A kind of methanation reactor and methanation process
A methanation reactor and reactor technology, applied in chemical instruments and methods, organic chemistry, petroleum industry, etc., can solve problems such as difficult to withstand high pressure, difficult to eliminate thermal expansion and contraction stress, large pressure drop of reactor, etc., to achieve The effect of short residence time, shortening processing time and prolonging service life
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[0065] According to a specific implementation manner of the first aspect of the present invention, the cooling medium inlet and the cooling medium outlet can be in fluid communication through a line tube arranged in the central pipe 6 and wound by a cooling medium pipeline . The cooling medium inlet and the cooling medium outlet may also be in fluid communication through a cooling medium pipeline arranged in the manifold 7 and surrounding the central cylinder 4 and / or the sleeve 5 . It should be noted that the same pair of cooling medium inlets and cooling medium outlets may be in fluid communication through multiple cooling medium pipelines.
[0066] According to the first aspect of the present invention, in order to enable the methanation reactor to produce methane, the inner surface of the micro-reaction channel 10 can be loaded with catalytically active components. Described catalytic active component can adopt the catalytic active component well known to those skilled in...
Embodiment 1
[0080] Such as image 3 As shown, the reaction device of this embodiment consists of 1# main methanation reactor 16, 2# main methanation reactor 17, 1# supplementary methanation reactor 18, 2# supplementary methanation reactor 19, steam superheater 21 , Boiler feed water heater 22, 2# cooler 23, 1# cooler 24, product separator 25 and steam drum 20 are connected. The two main methanation reactors are connected in parallel and share a steam drum 20 with the two supplementary methanation reactors.
[0081] The operation steps are as follows:
[0082] a. H 2 The / CO volume ratio is 3.0 (M=3.0), the pressure is 3.5MPa, the synthesis gas temperature is 250°C, and the total volume flow rate is 10m 3 / h, divided into two streams to enter the main methanation reactor, one stream enters the 1# main methanation reactor 16 for the main methanation reaction, and the other synthesis gas enters the 2# main methanation reactor 17 for the main methanation reaction, The micro-reaction chann...
Embodiment 2
[0093] Such as Figure 6 As shown, the reaction device of this embodiment consists of 1# main methanation reactor 16, 2# main methanation reactor 17, 1# supplementary methanation reactor 18, steam superheater 21, boiler feed water heater 22, 2# Cooler 23, 1# cooler 24, product separator 25 and steam drum 20 are connected. The two main methanation reactors are connected in parallel and share a steam drum 20 with the supplementary methanation reactor.
[0094] The operation steps are as follows:
[0095] a. The pressure is 3.0MPa, the temperature is 250°C, and the synthesis gas containing carbon monoxide, carbon dioxide and hydrogen with M=2.95 has a total volume flow rate of 10m 3 / h, divided into two streams to enter the main methanation reactor, one stream enters the 1# main methanation reactor 16 for the main methanation reaction, and the other synthesis gas enters the 2# main methanation reactor 17 for the main methanation reaction, The micro-reaction channels of the two...
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