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Космические корабли и станции, автоматические КА и методы их проектирования, бортовые комплексы управления, системы и средства жизнеобеспечения, особенности технологии производства ракетно-космических систем

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Применить Всего найдено 3. Отображено 3.
27-04-2011 дата публикации

CO conversion technique matched to coal gasification

Номер: CN0101050390B
Принадлежит:

This invention discloses a process for converting CO in pulverized coal gasification. The process comprises: introducing crude synthesis gas from pulverized coal gasification into a gas-liquid separator, mixing the gas from separator top with outside middle-pressure overheated steam, middle-pressure steam and a small amount of condensate from steam stripping, introducing into a pre-conversion furnace, controlling the temperature increase, introducing the converted gas into 1# conversion furnace, performing in-depth CO conversion, introducing high-temperature shift gas into a middle-pressure waste boiler to generate4.0 MPa steam with the condensate produced in the process, introducing all middle-pressure steam into fresh converted gas for recycling, quenching with the condensate for humidification, converting in 2# conversion furnace, cooling he converted gas by a water preheater, introducing into 3# conversion furnace, recovering waste heat until the output gas is less than or equal to ...

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09-04-2008 дата публикации

Waste heat reclaiming process for CO transformation

Номер: CN0101157442A
Принадлежит:

A waste heat recovery technics is used for CO conversion. The invention is characterized in that conversion gas recycles quantity of heat by a 1 conversion furnace, a medium-pressure waste pot, a 2 conversion furnace, a boiler water preheater, a 3 conversion furnace and a low-pressure waste pot, and then enters a low temperature formaldehyde washing reboiler and a desalting water preheater in turn after a 1 liquor condensate separator separates the liquor condensate to recycle reaction waste heat. The conversion gas enters the 2 liquor condensate separator and the conversion gas separated by the 2 liquor condensate separator is cooled 15 DEG C to not more than 40 DEG C by a conversion gas cooler, and then the conversion gas enters the 3 liquor condensate separator to be sent to the next working procedure. The generating low pressure steam is partly used for the steam of low pressure liquor condensate steam stripping. The invention has the advantages that a plurality of medium-pressure steam ...

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21-07-2010 дата публикации

Waste heat reclaiming process for CO transformation

Номер: CN0101157442B
Принадлежит:

A waste heat recovery technics is used for CO conversion. The invention is characterized in that conversion gas recycles quantity of heat by a 1 conversion furnace, a medium-pressure waste pot, a 2 conversion furnace, a boiler water preheater, a 3 conversion furnace and a low-pressure waste pot, and then enters a low temperature formaldehyde washing reboiler and a desalting water preheater in turn after a 1 liquor condensate separator separates the liquor condensate to recycle reaction waste heat. The conversion gas enters the 2 liquor condensate separator and the conversion gas separated by the 2 liquor condensate separator is cooled 15 DEG C to not more than 40 DEG C by a conversion gas cooler, and then the conversion gas enters the 3 liquor condensate separator to be sent to the next working procedure. The generating low pressure steam is partly used for the steam of low pressure liquor condensate steam stripping. The invention has the advantages that a plurality of medium-pressuresteam ...

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