[go: up one dir, main page]

AR111172A2 - Métodos y aparatos para mejorar la distribución de gas - Google Patents

Métodos y aparatos para mejorar la distribución de gas

Info

Publication number
AR111172A2
AR111172A2 ARP180100557A ARP180100557A AR111172A2 AR 111172 A2 AR111172 A2 AR 111172A2 AR P180100557 A ARP180100557 A AR P180100557A AR P180100557 A ARP180100557 A AR P180100557A AR 111172 A2 AR111172 A2 AR 111172A2
Authority
AR
Argentina
Prior art keywords
methods
appliances
gas distribution
improve gas
reaction zone
Prior art date
Application number
ARP180100557A
Other languages
English (en)
Original Assignee
Grupo Petrotemex Sa De Cv
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 Grupo Petrotemex Sa De Cv filed Critical Grupo Petrotemex Sa De Cv
Publication of AR111172A2 publication Critical patent/AR111172A2/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
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20—Mixing gases with liquids
    • 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
    • B01J10/00—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor
    • B01J10/002—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor carried out in foam, aerosol or bubbles
    • 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
    • B01J10/00—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or 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
    • B01J19/18—Stationary reactors having moving elements inside
    • B01J19/1812—Tubular reactors
    • B01J19/1818—Tubular reactors in series
    • 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
    • B01J19/24—Stationary reactors without moving elements inside
    • 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
    • B01J19/24—Stationary reactors without moving elements inside
    • B01J19/245—Stationary reactors without moving elements inside placed in series
    • 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
    • B01J4/004—Sparger-type elements
    • 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
    • B01J8/1827—Feeding of the fluidising gas the fluidising gas being a reactant
    • 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
    • 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
    • B01J2208/00893—Feeding means for the reactants
    • B01J2208/00911—Sparger-type feeding elements

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Mixers With Rotating Receptacles And Mixers With Vibration Mechanisms (AREA)

Abstract

Métodos y aparatos para introducir un gas en una zona de reacción de un reactor. Tales métodos y aparatos pueden distribuir de manera más uniforme el gas en la zona de reacción. Los rociadores para introducir un gas en la zona de reacción de un reactor se pueden emplear en sistemas y métodos para llevar a cabo la oxidación en fase líquida de un compuesto oxidable, tal como para-xileno.
ARP180100557A 2010-09-22 2018-03-09 Métodos y aparatos para mejorar la distribución de gas AR111172A2 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US12/887,535 US9849434B2 (en) 2010-09-22 2010-09-22 Methods and apparatus for enhanced gas distribution

Publications (1)

Publication Number Publication Date
AR111172A2 true AR111172A2 (es) 2019-06-12

Family

ID=45816902

Family Applications (2)

Application Number Title Priority Date Filing Date
ARP110103461A AR083084A1 (es) 2010-09-22 2011-09-22 Reactor, sistema para oxidar un compuesto y metodo para producir acido dicarboxilico
ARP180100557A AR111172A2 (es) 2010-09-22 2018-03-09 Métodos y aparatos para mejorar la distribución de gas

Family Applications Before (1)

Application Number Title Priority Date Filing Date
ARP110103461A AR083084A1 (es) 2010-09-22 2011-09-22 Reactor, sistema para oxidar un compuesto y metodo para producir acido dicarboxilico

Country Status (16)

Country Link
US (1) US9849434B2 (es)
EP (1) EP2618919B1 (es)
JP (2) JP2013542067A (es)
KR (1) KR101863390B1 (es)
CN (2) CN103228345A (es)
AR (2) AR083084A1 (es)
BR (1) BR112013006584B1 (es)
CA (1) CA2811334C (es)
ES (1) ES2975167T3 (es)
LT (1) LT2618919T (es)
MX (1) MX340072B (es)
MY (1) MY180224A (es)
PL (1) PL2618919T3 (es)
RU (1) RU2604371C2 (es)
TW (1) TWI611834B (es)
WO (1) WO2012040321A2 (es)

Families Citing this family (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9725688B2 (en) * 2011-06-30 2017-08-08 Peter Simpson Bell Bioreactor for syngas fermentation
ITMI20131139A1 (it) 2013-07-05 2015-01-06 Saipem Spa Sistema e metodo di diffusione di gas per immettere un flusso gassoso, in particolare un flusso gassoso passivante, in un apparato di un impianto urea
EP3157663A1 (en) * 2014-06-19 2017-04-26 SABIC Global Technologies B.V. Enhanced homogenous catalyzed reactor systems
RU2696384C2 (ru) * 2015-04-03 2019-08-01 САИПЕМ С.п.А. Реактор и способ синтеза мочевины
DE102015008503A1 (de) * 2015-07-03 2017-01-05 TE Connectivity Sensors Germany GmbH Elektrisches Bauteil und Herstellungsverfahren zum Herstellen eines solchen elektrischen Bauteils
RU2617397C1 (ru) * 2015-12-14 2017-04-24 Акционерное общество "Специальное конструкторско-технологическое бюро "Катализатор" Система дегидрирования парафиновых углеводородов C3-C5
US20190060819A1 (en) * 2017-08-22 2019-02-28 Larry Baxter Gas/Liquid Heat and Material Exchange in the Presence of Entrained Solids
CN108364700A (zh) * 2018-02-13 2018-08-03 中国核动力研究设计院 一种采用多鼓泡臂和鼓泡环结合的鼓泡器
CN110548454A (zh) * 2018-05-30 2019-12-10 丰城三友制笔科技有限公司 气体分布器
CN110270277B (zh) * 2019-07-09 2021-10-12 中国神华煤制油化工有限公司 气体物料分布器和煤直接液化加氢反应器
CN112295508A (zh) * 2019-07-25 2021-02-02 中国石油化工股份有限公司 一种带氢气分布管的反应器及应用方法
CN111036151B (zh) * 2019-12-30 2022-02-11 上海睿碳能源科技有限公司 具有多级穿孔结构分布板的浆态床反应器
FR3106138B1 (fr) * 2020-01-09 2022-02-25 Air Liquide Digesteur comprenant un système d’injection d’oxygène présentant un moyen tubulaire comprenant une partie en forme de T
FR3106140B1 (fr) * 2020-01-09 2022-01-21 Air Liquide Digesteur comprenant un système d’injection d’oxygène présentant un moyen tubulaire conformé en quadrillage
FR3106139A1 (fr) * 2020-01-09 2021-07-16 L'Air Liquide Société Anonyme pour l'Etude et l'Exploitation des Procedes Georges Claude Digesteur comprenant un système d’injection d’oxygène présentant un moyen tubulaire enroulé autour de son axe central
CN111569454B (zh) * 2020-03-31 2021-07-09 南京延长反应技术研究院有限公司 对二甲苯制备对苯二甲酸的内置微界面氧化系统及方法
KR102690910B1 (ko) 2020-09-17 2024-08-02 주식회사 엘지화학 스파저 및 이를 포함하는 반응기
CN112337131B (zh) * 2020-11-04 2022-02-18 江苏丽港稀土材料有限公司 一种稀土发光材料制备喷淋机构及其制备方法
CN113069947B (zh) * 2021-03-19 2025-05-16 上海齐耀热能工程有限公司 一种强化热载介质与裂解原料混合的装置
KR20240172455A (ko) 2023-06-01 2024-12-10 고등기술연구원연구조합 기액 접촉 반응기
FI20235824A1 (en) * 2023-07-14 2025-01-15 Metso Finland Oy Feeding arrangement for gasified liquid and flotation cell

Family Cites Families (37)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US689460A (en) * 1901-03-23 1901-12-24 Guston O Clark Carbureter.
US1157993A (en) * 1912-03-28 1915-10-26 Karl P Mcelroy Hydrogenating process and apparatus.
US2816011A (en) * 1954-11-22 1957-12-10 Shell Dev Fluid catalyst regeneration vessel
US2980515A (en) * 1958-03-06 1961-04-18 Standard Oil Co Reaction chamber
US3911064A (en) * 1971-04-08 1975-10-07 Union Carbide Corp System for gas sparging into liquid
US3785779A (en) * 1971-08-02 1974-01-15 Exxon Research Engineering Co Gas liquid inlet distributor
DE3806539A1 (de) * 1988-03-01 1989-09-14 Herbert Huettlin Wirbelschichtapparatur, insbes. zum granulieren pulverfoermiger substanz
JPS5912096B2 (ja) * 1975-10-31 1984-03-21 三菱化学株式会社 ホウコウゾクポリカルボンサンノセイゾウホウ
JPS5265179A (en) 1975-11-26 1977-05-30 Mitsubishi Heavy Ind Ltd Equipment for vibration type vapor-liquid contact
US4081378A (en) * 1977-01-17 1978-03-28 John Zink Company Liquid aeration to reduce biological oxygen demand
JPS56146916A (en) * 1980-03-28 1981-11-14 Jgc Corp Water sealing device
FR2520634B1 (fr) * 1982-02-02 1987-02-13 Inst Francais Du Petrole Procede et dispositif pour soutirer des particules solides et introduire une charge liquide a la partie inferieure d'une zone de contact
FR2529905B1 (fr) * 1982-07-09 1988-04-08 Inst Francais Du Petrole Procede et dispositif d'hydrotraitement d'hydrocarbures en phase liquide, en presence d'un catalyseur en lit expanse ou bouillonnant
SU1125210A1 (ru) 1983-07-27 1984-11-23 Томский инженерно-строительный институт Механический аэратор
US4580597A (en) * 1985-04-15 1986-04-08 Monsanto Company Fluid distribution system
US4809744A (en) * 1987-10-08 1989-03-07 James River Corporation Uniform fluid distribution system
US5256810A (en) * 1992-10-14 1993-10-26 The Standard Oil Company Method for eliminating nitriding during acrylonitrile production
JPH06300457A (ja) 1993-04-19 1994-10-28 Shihasuda Seisakusho:Yugen 粉末流動層
KR0130715B1 (ko) * 1995-02-01 1998-04-08 유미꾸라 레이이찌 유동상 반응기 및 이를 사용한 반응 방법
JPH10216501A (ja) 1997-01-31 1998-08-18 Nkk Corp スラリー床反応器
US6080372A (en) * 1998-09-11 2000-06-27 Air Products And Chemicals, Inc. Two stage reactor for continuous three phase slurry hydrogenation and method of operation
US6358483B1 (en) 1999-07-13 2002-03-19 The Standard Oil Company Sparger for oxygen injection into a fluid bed reactor
UA58154A (uk) 2002-10-14 2003-07-15 Приватне Підприємство Фірма "Техкон" Одоризатор газу
UA65170C2 (en) 2003-06-10 2005-07-15 Volodymyr Vitaliiovyc Maksymov An aerator
US7273950B2 (en) 2003-06-13 2007-09-25 Tereftalatos Mexicanos, S.A. De C.V. Process and apparatus for the efficient oxidation of alkyl aromatic compounds
GB2412612B (en) * 2004-04-02 2008-10-29 Statoil Asa Slurry bubble column reactor
US7683210B2 (en) 2004-09-02 2010-03-23 Eastman Chemical Company Optimized liquid-phase oxidation
EP1786550A2 (en) 2004-09-02 2007-05-23 Eastman Chemical Company Optimized production of aromatic dicarboxylic acids
US7326808B2 (en) * 2006-03-01 2008-02-05 Eastman Chemical Company Polycarboxylic acid production system employing cooled mother liquor from oxidative digestion as feed to impurity purge system
US20070208194A1 (en) * 2006-03-01 2007-09-06 Woodruff Thomas E Oxidation system with sidedraw secondary reactor
JP2007269655A (ja) 2006-03-30 2007-10-18 Sumitomo Chemical Co Ltd 反応方法および反応装置
CN101396647B (zh) * 2007-09-29 2011-03-16 中科合成油技术有限公司 用于费-托合成的气-液-固三相悬浮床反应器及其应用
KR100992835B1 (ko) * 2008-02-29 2010-11-08 한국화학연구원 피셔-트롭쉬 합성반응용 고체촉매와 생성물의 연속분리배출장치 및 방법
WO2010038395A1 (ja) * 2008-09-30 2010-04-08 独立行政法人石油天然ガス・金属鉱物資源機構 液体燃料合成方法及び液体燃料合成装置
JP2010119965A (ja) 2008-11-20 2010-06-03 Ihi Corp 攪拌装置
CN101811930B (zh) 2009-02-19 2013-04-03 中国石油化工股份有限公司 用于含苯乙炔的苯乙烯物流中苯乙炔选择加氢的方法
US20100275611A1 (en) 2009-05-01 2010-11-04 Edan Prabhu Distributing Fuel Flow in a Reaction Chamber

Also Published As

Publication number Publication date
WO2012040321A2 (en) 2012-03-29
EP2618919B1 (en) 2024-01-10
PL2618919T3 (pl) 2024-07-01
CA2811334A1 (en) 2012-03-29
EP2618919A2 (en) 2013-07-31
ES2975167T3 (es) 2024-07-03
CA2811334C (en) 2019-09-17
MY180224A (en) 2020-11-25
MX340072B (es) 2016-06-22
AR083084A1 (es) 2013-01-30
RU2604371C2 (ru) 2016-12-10
JP2017035690A (ja) 2017-02-16
TW201228721A (en) 2012-07-16
KR101863390B1 (ko) 2018-07-04
CN103228345A (zh) 2013-07-31
JP2013542067A (ja) 2013-11-21
TWI611834B (zh) 2018-01-21
KR20130109140A (ko) 2013-10-07
EP2618919A4 (en) 2017-11-08
US9849434B2 (en) 2017-12-26
LT2618919T (lt) 2024-04-10
RU2013118028A (ru) 2014-10-27
WO2012040321A3 (en) 2012-05-10
BR112013006584B1 (pt) 2021-09-21
US20120068111A1 (en) 2012-03-22
MX2013003046A (es) 2013-06-24
BR112013006584A2 (pt) 2016-06-21
CN106861564A (zh) 2017-06-20
JP6378272B2 (ja) 2018-08-22

Similar Documents

Publication Publication Date Title
AR111172A2 (es) Métodos y aparatos para mejorar la distribución de gas
MY162806A (en) Organo-catalytic biomass deconstruction
WO2012059726A3 (en) Apparatus for generating hydroxyl radicals
WO2015081122A3 (en) Reactors and systems for oxidative coupling of methane
WO2012166997A3 (en) Electrochemical reactor and process
MX2013008539A (es) Dispositivo de doble poro.
EP2663397A4 (en) Production of biochar absorbent from anaerobic digestate
MY162551A (en) Method for preparing a catalyst composition for oligomerization of ethylene and respective catalyst composition pre-formation unit
EP2900067A4 (en) PROCESS FOR CONVERTING AN INACTIVE BIOCIDE TO AN ACTIVE BIOCIDE USING A CHEMICAL REACTION
PT2768043T (pt) Dispositivo técnico melhorado para o armazenamento à escala industrial de energia elétrica
IN2015DN01902A (es)
WO2013144756A3 (en) Methods and apparatus for operating a lighting network according to energy demand and energy supply
IN2014DN09600A (es)
PL2831669T3 (pl) Zasilanie sterowanego elektrycznie oszklenia z ciekłymi kryształami, sposób zasilania takiego oszklenia
WO2013111015A8 (en) Hydrogen generation
GB201005926D0 (en) Cell poration
MX2017013692A (es) Reactor de biocida sumergible y metodo.
PH12014501240A1 (en) Film containing compositions
MX2015007293A (es) Proceso para convertir compuestos fenolicos en hidrocarburos aromaticos.
UY34670A (es) Planta para la producción de peróxido de hidrógeno y proceso para su uso
SG11201502718YA (en) Hydrogen generating composition, reactor, device and hydrogen production method
WO2012170098A3 (en) Arbovirus inhibitors and uses thereof
PL2627441T3 (pl) Sposób i urządzenie do ciągłego, wysokotemperaturowego, krótkoczasowego alkoksylowania (etoksylowania, propoksylowania) związków organicznych z aktywnymi atomami wodoru
PL2640491T3 (pl) Rozpuszczalnik, sposób dostarczania cieczy absorbującej, zastosowanie rozpuszczalnika i sposób aktywowania rozpuszczalnika
SG11201500006VA (en) Reactor for carrying out an exothermic reaction in the gas phase

Legal Events

Date Code Title Description
FG Grant, registration