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US 11,408,672 B2Granted
Synthesis gas production process for the implementation of a natural gas liquefaction
AssigneeL'Air Liquide, Societe Anonyme pour l'Etude et l'Exploitation des Procedes Georges Claude
InventorsPierre Costa De Beauregard, Pascal Marty, Thomas Morel
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Abstract
Natural gas liquefaction process in combination with a synthesis gas production process, where the steam derived from the synthesis gas production process is used as a heating source for the implementation of the pre-treatment step for eliminating the impurities liable to freeze during the natural gas liquefaction process.
Claims8
A process for the liquefaction of natural gas in combination with a process for the production of synthesis gas, the liquefaction process comprising the following stages:
- Stage a):
- pretreatment of a feed natural gas in order to remove the impurities liable to freeze during the liquefaction process;
- Stage b):
- extraction, from the gas stream resulting from stage a), of a stream enriched in hydrocarbons having more than two carbon atoms;
- Stage c):
- liquefaction of the gas stream depleted in hydrocarbons having more than two carbon atoms resulting from stage b);
- the process for the production of synthesis gas comprising the following stages:
- Stage a′):
- desulfurization at a temperature of greater than 350° C. of a natural gas feed stream;
- Stage b′):
- optional prereforming, at a temperature of greater than 500° C., in order to convert the hydrocarbon chains containing at least two carbon atoms of the gas stream resulting from stage a′) into methane;
- Stage c′):
- reforming consisting in reacting, at a temperature of greater than 800° C., the gas stream resulting from stage a′) or b′) with steam in order to produce hydrogen, carbon dioxide and carbon monoxide;
- wherein the steam resulting from the process for the production of synthesis gas is used as source of heating for the implementation of stage a);
- and wherein stage a) comprises a pretreatment by adsorption by means of an adsorption system comprising between two and five containers of at least one bed of adsorbent and at least one device for heating and/or cooling an adsorption and/or regeneration stream circulating in said adsorption system and wherein the steam resulting from the process for the production of synthesis gas is employed to reheat said regeneration stream.
12 more elements
Dependencies are inferred from the claim text.