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PE20050829A1 - Metodo y aparato para optimizar el rendimiento de un reactor de lecho percolador - Google Patents

Metodo y aparato para optimizar el rendimiento de un reactor de lecho percolador

Info

Publication number
PE20050829A1
PE20050829A1 PE2004000991A PE2004000991A PE20050829A1 PE 20050829 A1 PE20050829 A1 PE 20050829A1 PE 2004000991 A PE2004000991 A PE 2004000991A PE 2004000991 A PE2004000991 A PE 2004000991A PE 20050829 A1 PE20050829 A1 PE 20050829A1
Authority
PE
Peru
Prior art keywords
column
reactor
bed reactor
optimize
solute
Prior art date
Application number
PE2004000991A
Other languages
English (en)
Inventor
Mourad Hamedi
Thomas L Laporte
Yeung Yu Chan
Original Assignee
Bristol Myers Squibb Co
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 Bristol Myers Squibb Co filed Critical Bristol Myers Squibb Co
Publication of PE20050829A1 publication Critical patent/PE20050829A1/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
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1818—Feeding of the fluidising gas
    • 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
    • B01J8/065—Feeding reactive fluids
    • 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
    • B01J8/067—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
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1836—Heating and 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
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1872—Details of the fluidised bed 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
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
    • B01J8/22—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/0066—Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/06—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
    • F28F13/08—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media by varying the cross-section of the flow channels
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/22—Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide 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
    • 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
    • B01J2208/00212—Plates; Jackets; Cylinders
    • 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
    • B01J2208/00212—Plates; Jackets; Cylinders
    • B01J2208/00221—Plates; Jackets; Cylinders comprising baffles for guiding the flow of the heat exchange medium
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/02—Apparatus characterised by their chemically-resistant properties
    • B01J2219/025—Apparatus characterised by their chemically-resistant properties characterised by the construction materials of the reactor vessel proper
    • B01J2219/0277—Metal based
    • 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
    • B01J2219/19—Details relating to the geometry of the reactor
    • B01J2219/194—Details relating to the geometry of the reactor round
    • B01J2219/1941—Details relating to the geometry of the reactor round circular or disk-shaped
    • B01J2219/1946—Details relating to the geometry of the reactor round circular or disk-shaped conical

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion & Propulsion (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

SE REFIERE A UN REACTOR DE LECHO PERCOLADOR ADAPTADO PARA OXIDAR UN SOLUTO EN SU FASE LIQUIDA CARACTERIZADO PORQUE COMPRENDE UNA COLUMNA DEL REACTOR QUE CONTIENE UN EMPAQUE INERTE. DICHA COLUMNA TIENE UN EXTREMO DE ENTRADA DENTRO DEL CUAL UN SOLUTO ES INTRODUCIDO Y UN EXTREMO DE SALIDA DESDE EL CUAL UN PRODUCTO ES REMOVIDO, MEDIOS PARA CREAR UN FLUJO DE GAS QUE CONTIENE OXIGENO A TRAVES DE LA COLUMNA DEL REACTOR, UN RECPETACULO QUE RODEA LA COLUMNA DEL REACTOR, MEDIOS PARA INTRODUCIR REFRIGERANTE AL RECEPTACULO PROXIMO A UN EXTREMO DE LA COLUMNA Y PARA REMOVER EL REFRIGERANTE DEL RECEPTACULO PROXIMO AL OTRO EXTREMO DE LA COLUMNA. ADEMAS LA COLUMNA POSEE UNA PRIMERA Y SEGUNDA SECCIONES CONECTADAS, TAL QUE EL DIAMETRO INTERNO DE LA PRIMERA SECCION ES MAS PEQUENO QUE EL DIAMETRO INTERNO DE LA SEGUNDA SECCION. LA GEOMETRIA DEL REACTOR ESTA ADAPTADA PARA INCREMENTAR LA CAPACIDAD DE TRANSFERENCIA DE CALOR DE LAS SECCIONES INICIALES DE LAS COLUMNAS DEL REACTOR EN DONDE ES GENERADA LA CANTIDAD MAS GRANDE DE CALOR
PE2004000991A 2003-10-14 2004-10-14 Metodo y aparato para optimizar el rendimiento de un reactor de lecho percolador PE20050829A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US51098403P 2003-10-14 2003-10-14

Publications (1)

Publication Number Publication Date
PE20050829A1 true PE20050829A1 (es) 2005-09-25

Family

ID=34465172

Family Applications (1)

Application Number Title Priority Date Filing Date
PE2004000991A PE20050829A1 (es) 2003-10-14 2004-10-14 Metodo y aparato para optimizar el rendimiento de un reactor de lecho percolador

Country Status (5)

Country Link
US (1) US20050135978A1 (es)
AR (1) AR046336A1 (es)
PE (1) PE20050829A1 (es)
TW (1) TW200520843A (es)
WO (1) WO2005037423A1 (es)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BRPI0621101A2 (pt) 2005-12-21 2011-11-29 Virent Energy Systems Inc método de reforma de hidrocarbonetos oxigenados, catalisador suportado de reforma de fase aquosa, catalisador de reforma de fase aquosa e composição de matéria
AU2007353527B2 (en) * 2006-12-20 2012-12-20 Virent, Inc. Reactor system for producing gaseous products
US8017818B2 (en) 2007-03-08 2011-09-13 Virent Energy Systems, Inc. Synthesis of liquid fuels and chemicals from oxygenated hydrocarbons
NZ591808A (en) 2008-08-27 2012-12-21 Virent Inc Synthesis of C6+ alkanes from saccharides utilising multistage catalytic processes
DE102013111290B3 (de) * 2013-10-14 2014-08-21 ROOS GmbH Luft-Luft-Wärmetauscher
CN107339903B (zh) * 2017-08-02 2019-08-27 江苏宏远管业有限公司 一种热交换器放置架

Family Cites Families (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3081010A (en) * 1960-01-04 1963-03-12 Rexall Drug Chemical Pitcher and cover
US3064668A (en) * 1960-03-15 1962-11-20 Alkire Container vent valve
US3532472A (en) * 1967-03-20 1970-10-06 Shell Oil Co Apparatus for carrying out partial oxidation of organic compounds
GB1429336A (en) * 1973-05-15 1976-03-24 Shell Int Research Heat exchanger and process for cooling hot gases
CA1042021A (en) * 1975-04-10 1978-11-07 Universite D'ottawa/ University Of Ottawa Method and apparatus for carrying out hydro-genation reactions
US4203906A (en) * 1977-07-13 1980-05-20 Nippon Shokubai Kagaku Kogyo Co., Ltd. Process for catalytic vapor phase oxidation
US4378336A (en) * 1979-12-18 1983-03-29 Conoco Inc. Monolith reactor
US4405440A (en) * 1982-11-22 1983-09-20 Shell Oil Company Process for maintaining the temperature of a steam-making effluent above the dew point
DE3247821A1 (de) * 1982-12-23 1984-09-27 Kernforschungsanlage Jülich GmbH, 5170 Jülich Reaktionsrohr fuer eine exotherme, heterogen katalysierte gasreaktion, insbesondere zur fuehrung einer methanisierungsreaktion
GB2159431B (en) * 1984-05-29 1988-04-27 Shell Int Research Reactor for non-isothermic reactions and process for the preparation of hydrocarbons using such a reactor
US4693399A (en) * 1986-10-17 1987-09-15 Weatherchem Corporation Two-flap closure
DE3715713C1 (de) * 1987-05-12 1988-07-21 Borsig Gmbh Waermetauscher insbesondere zum Kuehlen von Spaltgasen
GB8721964D0 (en) * 1987-09-18 1987-10-28 Shell Int Research Multitube reactor
JPH0218303A (ja) * 1988-07-07 1990-01-22 Mitsubishi Gas Chem Co Inc 炭化水素の改質反応器および改質方法
US5211289A (en) * 1989-09-27 1993-05-18 Irving Oil Limited Removable lid
CA2072954C (en) * 1991-07-22 2001-01-02 Michael J. Forsyth Threaded dispensing closure with flap
DE4404068C1 (de) * 1994-02-09 1995-08-17 Wolfgang Engelhardt Wärmetauscher
US5671503A (en) * 1996-09-06 1997-09-30 Uebelacker; Peggy Attachable storage handle for beverage container
US6068161A (en) * 1997-07-01 2000-05-30 Creative Edge Design Group, Ltd. Stackable, thin-walled containers having a structural load distributing feature permitting caseless shipping
US6092647A (en) * 1997-09-15 2000-07-25 Yeh; Frank Beverage container with receptacle
US6301961B1 (en) * 1999-08-26 2001-10-16 Patrick J. Rolfes Insulated beverage carafe with volume indicator
WO2001044058A2 (en) * 1999-12-14 2001-06-21 Double 'h' Plastics, Inc. Stackable hinged container lid having detents
US7316804B2 (en) * 2001-08-02 2008-01-08 Ineos Usa Llc Flow reactors for chemical conversions with heterogeneous catalysts

Also Published As

Publication number Publication date
TW200520843A (en) 2005-07-01
US20050135978A1 (en) 2005-06-23
AR046336A1 (es) 2005-12-07
WO2005037423A1 (en) 2005-04-28

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