MX9602883A - Procedimiento y dispositivo de destilacion activa con distribucion de particulas en las fases liquida y vapor. - Google Patents

Procedimiento y dispositivo de destilacion activa con distribucion de particulas en las fases liquida y vapor.

Info

Publication number
MX9602883A
MX9602883A MX9602883A MX9602883A MX9602883A MX 9602883 A MX9602883 A MX 9602883A MX 9602883 A MX9602883 A MX 9602883A MX 9602883 A MX9602883 A MX 9602883A MX 9602883 A MX9602883 A MX 9602883A
Authority
MX
Mexico
Prior art keywords
zone
liquid
distillation
catalytic
vapour
Prior art date
Application number
MX9602883A
Other languages
English (en)
Other versions
MX195220B (es
Inventor
Marie-Claire Marion
Jean-Charles Viltard
Philippe Travers
Isabelle Harter
Alain Forestiere
Original Assignee
Inst Francais Du Petrole
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
Priority claimed from FR9509060A external-priority patent/FR2737131B3/fr
Application filed by Inst Francais Du Petrole filed Critical Inst Francais Du Petrole
Publication of MX9602883A publication Critical patent/MX9602883A/es
Publication of MX195220B publication Critical patent/MX195220B/es

Links

Classifications

    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
    • B01J8/0446—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical
    • B01J8/0461—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical annular shaped beds
    • B01J8/0469—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical annular shaped beds the beds being superimposed one above the other
    • 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
    • B01D3/32—Other features of fractionating columns ; Constructional details of fractionating columns not provided for in groups B01D3/16 - B01D3/30
    • 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
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
    • B01J8/0492—Feeding reactive fluids
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C15/00—Cyclic hydrocarbons containing only six-membered aromatic rings as cyclic parts
    • C07C15/02—Monocyclic hydrocarbons
    • C07C15/067—C8H10 hydrocarbons
    • C07C15/073—Ethylbenzene
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
    • C07C2/54—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition of unsaturated hydrocarbons to saturated hydrocarbons or to hydrocarbons containing a six-membered aromatic ring with no unsaturation outside the aromatic ring
    • C07C2/64—Addition to a carbon atom of a six-membered aromatic ring
    • 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)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

La presente invencion se refiere a un procedimiento de destilacion reactiva en una zona de destilacion reactiva que contiene cuando menos una zona catalítica, enmarcada por dos zonas de destilacion, en donde el vapor de la destilacion circula desde la porcion inferior hacia la porcion superior, de manera que no entre prácticamente en contacto con el catalizador, y en donde el líquido circula después de la zona de destilacion superior (5) hasta la zona sensiblemente central por abajo de la zona catalítica, sin entrar en contacto con el catalizador, circulando después radialmente por abajo de la zona catalítica mediante cuando menos un elemento (20), de manera que se introduzca en una zona de reparticion (23) de líquido, circulando después a través del lecho catalítico (8) en la zona catalítica, después de lo cual el líquido es recuperado por cuando menos un elemento derramador o vertedor (19) de líquido, en la zona de destilacion inferior (14). La presente invencion se refiere también a un dispositivo de destilacion reactiva.
MX9602883A 1995-07-24 1996-07-19 Procedimiento y dispositivo de destilacion activa con distribucion de particulas en las fases liquida y vapor. MX195220B (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR9509060A FR2737131B3 (fr) 1995-07-24 1995-07-24 Procede et dispositif de distillation reactive avec distribution particuliere des phases liquide et vapeur
FR9515532A FR2737132B1 (fr) 1995-07-24 1995-12-27 Procede et dispositif de distillation reactive avec distribution particuliere des phases liquide et vapeur

Publications (2)

Publication Number Publication Date
MX9602883A true MX9602883A (es) 1997-01-31
MX195220B MX195220B (es) 2000-02-04

Family

ID=26232122

Family Applications (1)

Application Number Title Priority Date Filing Date
MX9602883A MX195220B (es) 1995-07-24 1996-07-19 Procedimiento y dispositivo de destilacion activa con distribucion de particulas en las fases liquida y vapor.

Country Status (8)

Country Link
US (1) US5776320A (es)
EP (1) EP0755706B1 (es)
JP (1) JP4069217B2 (es)
KR (1) KR100400424B1 (es)
DE (1) DE69636787T2 (es)
ES (1) ES2280081T3 (es)
FR (1) FR2737132B1 (es)
MX (1) MX195220B (es)

Families Citing this family (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2743079B1 (fr) * 1995-12-27 1998-02-06 Inst Francais Du Petrole Procede et dispositif d'hydrogenation selective par distillation catalytique comportant une zone reactionnelle a co-courant ascendant liquide-gaz
FR2743081B1 (fr) * 1995-12-27 1998-01-30 Inst Francais Du Petrole Procede de reduction selective de la teneur en benzene et en composes insatures legers d'une coupe d'hydrocarbures
FR2759303B1 (fr) * 1997-02-12 1999-03-19 Inst Francais Du Petrole Colonne modulaire comportant une zone de reaction et une zone de separation
US6149879A (en) * 1997-02-12 2000-11-21 Institut Francais Du Petrole Modular device that comprises a reaction zone and a separation zone
DE19860146A1 (de) 1998-12-24 2000-06-29 Bayer Ag Verfahren und Anlage zur Herstellung von Silan
US6284104B1 (en) * 1999-03-04 2001-09-04 Catalytic Distillation Technologies Apparatus and process for hydrogenations
US7273957B2 (en) * 1999-05-04 2007-09-25 Catalytic Distillation Technologies Process for the production of gasoline stocks
US6500309B1 (en) * 1999-12-11 2002-12-31 Peter Tung Dimensions in reactive distillation technology
RU2326106C2 (ru) 2002-10-11 2008-06-10 Акцо Нобель Н.В. Способ получения монохлоруксусной кислоты
US20060260927A1 (en) * 2005-05-19 2006-11-23 Armen Abazajian Apparatus and method for continuous catalytic reactive distillation and on-line regeneration of catalyst
US20080116053A1 (en) * 2006-11-20 2008-05-22 Abb Lummus Global Inc. Non-refluxing reactor stripper
CN101254444B (zh) * 2007-12-05 2010-12-01 南京大学 一种催化反应、精馏集成工艺及其专用设备
US20090183981A1 (en) * 2008-01-23 2009-07-23 Catalytic Distillation Technologies Integrated pyrolysis gasoline treatment process
CN102485305B (zh) * 2010-12-03 2013-11-06 中国石油天然气股份有限公司 一种用于叔丁醇催化精馏脱水的催化剂填装结构及工艺
CN104203388B (zh) * 2012-02-13 2018-01-02 反应性精馏技术有限公司 用于进行化学反应的反应性精馏塔
CN103421532B (zh) * 2012-05-15 2015-07-29 中国石油化工股份有限公司 一种固体酸烷基化反应方法
FR3045599B1 (fr) 2015-12-18 2018-01-12 IFP Energies Nouvelles Procede de production de butadiene a partir de butanediols
FR3050649B1 (fr) * 2016-04-29 2021-03-19 Ifp Energies Now Nouveau dispositif de distribution du gaz et du liquide dans les colonnes de distillation catalytique
US10518235B2 (en) * 2017-07-28 2019-12-31 Uop Llc Methods and apparatus for fluid contacting in a downflow vessel
US10376856B2 (en) * 2017-07-28 2019-08-13 Uop Llc Methods for fluid contacting in a downflow vessel
JP7066871B2 (ja) * 2017-12-15 2022-05-13 シロニックス リニューアブルス，インコーポレイティド 界面活性剤を形成するための反応性蒸留
FR3077818B1 (fr) 2018-02-09 2020-02-28 IFP Energies Nouvelles Procede de separation d'olefines non lineaires d'une charge olefinique par distillation reactive
WO2020014304A1 (en) 2018-07-12 2020-01-16 Sironix Renewables, Llc Surfactants from long-chain carbon-containing molecules
EP4081508A4 (en) 2019-12-23 2024-01-17 Sironix Renewables Inc SURFACTANTS FROM ALDEHYDES
US11492338B2 (en) 2020-05-04 2022-11-08 Sironix Renewables, Inc. Furan surfactant compositions and methods

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CH366519A (de) * 1961-10-06 1963-01-15 Lonza Ag Vorrichtung für langsam verlaufende chemische Reaktionen und zur Trennung der Reaktionsprodukte
DE1801538A1 (de) * 1968-10-05 1970-06-04 Metallgesellschaft Ag Ablauf fuer Kolonnenboeden
CH667704A5 (de) * 1986-02-07 1988-10-31 Sulzer Ag Verfahren und vorrichtung zur gleichmaessigen verteilung einer fluessigkeit auf eine querschnittsflaeche.
IT1243773B (it) * 1990-08-01 1994-06-28 Snam Progetti Procedimento per la preparazione di eteri alchilici terziari ed apparecchiatura di distillazione reattiva
US5338517A (en) * 1992-05-18 1994-08-16 Chemical Research & Licensing Company Catalytic distillation column reactor and tray

Also Published As

Publication number Publication date
JP4069217B2 (ja) 2008-04-02
FR2737132B1 (fr) 1997-09-19
US5776320A (en) 1998-07-07
MX195220B (es) 2000-02-04
DE69636787D1 (de) 2007-02-08
FR2737132A1 (fr) 1997-01-31
KR970005334A (ko) 1997-02-19
DE69636787T2 (de) 2007-10-04
ES2280081T3 (es) 2007-09-01
EP0755706B1 (fr) 2006-12-27
EP0755706A1 (fr) 1997-01-29
JPH0929090A (ja) 1997-02-04
KR100400424B1 (ko) 2004-01-07

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