BR112022017326A2 - Método para a preparação de um gás de síntese - Google Patents

Método para a preparação de um gás de síntese

Info

Publication number
BR112022017326A2
BR112022017326A2 BR112022017326A BR112022017326A BR112022017326A2 BR 112022017326 A2 BR112022017326 A2 BR 112022017326A2 BR 112022017326 A BR112022017326 A BR 112022017326A BR 112022017326 A BR112022017326 A BR 112022017326A BR 112022017326 A2 BR112022017326 A2 BR 112022017326A2
Authority
BR
Brazil
Prior art keywords
synthesis gas
stream
preparation
pgo
ncc
Prior art date
Application number
BR112022017326A
Other languages
English (en)
Inventor
June Hwang Sung
Woo Kim Tae
Ki Sik
Kyu Lee Sung
Original Assignee
Lg Chemical Ltd
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 Lg Chemical Ltd filed Critical Lg Chemical Ltd
Publication of BR112022017326A2 publication Critical patent/BR112022017326A2/pt

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/36—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using oxygen or mixtures containing oxygen as gasifying agents
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G7/00—Distillation of hydrocarbon oils
    • C10G7/12—Controlling or regulating
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G35/00—Reforming naphtha
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G9/00—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/12—Feeding the process for making hydrogen or synthesis gas
    • C01B2203/1205—Composition of the feed
    • C01B2203/1211—Organic compounds or organic mixtures used in the process for making hydrogen or synthesis gas
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/12—Feeding the process for making hydrogen or synthesis gas
    • C01B2203/1205—Composition of the feed
    • C01B2203/1211—Organic compounds or organic mixtures used in the process for making hydrogen or synthesis gas
    • C01B2203/1235—Hydrocarbons
    • C01B2203/1247—Higher hydrocarbons
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/12—Feeding the process for making hydrogen or synthesis gas
    • C01B2203/1258—Pre-treatment of the feed

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

MÉTODO PARA A PREPARAÇÃO DE UM GÁS DE SÍNTESE. A presente invenção se refere a um método para a preparação de um gás de síntese, e mais particularmente, um método para a preparação de um gás de síntese que inclui: fornecer uma corrente de PGO que inclui um óleo de gás de pirólise (PGO) descarregado a partir de um processo de centro de craqueamento de nafta (NCC) para uma torre de destilação; e fornecer uma corrente de descarga inferior a partir da torre de destilação e uma corrente de PFO que inclui um óleo combustível de pirólise (PFO) descarregado a partir do processo de centro de craqueamento de nafta (NCC) para a câmara de combustão para um processo de gaseificação como uma corrente de alimentação.
BR112022017326A 2021-06-24 2021-12-11 Método para a preparação de um gás de síntese BR112022017326A2 (pt)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
KR1020210082447A KR20230000252A (ko) 2021-06-24 2021-06-24 합성가스의 제조방법
PCT/KR2021/018819 WO2022270701A1 (ko) 2021-06-24 2021-12-11 합성가스의 제조방법

Publications (1)

Publication Number Publication Date
BR112022017326A2 true BR112022017326A2 (pt) 2023-01-17

Family

ID=83457528

Family Applications (1)

Application Number Title Priority Date Filing Date
BR112022017326A BR112022017326A2 (pt) 2021-06-24 2021-12-11 Método para a preparação de um gás de síntese

Country Status (9)

Country Link
US (1) US20230257262A1 (pt)
EP (1) EP4155258A4 (pt)
JP (1) JP7436124B2 (pt)
KR (1) KR20230000252A (pt)
CN (1) CN115720570B (pt)
BR (1) BR112022017326A2 (pt)
MX (1) MX2022010767A (pt)
TW (1) TW202319333A (pt)
WO (1) WO2022270701A1 (pt)

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008050303A (ja) 2006-08-24 2008-03-06 Mitsubishi Chemicals Corp 蒸留系の制御方法、制御システム及び制御プログラム
US8083931B2 (en) * 2006-08-31 2011-12-27 Exxonmobil Chemical Patents Inc. Upgrading of tar using POX/coker
US20120291351A1 (en) 2011-05-16 2012-11-22 Lawrence Bool Reforming methane and higher hydrocarbons in syngas streams
EA033009B1 (ru) * 2013-07-02 2019-08-30 Сауди Бейсик Индастриз Корпорейшн Способ и установка для конверсии сырой нефти в нефтехимические продукты с повышенным выходом бтк
KR101811676B1 (ko) * 2015-03-12 2017-12-22 주식회사 에젤 나프타 정제 장치 및 이를 이용한 정제 방법
KR20170089253A (ko) 2016-01-26 2017-08-03 성균관대학교산학협력단 분해 가스 오일을 이용한 수소 및 메탄 가스 생성 공정
US10472580B2 (en) * 2016-11-21 2019-11-12 Saudi Arabian Oil Company Process and system for conversion of crude oil to petrochemicals and fuel products integrating steam cracking and conversion of naphtha into chemical rich reformate
US10689587B2 (en) 2017-04-26 2020-06-23 Saudi Arabian Oil Company Systems and processes for conversion of crude oil
RU2747398C1 (ru) 2017-12-29 2021-05-04 ЛАММУС ТЕКНОЛОДЖИ ЭлЭлСи Превращение мазута в химические продукты
KR20210022870A (ko) * 2019-08-21 2021-03-04 주식회사 엘지화학 스티렌 및 벤젠의 제조 방법

Also Published As

Publication number Publication date
KR20230000252A (ko) 2023-01-02
US20230257262A1 (en) 2023-08-17
MX2022010767A (es) 2023-04-03
TW202319333A (zh) 2023-05-16
WO2022270701A1 (ko) 2022-12-29
JP2023534335A (ja) 2023-08-09
EP4155258A1 (en) 2023-03-29
CN115720570A (zh) 2023-02-28
JP7436124B2 (ja) 2024-02-21
CN115720570B (zh) 2024-03-26
EP4155258A4 (en) 2023-12-20

Similar Documents

Publication Publication Date Title
Duan et al. Non-catalytic hydropyrolysis of microalgae to produce liquid biofuels
AR121557A1 (es) Proceso y planta para la producción de hidrocarburos con huella de co₂ reducida e integración de hidrógeno mejorada
WO2013015895A3 (en) Aromatic hydrocarbons from depolymerization and deoxygenation of lignin
MY155339A (en) Process for the manufacture of hydrocarbons of biological origin
BRPI0920779A8 (pt) Método de produção de óleo biológico.
EA201891551A1 (ru) Способ и установка для превращения сырой нефти в нефтехимические продукты с повышенным выходом
ECSP11011431A (es) Hidropirólisis de biomasa para la producción de combustibles líquidos de alta calidad
MY158908A (en) Hydrocarbon thermal cracking using atmospheric distillation
WO2008092557A3 (de) Verfahren und vorrichtung zur umwandlung von biomasse in kraftstoff
MY150287A (en) Fuel and fuel blending components from biomass derived pyrolysis oil
AR082398A1 (es) Mejoramiento del proceso de fischer-tropsch para la formulacion de combustible de hidrocarburos
FI20136345L (fi) Integroitu prosessi hiilivetyjen tuottamiseksi
RU2015105405A (ru) Способ конверсии углеводородных исходных материалов с получением потоков олефиновых продуктов посредством термического парового крекинга
BR102012005735A2 (pt) mÉtodo para processamento cinza,e, usina de processamento de cinza com um reator de leito fluidizado
RU2015105404A (ru) Способ получения олефинов путем термического парового крекинга
RU2014149072A (ru) Способ модернизации установок для получения аммиака, использующих природный газ
CL2020000948A1 (es) Proceso y aparato para el hidrotratamiento de aceite de pirólisis.
BR112022017326A2 (pt) Método para a preparação de um gás de síntese
CO6310985A2 (es) Dispositivo para generar un destilado intermedio a partir de fuentes de energia hidrocarbonaceas, un catalizador y al menos un aditivo para asegurar una elevada estabilidad de aceite que fluye en el reactor, y sus procedimientos
MX356953B (es) Mejoramiento del proceso de fischer-tropsch para la formulación de combustible de hidrocarburo.
CO2018010347A2 (es) Gasificador de dos etapas y proceso de gasificación con flexibilidad de materias primas
BR112022017005A2 (pt) Método para preparar gás de síntese e hidrocarboneto aromático
BR112017012387A2 (pt) reator para produzir um gás de produto de um combustível
BR112022017321A2 (pt) Método para preparar gás de síntese e hidrocarboneto aromático
BR112023021883A2 (pt) Sistema e processo para a produção de combustíveis sintéticos sem emissão de dióxido de carbono