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A continuous reaction and regeneration process of methanol conversion to gasoline in a fixed-bed adiabatic reactor

An adiabatic reactor and methanol conversion technology, applied in the petroleum industry, bulk chemical production, biological raw materials, etc., can solve the problem of "residual activity of the catalyst is difficult to use, etc., to improve the effective utilization rate, extend the operating life, and avoid methanol breakthrough. transparent effect

Active Publication Date: 2015-09-16
SHANXI FEISHI TECH +2
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0021] The purpose of the present invention is to provide a continuous reaction and regeneration process of methanol conversion to gasoline in a fixed bed adiabatic reactor with simple operation and high catalyst reactivity utilization rate in the reaction process, so as to solve the existing technology of methanol conversion in a fixed bed adiabatic reactor to gasoline The problem that the existing catalyst "residual activity" is difficult to use, to achieve the purpose of improving catalyst activity and simplifying the operation method

Method used

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  • A continuous reaction and regeneration process of methanol conversion to gasoline in a fixed-bed adiabatic reactor
  • A continuous reaction and regeneration process of methanol conversion to gasoline in a fixed-bed adiabatic reactor

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0060] Two fixed-bed adiabatic reactors are attached by several pipes and valves figure 1 Process connections shown.

[0061] R-a and R-b are fixed-bed adiabatic reactors made of stainless steel with an inner diameter of 3200mm. The two reactors are respectively equipped with 23.29 tons of FeZrZSM-5 molecular sieve catalyst manufactured according to the method published in Chinese patent ZL200610012810.4, and the net height of the catalyst bed is 4830mm. The total installed capacity of FeZrZSM-5 molecular sieve catalyst in the two reactors is 46.58 tons.

[0062] The whole system is purged with nitrogen, and the oxygen content is confirmed to be less than 0.5%, and the system pressure is controlled at 1.8MPa.

[0063] The valves 3a, 7a are in the open state, and the valves 3b, 7b, 10a, 10b, 12a, 12b, 14a, 14b, 15a, 15b are in the closed state.

[0064] The nitrogen circulation of the system is established through the external circulation system, and the flow of nitrogen gas...

Embodiment 2

[0102] The catalyst loading conditions and operating conditions are completely the same as in Example 1, but the catalyst is a ZSM-5 molecular sieve catalyst.

[0103] The main parameters of embodiment 2 are shown in table 3.

[0104] The main technical index of embodiment 2 is shown in table 4.

Embodiment 3

[0114] With embodiment 1, but catalyst adopts ZSM-12 molecular sieve catalyst.

[0115] The main parameters of embodiment 3 are shown in table 5.

[0116] The main technical indicators of embodiment 3 are shown in table 6.

[0117] The main parameter of table 5 embodiment 3

[0118] project

[0119] The main technical index of table 6 embodiment 3

[0120] project

[0121] The number of regenerated reactors is switched every year

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Abstract

Provided is a continuous reaction and regeneration technology used for conversion of methanol to gasoline through stationary bed adiabatic reactors. The two stationary bed adiabatic reactors work independently, the first reactor carries out a reaction for conversion of methanol to gasoline independently, and the second reactor is in a standby state; when catalysts in the first reactor approach to inactivation, the two reactors can work in a series connection mode through valve switchover until residual activity of the catalysts in the first reactor is fully utilized; the two reactors are made to work in a respective independent mode through valve switchover, the second reactor completes the reaction for conversion of methanol to gasoline independently, and the first reactor finishes catalyst regeneration operation independently and gets into the standby state. The technology is repeated in that way. The technology has the advantages that operation is simple, and the utilization rate of reactivity of the catalysts in the reaction process is high.

Description

technical field [0001] The invention belongs to the technique of converting methanol into gasoline. Specifically, it relates to a continuous reaction and regeneration process for methanol conversion to gasoline in a fixed-bed adiabatic reactor. Background technique [0002] Mobil Corporation of the United States first discovered in the 1970s that under the catalysis of ZSM-5 molecular sieves, methanol can be converted into hydrocarbon products. In September 1974, Mobil applied for the first patent of its MTG technology (USP3931349, Conversion of methanol to gasoline components). The discovery of this process is another new synthesis following the industrialization of FT technology for more than fifty years. The new process of oil products provides a new way to synthesize high-octane gasoline from coal or natural gas. [0003] To date, processes and catalysts for the conversion of methanol to hydrocarbon products, including gasoline components, have been extensively documen...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G3/00
CPCY02P20/52Y02P30/20
Inventor 李文怀张庆庚李晓崔晓曦潘国平范辉牛凤芹黄居彬黄举天
Owner SHANXI FEISHI TECH