FIELD: machine building.
SUBSTANCE: reactor of synthetic gas has jacket-tubular configuration. Also, a flow of fluid medium has a lengthwise configuration in tube space through a tube bunch. The reactor has a distributing plate of fluid medium at inlet of tube space below a lower end of the tube bunch and a flow sleeve on outlet circular space of increased diametre at an upper end adjacent to a tube sheet, which prevents direct inflow of fluid medium of tube space into outlet of fluid medium of tube space. The tube bunch includes multitude of circular partitions and grate partitions. A lengthwise configuration of flow facilitates lower pressure drop in tube space and lower cost in comparison with regular heat exchanger of reforming with cross flow.
EFFECT: improved main design of heat exchanger of reforming.
18 cl, 9 dwg
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Authors
Dates
2011-12-20—Published
2007-07-18—Filed