US2020290869A1PendingUtilityA1

Process for producing a synthesis gas

Assignee: CASALE SAPriority: Nov 6, 2014Filed: May 29, 2020Published: Sep 17, 2020
Est. expiryNov 6, 2034(~8.3 yrs left)· nominal 20-yr term from priority
B01J 2219/00024C10J 2300/1668C01B 2203/0822Y02P20/10C01B 2203/0455C01B 2203/127C10J 2300/1838C01B 2203/025C01B 2203/0811C01B 2203/84C01B 2203/068C10J 3/82C01B 2203/1241C01B 2203/046C01B 2203/061C10K 1/005C01B 3/384Y02P20/129C01B 2203/0415C01B 2203/0445C10J 2300/0956C10J 2300/0959C10J 2300/1853C01B 2203/0288C01B 2203/0405C01B 2203/0233C01B 3/025C01B 2203/0485C10J 3/002C10J 2300/1678C01B 2203/0475C10J 2300/0943C10J 2300/0996C01B 2203/0255C10J 3/463B01J 2208/00504F25J 3/0233B01D 53/229B01J 8/067C10J 2300/0976C10J 2300/093C01B 2203/0244F25J 3/0223Y02P20/128Y02P20/13
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Claims

Abstract

Process for manufacturing a hydrogen-containing synthesis gas from a natural gas feedstock, comprising the conversion of said natural gas into a raw product gas and purification of said product gas, the process having a heat input provided by combustion of a fuel; said process comprises a step of conversion of a carbonaceous feedstock, and at least a portion of said fuel is a gaseous fuel obtained by said step of conversion of said carbonaceous feedstock.

Claims

exact text as granted — not AI-modified
What is claimed is: 
     
         1 . A plant for the production of a hydrogen-containing synthesis gas from a natural gas feedstock, comprising a section for the conversion of said natural gas into a raw product gas, at least one fired device producing heat, a fuel line directed to said fired device(s), and a purification section fed with said raw product gas;
 wherein it comprises a gasifier fed with a carbonaceous feedstock and in that said gasifier provides at least part of the fuel directed to said at least one fired device.   
     
     
         2 . The plant according to  claim 1 , wherein said fired device comprises at least one of the following:
 one or more burners of a radiant section of a primary reformer;   one or more burners of a convective section of a primary reformer;   one or more burners of a desulphurizer pre-heater arranged to preheat said natural gas before desulphurization and subsequent reforming;   one or more burners of a process fired heater; one or more burners of an auxiliary steam generator or steam superheater or a heat recovery steam generator downstream a gas turbine;   one or more gas turbines.   
     
     
         3 . The plant according to  claim 1 , wherein said gasifier is a solid particles-agglomerating gasifier providing a flow of ash and unconverted carbon along with a stream of raw synthesis gas. 
     
     
         4 . The plant according to  claim 1 , wherein said gasifier is fed with a sulphur sorbent and provides a stream of partly desulphurized synthesis gas.

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