MX9501161A - Montaje catalizador de fase liquida para torre de proceso quimico. - Google Patents

Montaje catalizador de fase liquida para torre de proceso quimico.

Info

Publication number
MX9501161A
MX9501161A MX9501161A MX9501161A MX9501161A MX 9501161 A MX9501161 A MX 9501161A MX 9501161 A MX9501161 A MX 9501161A MX 9501161 A MX9501161 A MX 9501161A MX 9501161 A MX9501161 A MX 9501161A
Authority
MX
Mexico
Prior art keywords
liquid phase
tower
vapor
assembly
phase
Prior art date
Application number
MX9501161A
Other languages
English (en)
Inventor
Joseph Charles Gentry
Original Assignee
Glitsch
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 Glitsch filed Critical Glitsch
Publication of MX9501161A publication Critical patent/MX9501161A/es

Links

Classifications

    • 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
    • B01D3/007—Energy recuperation; Heat pumps
    • 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
    • B01D3/16—Fractionating columns in which vapour bubbles through liquid
    • B01D3/18—Fractionating columns in which vapour bubbles through liquid with horizontal bubble plates
    • B01D3/20—Bubble caps; Risers for vapour; Discharge pipes for liquid
    • 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
    • B01D3/16—Fractionating columns in which vapour bubbles through liquid
    • 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
    • B01J19/32—Packing elements in the form of grids or built-up elements for forming a unit or module inside the apparatus for mass or heat transfer
    • 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
    • B01J8/008—Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
    • 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
    • B01J8/0446—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
    • B01J8/0449—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 beds
    • B01J8/0453—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 beds the beds being superimposed one above the other
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
    • B01J2208/00247—Reflux columns
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00548—Flow
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00796—Details of the reactor or of the particulate material
    • B01J2208/00884—Means for supporting the bed of particles, e.g. grids, bars, perforated plates
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32—Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/324—Composition or microstructure of the elements
    • B01J2219/32466—Composition or microstructure of the elements comprising catalytically active material
    • 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
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S261/00—Gas and liquid contact apparatus
    • Y10S261/06—Backfire

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Catalysts (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)

Abstract

Se describe un montaje catalítico o de catalizador, mejorado, para torres de contacto vapor/líquido. Los medios catalíticos utilizados para promover reacciones químicas se aseguran sustancialmente en la fase líquida de la torre, tal como en la porcion inferior de la misma, para mejorar la eficiencia de transferencia de masa. A diferencia de los montajes para torre de proceso de la técnica previa, en donde la destilacion en conjuncion con la reaccion química se presenta en la fase vapor o en una fase mezclada, la presente invencion confina sustancialmente la etapa de reaccion a la fase líquida. De esta manera, la reaccion es menos obstaculizante al flujo de vapor dentro de la torre, para promover un mejor mezclado y difusion de los componentes de alimentacion.
MX9501161A 1994-03-04 1995-03-01 Montaje catalizador de fase liquida para torre de proceso quimico. MX9501161A (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US20674894A 1994-03-04 1994-03-04

Publications (1)

Publication Number Publication Date
MX9501161A true MX9501161A (es) 1997-02-28

Family

ID=22767776

Family Applications (1)

Application Number Title Priority Date Filing Date
MX9501161A MX9501161A (es) 1994-03-04 1995-03-01 Montaje catalizador de fase liquida para torre de proceso quimico.

Country Status (14)

Country Link
US (1) US5779993A (es)
EP (1) EP0670178A3 (es)
JP (1) JP2884139B2 (es)
KR (1) KR950031153A (es)
CN (1) CN1112853A (es)
AU (1) AU1352095A (es)
BR (1) BR9500812A (es)
CA (1) CA2143527A1 (es)
CZ (1) CZ55095A3 (es)
HU (1) HUT71029A (es)
MX (1) MX9501161A (es)
RU (1) RU95103104A (es)
SK (1) SK27595A3 (es)
TW (1) TW354505U (es)

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Publication number Priority date Publication date Assignee Title
DE19541213A1 (de) * 1995-11-04 1997-05-07 Rwe Dea Ag Verfahren zur chemischen Umsetzung von Stoffen in einer Reaktionskolonne
WO1998047824A1 (fr) * 1997-04-22 1998-10-29 Nippon Shokubai Co., Ltd. Appareil pour le traitement des eaux usees
DE19860146A1 (de) 1998-12-24 2000-06-29 Bayer Ag Verfahren und Anlage zur Herstellung von Silan
US6846959B2 (en) 2002-10-07 2005-01-25 Air Products And Chemicals, Inc. Process for producing alkanolamines
US6919000B2 (en) * 2002-12-17 2005-07-19 University Of Florida Diffusion driven desalination apparatus and process
US7225620B2 (en) * 2002-12-17 2007-06-05 University Of Florida Research Foundation, Inc. Diffusion driven water purification apparatus and process
US7265189B2 (en) * 2003-03-25 2007-09-04 Crystaphase Products, Inc. Filtration, flow distribution and catalytic method for process streams
US7722832B2 (en) 2003-03-25 2010-05-25 Crystaphase International, Inc. Separation method and assembly for process streams in component separation units
US7718137B2 (en) * 2005-10-28 2010-05-18 Eastman Chemical Company Reactor with optimized internal tray design
US7909966B2 (en) * 2005-11-02 2011-03-22 Amt International, Inc. Apparatus for catalytic distillation processes
JP5093135B2 (ja) * 2008-12-22 2012-12-05 東ソー株式会社 Ｃｏｄ除去方法及びｃｏｄ分解触媒充填塔
WO2012103653A1 (en) * 2011-02-03 2012-08-09 Co2 Solutions Inc. C02 treatments using enzymatic particles sized according to reactive liquid film thickness for enhanced catalysis
DE102011005581A1 (de) * 2011-03-15 2012-09-20 Wacker Chemie Ag Kontinuierliches Verfahren zur Herstellung SiOC-enthaltender Verbindungen
DE102013003329A1 (de) * 2013-02-25 2014-08-28 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Silane, Hybridpolymere und Photolack mit Positiv-Resist Verhalten sowie Verfahren zur Herstellung
US10744426B2 (en) 2015-12-31 2020-08-18 Crystaphase Products, Inc. Structured elements and methods of use
US10054140B2 (en) 2016-02-12 2018-08-21 Crystaphase Products, Inc. Use of treating elements to facilitate flow in vessels
JP7078055B2 (ja) * 2017-05-01 2022-05-31 ディーエスエム アイピー アセッツ ビー．ブイ． デバイスを通って輸送される材料を処理及び条件付けするためのデバイス
WO2021127644A1 (en) 2019-12-20 2021-06-24 Crystaphase Products, Inc. Resaturation of gas into a liquid feedstream
EP4210865A1 (en) 2020-09-09 2023-07-19 Crystaphase Products Inc. Process vessel entry zones

Family Cites Families (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4385033A (en) * 1980-12-04 1983-05-24 Exxon Research And Engineering Co. Reactor for fouling prone feeds
US4380529A (en) * 1980-12-04 1983-04-19 Exxon Research And Engineering Co. Hydroprocessing reactor with extended operating life
IT1137527B (it) * 1981-04-10 1986-09-10 Anic Spa Procedimento per la preparazione di eteri alchilici terziari
US4615796A (en) * 1981-10-29 1986-10-07 Chevron Research Company Method for contacting solids-containing feeds in a layered bed reactor
US4526757A (en) * 1982-11-01 1985-07-02 Exxon Research And Engineering Co. Pulsed flow vapor-liquid reactor
US4842778A (en) * 1985-12-23 1989-06-27 Glitsch, Inc. Apparatus for flow distribution in packed towers
EP0302336B1 (de) * 1987-08-04 1992-03-04 Ec Erdölchemie Gmbh Verfahren zur Spaltung von Alkyl-tert.-alkylethern
FR2628418B1 (fr) * 1988-03-08 1991-01-04 Inst Francais Du Petrole Procede de preparation d'un ether alkylique tertiaire par distillation reactive
FR2628737B1 (fr) * 1988-03-21 1990-08-24 Inst Francais Du Petrole Procede de preparation d'un ether alkylique tertiaire par distillation reactive
JPH01310732A (ja) * 1988-06-10 1989-12-14 Hitachi Ltd 固体ゲル反応筒
US5164125A (en) * 1989-03-08 1992-11-17 Glitsch, Inc. Method and apparatus for downcomer-tray operation
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Also Published As

Publication number Publication date
TW354505U (en) 1999-03-11
JP2884139B2 (ja) 1999-04-19
JPH07284656A (ja) 1995-10-31
CZ55095A3 (en) 1995-11-15
RU95103104A (ru) 1996-12-27
HUT71029A (en) 1995-11-28
KR950031153A (ko) 1995-12-18
BR9500812A (pt) 1995-10-17
AU1352095A (en) 1995-09-14
CA2143527A1 (en) 1995-09-05
EP0670178A3 (en) 1995-11-22
EP0670178A2 (en) 1995-09-06
US5779993A (en) 1998-07-14
SK27595A3 (en) 1995-09-13
HU9500554D0 (en) 1995-04-28
CN1112853A (zh) 1995-12-06

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