MX2012013292A - Metodo y aparato para la separacion de un liquido de una corriente de alimentacion de gas en un reactor catalitico. - Google Patents

Metodo y aparato para la separacion de un liquido de una corriente de alimentacion de gas en un reactor catalitico.

Info

Publication number
MX2012013292A
MX2012013292A MX2012013292A MX2012013292A MX2012013292A MX 2012013292 A MX2012013292 A MX 2012013292A MX 2012013292 A MX2012013292 A MX 2012013292A MX 2012013292 A MX2012013292 A MX 2012013292A MX 2012013292 A MX2012013292 A MX 2012013292A
Authority
MX
Mexico
Prior art keywords
catalytic reactor
separation
liquid
feed stream
gas feed
Prior art date
Application number
MX2012013292A
Other languages
English (en)
Inventor
Max Thorhauge
Original Assignee
Haldor Topsoe As
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 Haldor Topsoe As filed Critical Haldor Topsoe As
Publication of MX2012013292A publication Critical patent/MX2012013292A/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
    • B01J8/0242—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 flow within the bed being predominantly vertical
    • B01J8/025—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 flow within the bed being predominantly vertical in a cylindrical shaped bed
    • 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
    • B01D5/0027—Condensation of vapours; Recovering volatile solvents by condensation by direct contact between vapours or gases and the cooling medium
    • 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
    • B01D5/0078—Condensation of vapours; Recovering volatile solvents by condensation characterised by auxiliary systems or arrangements
    • B01D5/009—Collecting, removing and/or treatment of the condensate
    • 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
    • B01J8/009—Membranes, e.g. feeding or removing reactants or products to or from the catalyst bed through a membrane
    • 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
    • B01J8/0285—Heating or cooling the reactor
    • 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
    • B01J8/0292—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 with stationary packing material in the bed, e.g. bricks, wire rings, baffles
    • 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
    • B01J8/06—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 in tube reactors; the solid particles being arranged in tubes
    • 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
    • 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
    • C07C29/1516—Multisteps
    • C07C29/1518—Multisteps one step being the formation of initial mixture of carbon oxides and hydrogen for synthesis
    • 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
    • C07C31/02—Monohydroxylic acyclic alcohols
    • C07C31/04—Methanol
    • 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
    • B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
    • B01J2208/00132—Tubes
    • 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
    • B01J2219/322—Basic shape of the elements
    • B01J2219/32203—Sheets
    • B01J2219/32237—Sheets comprising apertures or perforations
    • B01J2219/32241—Louvres

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Fluid Mechanics (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

La presente invención se refiere a un método y un aparato para la separación de un producto de reacción líquido de una corriente gaseosa en un reactor catalítico por medio de una lámina metálica que es enfriada indirectamente por una superficie de enfriamiento y que tiene una pluralidad de percolaciones en forma de protrusiones con configuración geométrica en ambos lados de la lámina cada uno con una base abierta, la base abierta está sobre el lado de la lámina que está orientado hacia un lecho de catalizador que está dispuesto hacia arrita y sobre el lado que está orientado hacia la superficie de enfriamiento, la base abierta está orientada hacia abajo. La figura más representativa de la invención es la número 1.
MX2012013292A 2010-05-20 2010-06-17 Metodo y aparato para la separacion de un liquido de una corriente de alimentacion de gas en un reactor catalitico. MX2012013292A (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DKPA201000444 2010-05-20
PCT/EP2010/003635 WO2011144229A1 (en) 2010-05-20 2010-06-17 Method and apparatus for the separation of a liquid from a gas feed stream in a catalytic reactor

Publications (1)

Publication Number Publication Date
MX2012013292A true MX2012013292A (es) 2012-12-17

Family

ID=43302861

Family Applications (1)

Application Number Title Priority Date Filing Date
MX2012013292A MX2012013292A (es) 2010-05-20 2010-06-17 Metodo y aparato para la separacion de un liquido de una corriente de alimentacion de gas en un reactor catalitico.

Country Status (15)

Country Link
US (1) US8951482B2 (es)
EP (1) EP2571612B1 (es)
KR (1) KR101504967B1 (es)
CN (1) CN102917782B (es)
AU (1) AU2010353478B2 (es)
BR (1) BR112012029429B1 (es)
CA (1) CA2799460C (es)
DK (1) DK2571612T3 (es)
EA (1) EA023818B1 (es)
ES (1) ES2530262T3 (es)
MX (1) MX2012013292A (es)
PL (1) PL2571612T3 (es)
UA (1) UA104958C2 (es)
WO (1) WO2011144229A1 (es)
ZA (1) ZA201208611B (es)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015030578A1 (en) * 2013-08-27 2015-03-05 Universiteit Twente Method of preparing methanol and reactor for use in said method

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS504626B1 (es) * 1970-08-21 1975-02-21
JPS504626Y2 (es) * 1972-04-25 1975-02-07
US5266281A (en) * 1989-09-16 1993-11-30 Xytel Technologies Partnership Catalytic reactor
US5262443A (en) 1990-03-19 1993-11-16 Haldor Topsoe A/S Method of preparing methanol
US5512255A (en) * 1994-12-06 1996-04-30 Wright Malta Corporation Apparatus for producing methanol
US6881759B2 (en) 2003-04-07 2005-04-19 Haldor Topsoe A/S Process for the preparation of methanol
DE102005001952A1 (de) * 2005-01-14 2006-07-27 Man Dwe Gmbh Rohrbündelreaktor zur Durchführung exothermer oder endothermer Gasphasenreaktionen
JP2008116102A (ja) 2006-11-02 2008-05-22 Denso Corp 冷却用熱交換器
MX2010007376A (es) * 2008-02-25 2010-08-11 Haldor Topsoe As Metodo y reactor para la preparacion de metanol.
US8258194B2 (en) * 2008-02-25 2012-09-04 Haldor Topsoe A/S Method and reactor for performing fischer-tropsch synthesis
GB201107072D0 (en) * 2011-04-27 2011-06-08 Davy Process Techn Ltd Process

Also Published As

Publication number Publication date
PL2571612T3 (pl) 2015-05-29
AU2010353478A1 (en) 2012-12-06
AU2010353478A9 (en) 2013-01-24
AU2010353478B2 (en) 2013-11-07
BR112012029429A2 (pt) 2017-02-21
BR112012029429B1 (pt) 2018-07-17
EA201291237A1 (ru) 2013-04-30
US8951482B2 (en) 2015-02-10
EP2571612B1 (en) 2014-12-24
ZA201208611B (en) 2014-01-29
DK2571612T3 (en) 2015-04-07
CA2799460C (en) 2015-08-11
CA2799460A1 (en) 2011-11-24
ES2530262T3 (es) 2015-02-27
EP2571612A1 (en) 2013-03-27
CN102917782A (zh) 2013-02-06
KR101504967B1 (ko) 2015-03-23
WO2011144229A1 (en) 2011-11-24
KR20130087377A (ko) 2013-08-06
EA023818B1 (ru) 2016-07-29
UA104958C2 (uk) 2014-03-25
CN102917782B (zh) 2015-05-27
US20130066119A1 (en) 2013-03-14

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