MX2020013185A - Procesos para iniciar el funcionamiento de los sistemas de reactor catalitico fluidizado. - Google Patents
Procesos para iniciar el funcionamiento de los sistemas de reactor catalitico fluidizado.Info
- Publication number
- MX2020013185A MX2020013185A MX2020013185A MX2020013185A MX2020013185A MX 2020013185 A MX2020013185 A MX 2020013185A MX 2020013185 A MX2020013185 A MX 2020013185A MX 2020013185 A MX2020013185 A MX 2020013185A MX 2020013185 A MX2020013185 A MX 2020013185A
- Authority
- MX
- Mexico
- Prior art keywords
- catalyst
- temperature
- commencement
- fuel gas
- processes
- Prior art date
Links
- 238000000034 method Methods 0.000 title abstract 3
- 230000003197 catalytic effect Effects 0.000 title 1
- 239000003054 catalyst Substances 0.000 abstract 9
- 239000002737 fuel gas Substances 0.000 abstract 5
- 238000002485 combustion reaction Methods 0.000 abstract 2
- 238000006243 chemical reaction Methods 0.000 abstract 1
- 239000000446 fuel Substances 0.000 abstract 1
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
- B01J8/001—Controlling 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
- B01J8/08—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
- B01J8/12—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles moved by gravity in a downward flow
- B01J8/125—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles moved by gravity in a downward flow with multiple sections one above the other separated by distribution aids, e.g. reaction and regeneration sections
-
- 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
- B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
- B01J8/26—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with two or more fluidised beds, e.g. reactor and regeneration installations
-
- 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
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
- C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
- C10G11/182—Regeneration
-
- 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
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
- C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
- C10G11/187—Controlling or regulating
-
- 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
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/20—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert heated gases or vapours
- C10G11/22—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert heated gases or vapours produced by partial combustion of the material to be cracked
-
- 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
- C10G2/00—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
- C10G2/30—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen
- C10G2/32—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts
- C10G2/33—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts characterised by the catalyst used
- C10G2/331—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts characterised by the catalyst used containing group VIII-metals
- C10G2/333—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts characterised by the catalyst used containing group VIII-metals of the platinum-group
-
- 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
- C10G9/28—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid material
- C10G9/32—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid material according to the "fluidised-bed" technique
-
- 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
-
- 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
- B01J2208/00716—Means for reactor start-up
-
- 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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1081—Alkanes
-
- 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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1088—Olefins
- C10G2300/1092—C2-C4 olefins
-
- 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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1096—Aromatics or polyaromatics
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)
- Combustion & Propulsion (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Feeding And Controlling Fuel (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Un proceso para iniciar una reacción continua en un sistema de reactor incluye introducir un catalizador en una porción de procesamiento de catalizador del sistema de reactor, en donde inicialmente el catalizador tiene una primera temperatura de 500 °C o menos, y poner en contacto el catalizador a la primera temperatura con una corriente de gas combustible de inicio que incluye al menos 80 % molar de un gas combustible de inicio, en la porción de procesamiento de catalizador. Poner en contacto el catalizador con la corriente de gas combustible de inicio causa la combustión del gas combustible de inicio. El proceso incluye mantener el contacto del catalizador con la corriente de gas combustible de inicio hasta que la temperatura del catalizador aumente de la primera temperatura a una segunda temperatura a la cual la combustión de una fuente de combustible del regenerador mantiene un intervalo de temperatura de funcionamiento en la porción de procesamiento de catalizador.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US201862694190P | 2018-07-05 | 2018-07-05 | |
| PCT/US2019/039212 WO2020009862A1 (en) | 2018-07-05 | 2019-06-26 | Processes for commencing operations of fluidized catalytic reactor systems |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| MX2020013185A true MX2020013185A (es) | 2021-02-26 |
Family
ID=67263115
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| MX2020013185A MX2020013185A (es) | 2018-07-05 | 2019-06-26 | Procesos para iniciar el funcionamiento de los sistemas de reactor catalitico fluidizado. |
Country Status (9)
| Country | Link |
|---|---|
| US (1) | US11596914B2 (es) |
| EP (1) | EP3817849B1 (es) |
| KR (1) | KR102776067B1 (es) |
| CN (1) | CN112236222B (es) |
| AR (1) | AR115716A1 (es) |
| BR (1) | BR112020024658A2 (es) |
| CA (1) | CA3104492A1 (es) |
| MX (1) | MX2020013185A (es) |
| WO (1) | WO2020009862A1 (es) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20220126281A1 (en) * | 2021-06-30 | 2022-04-28 | Uop Llc | Process for regenerating a dehydrogenation catalyst |
Family Cites Families (25)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3033906A (en) | 1958-08-06 | 1962-05-08 | Gulf Research Development Co | Process for converting normal hexane to benzene |
| US3657153A (en) | 1969-04-08 | 1972-04-18 | Inst De Cercetari Pentru Prelu | Process for the preparation of a catalyst for the reforming and aromatization of benzines |
| US4072600A (en) * | 1974-02-08 | 1978-02-07 | Mobil Oil Corporation | Catalytic cracking process |
| NL8800973A (nl) | 1988-04-14 | 1989-11-01 | Cardee Netherlands B V | Werkwijze voor het vervaardigen van prentbriefkaarten alsmede inrichting voor het uitvoeren van de werkwijze. |
| US7002052B2 (en) * | 2000-02-02 | 2006-02-21 | Dow Global Technologies Inc. | Integrated process for producing an alkenyl-substituted aromatic compound |
| DE10060099A1 (de) | 2000-12-04 | 2002-06-06 | Basf Ag | Regenerierung eines Dehydrierkatalysators |
| ITMI20011110A1 (it) * | 2001-05-25 | 2002-11-25 | Snam Progetti | Procedimento integrato per la preparazione di composti aromatici alchil e alchenil sostituiti |
| ITMI20012709A1 (it) | 2001-12-20 | 2003-06-20 | Snam Progetti | Composizione catalitica per la deidrogenazione di idrocarburi alchilaromatici |
| ITMI20040198A1 (it) | 2004-02-09 | 2004-05-09 | Snam Progetti | Dispositivo reattore-rigeneratore e suo impiego nella produzione di stirene |
| MXPA06008965A (es) | 2004-02-09 | 2007-02-20 | Down Chemical Company | Proceso para la preparacion de compuestos de hidrocarburos deshidrogenados. |
| WO2006068814A2 (en) * | 2004-12-22 | 2006-06-29 | Exxonmobil Chemical Patents, Inc. | Production of aromatic hydrocarbons from methane |
| BE1016661A3 (fr) | 2005-06-28 | 2007-04-03 | Lhoist Rech & Dev Sa | Composition de chaux pulverulente, son procede de fabrication et son utilisation. |
| CN101130466B (zh) | 2006-08-23 | 2011-05-04 | 中国科学院大连化学物理研究所 | 制取低碳烯烃流态化催化反应装置的开工方法 |
| WO2010107591A1 (en) | 2009-03-19 | 2010-09-23 | Dow Global Technologies Inc. | Dehydrogenation process and catalyst |
| US8415264B2 (en) * | 2010-04-30 | 2013-04-09 | Uop Llc | Process for regenerating catalyst in a fluid catalytic cracking unit |
| BR112014000199B1 (pt) | 2011-07-13 | 2020-06-02 | Dow Global Technologies Llc | Processo para desidrogenar um alcano |
| JP6158807B2 (ja) * | 2011-07-27 | 2017-07-05 | サウジ アラビアン オイル カンパニー | 下降流反応装置におけるパラフィン系ナフサの流動接触分解 |
| ITMI20112403A1 (it) | 2011-12-28 | 2013-06-29 | Polimeri Europa Spa | Composizione catalitica e procedimento per la deidrogenazione di buteni o miscele di butani e buteni a dare 1-3 butadiene |
| FR3002946B1 (fr) | 2013-03-06 | 2016-09-16 | Eurecat Sa | Procede pour le demarrage d'unites d'hydrotraitement ou d'hydroconversion |
| US20160060542A1 (en) | 2014-08-26 | 2016-03-03 | Exxonmobil Research And Engineering Company | Fluidized bed unit startup |
| US10227271B2 (en) | 2015-03-30 | 2019-03-12 | Dow Global Technologies Llc | Integrated C3—C4 hydrocarbon dehydrogenation process |
| US9815040B2 (en) | 2015-06-26 | 2017-11-14 | Dow Global Technologies Llc | Fluid solids contacting device |
| US9827543B2 (en) | 2015-06-30 | 2017-11-28 | Dow Global Technologies Llc | Fluid solids contacting device |
| US9889418B2 (en) | 2015-09-29 | 2018-02-13 | Dow Global Technologies Llc | Fluidized fuel gas combustor system for a catalytic dehydrogenation process |
| AR107628A1 (es) | 2016-03-01 | 2018-05-16 | Dow Global Technologies Llc | Regeneración de catalizador |
-
2019
- 2019-06-26 BR BR112020024658-1A patent/BR112020024658A2/pt not_active Application Discontinuation
- 2019-06-26 CN CN201980037668.4A patent/CN112236222B/zh active Active
- 2019-06-26 KR KR1020217001210A patent/KR102776067B1/ko active Active
- 2019-06-26 WO PCT/US2019/039212 patent/WO2020009862A1/en not_active Ceased
- 2019-06-26 CA CA3104492A patent/CA3104492A1/en active Pending
- 2019-06-26 MX MX2020013185A patent/MX2020013185A/es unknown
- 2019-06-26 US US17/256,690 patent/US11596914B2/en active Active
- 2019-06-26 EP EP19739833.2A patent/EP3817849B1/en active Active
- 2019-07-05 AR ARP190101924A patent/AR115716A1/es active IP Right Grant
Also Published As
| Publication number | Publication date |
|---|---|
| US11596914B2 (en) | 2023-03-07 |
| KR20210029201A (ko) | 2021-03-15 |
| US20210260555A1 (en) | 2021-08-26 |
| CA3104492A1 (en) | 2020-01-09 |
| KR102776067B1 (ko) | 2025-03-07 |
| WO2020009862A1 (en) | 2020-01-09 |
| CN112236222A (zh) | 2021-01-15 |
| EP3817849B1 (en) | 2025-11-19 |
| EP3817849A1 (en) | 2021-05-12 |
| AR115716A1 (es) | 2021-02-17 |
| CN112236222B (zh) | 2023-02-28 |
| BR112020024658A2 (pt) | 2021-03-02 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| MX2020013189A (es) | Procesos y sistemas quimicos que incluyen la combustion de combustibles complementarios. | |
| MX2020013186A (es) | Procesamiento quimico que usa hidrogeno que contiene combustible complementario para el procesamiento de catalizadores. | |
| MY169176A (en) | Reactor system for the production of carbon allotropes | |
| SA519410665B1 (ar) | أنظمة تكسير حفزي عالي الشدة في وجود طبقة متميعة وعمليات تتضمن إعادة تدوير محفز جزئية | |
| EA201290507A1 (ru) | Непрерывный способ карбонилирования этилена | |
| MX2020000605A (es) | Craqueo termico y catalitico integrado para la produccion de olefinas. | |
| NO20081301L (no) | Forbedret katalysatorsystem | |
| EA201791431A1 (ru) | Способ перехода между несовместимыми катализаторами | |
| EA032939B1 (ru) | Способ получения метилацетата | |
| US11325069B2 (en) | Method and apparatus for removing NOx and N2O from a gas | |
| MX2009005152A (es) | Sistemas catalizadores y procesos de polimerizacion. | |
| SG11201910001TA (en) | Fluidized bed gas distributor, reactor using fluidized bed gas distributor, and method for producing para-xylene and co-producing light olefins | |
| MX2010007480A (es) | Sistemas de alimentacion de catalizador y metodos para usarlos. | |
| MX2021002462A (es) | Metodos para operar procesos de deshidrogenacion en condiciones anormales de funcionamiento. | |
| WO2018236630A3 (en) | Reactor systems comprising fluid recycling | |
| EA202092378A1 (ru) | Способ получения водорода и углеродных продуктов | |
| MY202049A (en) | Biomass injection into fluid bed catalytic pyrolysis reactor | |
| MX2019004771A (es) | Catalizador de reduccion catalitica selectiva (scr) integrado y trampa de nox (lnt) para la reduccion del nox. | |
| MX2020013185A (es) | Procesos para iniciar el funcionamiento de los sistemas de reactor catalitico fluidizado. | |
| MY109128A (en) | Method and apparatus for stopping reaction in a gas phase polymerization reactor system | |
| EA023914B9 (ru) | Способ очистки сырьевых потоков этиленсодержащих отходящих газов | |
| MX2020006299A (es) | Planta de produccion de escoria y metodo para producir escoria en tal planta. | |
| SA521430118B1 (ar) | جهاز تفاعل ألكلة ونظام تفاعل وعملية تفاعل ألكلة محفزة بالحمض السائل | |
| SA521430022B1 (ar) | نظام اختزال مباشر وعملية ذات صلة | |
| ZA202101850B (en) | Process for preparing c2-c5 hydrocarbons using a hybrid catalyst |