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MX2019006282A - Sistema de reactor en paralelo para deshidrogenacion de etilbenceno. - Google Patents

Sistema de reactor en paralelo para deshidrogenacion de etilbenceno.

Info

Publication number
MX2019006282A
MX2019006282A MX2019006282A MX2019006282A MX2019006282A MX 2019006282 A MX2019006282 A MX 2019006282A MX 2019006282 A MX2019006282 A MX 2019006282A MX 2019006282 A MX2019006282 A MX 2019006282A MX 2019006282 A MX2019006282 A MX 2019006282A
Authority
MX
Mexico
Prior art keywords
stage
dehydrogenation
reactor
effluent
reactor system
Prior art date
Application number
MX2019006282A
Other languages
English (en)
Inventor
Clark Jason
E Pelati Joseph
Original Assignee
Fina Technology
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 Fina Technology filed Critical Fina Technology
Publication of MX2019006282A publication Critical patent/MX2019006282A/es

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
    • C07C5/32—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with formation of free hydrogen
    • C07C5/327—Formation of non-aromatic carbon-to-carbon double bonds only
    • C07C5/333—Catalytic processes
    • 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
    • B01J8/0496—Heating or cooling the reactor
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C15/00—Cyclic hydrocarbons containing only six-membered aromatic rings as cyclic parts
    • C07C15/40—Cyclic hydrocarbons containing only six-membered aromatic rings as cyclic parts substituted by unsaturated carbon radicals
    • C07C15/42—Cyclic hydrocarbons containing only six-membered aromatic rings as cyclic parts substituted by unsaturated carbon radicals monocyclic
    • C07C15/44—Cyclic hydrocarbons containing only six-membered aromatic rings as cyclic parts substituted by unsaturated carbon radicals monocyclic the hydrocarbon substituent containing a carbon-to-carbon double bond
    • C07C15/46—Styrene; Ring-alkylated styrenes
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
    • C07C5/32—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with formation of free hydrogen
    • C07C5/327—Formation of non-aromatic carbon-to-carbon double bonds only
    • C07C5/333—Catalytic processes
    • C07C5/3332—Catalytic processes with metal oxides or metal sulfides
    • 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
    • B01J2208/00026—Controlling or regulating the heat exchange system
    • B01J2208/00035—Controlling or regulating the heat exchange system involving measured parameters
    • B01J2208/00044—Temperature measurement
    • B01J2208/00061—Temperature measurement of the reactants
    • 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
    • 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
    • B01J2208/00539—Pressure
    • 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
    • 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
    • B01J2219/00002—Chemical plants
    • B01J2219/00027—Process aspects
    • B01J2219/00038—Processes in parallel
    • 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
    • B01J2219/00002—Chemical plants
    • B01J2219/00027—Process aspects
    • B01J2219/0004—Processes 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
    • 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
    • C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/02—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the alkali- or alkaline earth metals or beryllium
    • C07C2523/04—Alkali metals
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
    • C07C2523/74—Iron group metals
    • C07C2523/745—Iron
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
    • C07C2523/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups C07C2523/02 - C07C2523/36
    • C07C2523/78—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups C07C2523/02 - C07C2523/36 with alkali- or alkaline earth metals or beryllium

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

Un proceso de deshidrogenación de múltiples etapas que incluye poner en contacto, en una primera etapa, una corriente de alimentación que comprende un hidrocarburo y vapor con un catalizador de deshidrogenación bajo condiciones de deshidrogenación para producir un efluente de primera etapa, calentar el efluente de primera etapa, y poner en contacto, en una segunda etapa, el efluente de primera etapa calentado con un catalizador de deshidrogenación bajo condiciones de deshidrogenación para producir un efluente de segunda etapa que comprende un producto de deshidrogenación, en donde la primera etapa incluye un primer reactor y un segundo reactor arreglados en paralelo, y en donde la segunda etapa incluye un tercer reactor conectado en serie con el primer reactor y el segundo reactor. También se proporciona un sistema de deshidrogenación de múltiples etapas para llevar a cabo la deshidrogenación.
MX2019006282A 2016-12-20 2017-12-12 Sistema de reactor en paralelo para deshidrogenacion de etilbenceno. MX2019006282A (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US201662436653P 2016-12-20 2016-12-20
PCT/US2017/065709 WO2018118505A1 (en) 2016-12-20 2017-12-12 Parallel reactor system for ethylbenzene dehydrogenation

Publications (1)

Publication Number Publication Date
MX2019006282A true MX2019006282A (es) 2019-08-21

Family

ID=60888695

Family Applications (1)

Application Number Title Priority Date Filing Date
MX2019006282A MX2019006282A (es) 2016-12-20 2017-12-12 Sistema de reactor en paralelo para deshidrogenacion de etilbenceno.

Country Status (12)

Country Link
US (2) US11053178B2 (es)
EP (1) EP3558909B1 (es)
JP (1) JP2020504113A (es)
KR (1) KR20190098128A (es)
CN (1) CN110099887B (es)
AR (1) AR110657A1 (es)
BR (1) BR112019010295A2 (es)
CA (1) CA3043622A1 (es)
EA (1) EA201900331A1 (es)
MX (1) MX2019006282A (es)
TW (1) TWI756323B (es)
WO (1) WO2018118505A1 (es)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA3074035A1 (en) 2017-08-28 2019-03-07 8 Rivers Capital, Llc Oxidative dehydrogenation of ethane using carbon dioxide
CN109963896B (zh) * 2017-10-12 2021-10-19 株式会社吴羽 芳香族环状低聚物的连续制造方法及连续制造装置、以及芳香族聚合物的制造方法
EP3823948A1 (en) * 2018-07-18 2021-05-26 The Chemours Company FC, LLC Production of haloolefins in an adiabatic reaction zone

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56135427A (en) 1980-03-27 1981-10-22 Mitsubishi Petrochem Co Ltd Preparation of styrene
US4628136A (en) * 1985-12-17 1986-12-09 Lummus Crest, Inc. Dehydrogenation process for production of styrene from ethylbenzene comprising low temperature heat recovery and modification of the ethylbenzene-steam feed therewith
US6380449B1 (en) * 2000-11-22 2002-04-30 Fina Technology, Inc. Dehydrogenation process
CN1259294C (zh) * 2004-07-09 2006-06-14 华东理工大学 乙苯催化脱氢生产苯乙烯的改进方法
JP2011516559A (ja) * 2008-04-09 2011-05-26 シエル・インターナシヨナル・リサーチ・マートスハツペイ・ベー・ヴエー 脱水素プロセスを改善する方法
US8084660B2 (en) * 2008-04-18 2011-12-27 Fina Technology, Inc Use of direct heating device with a reheater in a dehydrogenation unit
CN103664497B (zh) * 2012-09-05 2015-07-08 中国石油化工股份有限公司 乙苯催化脱氢生产苯乙烯的方法
EP3000800A1 (en) * 2014-09-23 2016-03-30 Borealis AG An endothermic gas phase catalytic dehydrogenation process
US9844763B2 (en) * 2015-03-31 2017-12-19 Technip Process Technology, Inc. Method of preheating dehydrogenation reactor feed

Also Published As

Publication number Publication date
US11053178B2 (en) 2021-07-06
US20210284587A1 (en) 2021-09-16
US11661386B2 (en) 2023-05-30
EP3558909A1 (en) 2019-10-30
CN110099887B (zh) 2022-07-12
BR112019010295A2 (pt) 2019-09-03
AR110657A1 (es) 2019-04-17
US20180170836A1 (en) 2018-06-21
CA3043622A1 (en) 2018-06-28
JP2020504113A (ja) 2020-02-06
EP3558909B1 (en) 2021-09-29
WO2018118505A1 (en) 2018-06-28
CN110099887A (zh) 2019-08-06
TWI756323B (zh) 2022-03-01
TW201835010A (zh) 2018-10-01
KR20190098128A (ko) 2019-08-21
EA201900331A1 (ru) 2019-12-30

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