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17-12-2014 дата публикации

Method for controlling hydrogen-gasoline mixing ratio of catalytic gasoline selective hydrogenation

Номер: CN104212483A
Принадлежит:

The invention relates to a method for controlling the hydrogen-gasoline mixing ratio of catalytic gasoline selective hydrogenation. The method is completed by a flow ratio control system. The system is located on a gasoline pipeline connecting a selective hydrogenation reaction feeding pump outlet and a feed heat exchanger inlet and a hydrogen feed pipeline, and is composed of a gasoline flow orifice plate, a gasoline flow regulating valve, a hydrogen flow orifice plate, a hydrogen flow regulating valve, and a hydrogen calculator. The gasoline feed flow control and the hydrogen feed flow control are realized respectively through the flow transmitter and control valve on each pipeline. The hydrogen calculator calculates a needed hydrogen flow according to the gasoline flow and an initial given hydrogen-gasoline mixing ratio. The flow of hydrogen entering a selective hydrogenation reactor is controlled, the flow adjusted hydrogen is mixed with gasoline and heat exchange is carried out, and ...

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17-12-2014 дата публикации

Method for removing arsenic from catalytic gasoline hydrogenation raw material

Номер: CN104212487A
Принадлежит:

The invention relates to a method for removing arsenic from a catalytic gasoline hydrogenation raw material. According to the method, when a fixed bed hydrogenation technology is adopted for hydrotreatment on catalytic cracking gasoline, Ni-Mo and Co-Mo series catalysts are used as the hydrogenation catalysts, and when the arsenic content of the raw material is greater than or equal to 20ppbw, the catalytic cracking gasoline firstly enters a coalescence dehydration device to undergo coalescence dehydration so as to make the free water content less than or equal to 100ppm, and the dehydrated catalytic cracking gasoline enters a dearsenication reactor by means of entering at bottom and leaving at top. The inlet temperature of the dearsenication reactor is the catalytic gasoline feed temperature 40DEG C, the inlet pressure is the catalytic gasoline feed pressure 0.5-1.0MPag, and the volume space velocity is 1.5-2.0h<-1>. The method provided by the invention can make the arsenic content of ...

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