Reaction device and production process for synthesis gas to olefin test
A technology of a reaction device and a production process, which is applied in the field of reaction devices for synthesis gas to olefins test, can solve the problems of inability to obtain quantitative parameters, hindering the large-scale development of synthesis gas to olefins, etc.
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Embodiment 1
[0059] The reactor 300 will be described first below, which is a radial reactor.
[0060] see figure 1 , the test reactor 300 for syngas to olefins has a shell 10, which is a two-stage shell, including an upper shell and a lower shell, wherein the upper shell includes a middle cylinder 12 and an upper head 11 installed on the top of the middle cylinder . The lower shell is the lower end cap 13 . A first flange 22 is installed at the lower end of the middle cylinder 12 of the upper shell, and a second flange 23 is installed at the end of the lower head 13. Bolts 25 fasten the first flange 22 and the second flange 23 on the Together, the upper shell and the lower shell form a complete shell 10 .
[0061] In this embodiment, the housing includes two housing parts, the upper housing and the lower housing. It can be understood that in other embodiments, the housing can also be composed of three housing parts or four housing parts, that is, the housing is composed of at least Co...
Embodiment 2
[0098] A synthesis gas-to-olefins production process, the production process is carried out using the reaction device described in Example 2, and the reactor 300 is filled with a silicon-aluminum catalyst, and the production process specifically includes the following steps:
[0099] (1) After being heated by the electric heater 370, the nitrogen gas enters the heat medium channel of the start-up heater, exchanges heat with the synthesis gas, and then is discharged.
[0100] (2) The synthetic gas enters the adsorber through the inlet A311 of the adsorber 310 for purification, and the purified synthetic gas is discharged from the outlet A312 of the adsorber 310 into the raw material pipe 315, and is then divided into two streams of synthetic gas, of which A stream of synthesis gas enters the refrigerant channel of the start-up heater 320 along the branch pipe A316, and enters the reactor 300 for reaction after being indirectly heated by nitrogen. Another stream of synthesis gas...
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