (1)

Application Number Title Priority Date Filing Date
CL2020002701A CL2020002701A1 (es) 2018-04-20 2020-10-19 Método para operar una instalación de reactor

Country Status (7)

Country Link
US (1) US20210146296A1 (es)
EP (1) EP3556451B1 (es)
CN (1) CN112004589A (es)
CL (1) CL2020002701A1 (es)
DK (1) DK3556451T3 (es)
MA (1) MA51535B1 (es)
WO (1) WO2019201643A1 (es)

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GB8927266D0 (en) * 1989-12-01 1990-01-31 Csir Production of methanol
DE4019170A1 (de) * 1990-06-15 1991-12-19 Henkel Kgaa Verfahren zum durchfuehren einer gleichgewichtsreaktion unter anwendung von daempfepermeation
CH687004A5 (de) * 1994-04-08 1996-08-30 Methanol Casale Sa Membranreaktor fuer die Umsetzung von gasfoermigen Ausgangsstoffen.
CN1049209C (zh) * 1995-08-25 2000-02-09 中国科学院山西煤炭化学研究所 一种合成甲醇的方法
DE19641707A1 (de) * 1996-10-10 1998-04-16 Basf Ag Verfahren zur Herstellung von 1,4-Butandiol durch katalytische Hydrierung von 1,4-Butindiol
DE59710184D1 (de) * 1996-10-18 2003-07-03 Vincent Simon Ellis Verfahren zur durchführung von durch ein gleichgewicht gekennzeichneten reaktionen
PT1034160E (pt) * 1997-11-24 2002-10-31 Energea Umwelttechnologie Gmbh Metodo para producao de metil ester de acido graxo e equipamento para realizar o mesmo
DE19814879A1 (de) * 1998-04-02 1999-10-07 Basf Ag Verfahren zur selektiven Flüssigphasenhydrierung von alpha,beta-ungesättigten Carbonylverbindungen
JP4508327B2 (ja) * 1998-12-07 2010-07-21 三菱重工業株式会社 メタノールの製造方法
CN1272094C (zh) * 1999-11-09 2006-08-30 纳幕尔杜邦公司 液体喷射压缩机
DE10050709A1 (de) * 2000-10-13 2002-04-25 Basf Ag Verfahren zur Hydrierung von unsubstituierten oder alkylsubstituierten Aromaten unter Verwendung eines Katalysators mit einem strukturierten oder monolithischen Träger
JP3806416B2 (ja) * 2003-05-28 2006-08-09 三菱重工業株式会社 除塵装置、有機系燃料のガス化システムおよびメタノール合成システム
GB0418654D0 (en) * 2004-08-20 2004-09-22 Davy Process Techn Ltd Process
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JP6121894B2 (ja) * 2013-12-25 2017-04-26 株式会社東芝 酸性ガス除去装置及び酸性ガス除去方法
CN104258913B (zh) * 2014-08-06 2016-03-30 中国科学院广州能源研究所 一种用于催化生物质合成气合成低碳混合醇的催化剂的还原装置及还原方法
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DE102016204719A1 (de) * 2016-03-22 2017-09-28 Siemens Aktiengesellschaft Reaktor
DE102016210224A1 (de) 2016-06-09 2017-12-14 Friedrich-Alexander-Universität Erlangen-Nürnberg Reaktor und Verfahren zur Umsetzung von gleichgewichtslimitierten Reaktionen
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Also Published As

Publication number Publication date
DK3556451T3 (da) 2020-08-31
MA51535A1 (fr) 2021-04-30
MA51535B1 (fr) 2022-03-31
EP3556451A1 (de) 2019-10-23
US20210146296A1 (en) 2021-05-20
CN112004589A (zh) 2020-11-27
EP3556451B1 (de) 2020-06-03
WO2019201643A1 (de) 2019-10-24

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