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Methanol and light hydrocarbon coupling cracking device and method

A cracking device and technology for light hydrocarbons, applied in chemical instruments and methods, molecular cracking to produce hydrocarbons, bulk chemical production, etc., can solve the problems of low yield of low-carbon olefins and high reaction energy consumption

Active Publication Date: 2020-09-01
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

After decades of development, steam cracking has become a very mature technology, but there are still the following problems: high reaction energy consumption, low yield of low-carbon olefins

Method used

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  • Methanol and light hydrocarbon coupling cracking device and method
  • Methanol and light hydrocarbon coupling cracking device and method
  • Methanol and light hydrocarbon coupling cracking device and method

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Embodiment 1

[0076] in such as figure 1 In the methanol-light hydrocarbon coupled cracking unit shown, the light hydrocarbon feed is straight-run naphtha, and the properties of the straight-run naphtha are shown in Table 1. The mass flow rate of the first catalyst in the first regeneration inclined tube and the mass flow rate of the first catalyst in the second regeneration inclined tube to the mass flow ratio of the straight-run naphtha entering the riser reactor is 30:1, and the regenerant temperature is 700°C, the inlet temperature of the riser reactor is 680°C, the outlet temperature is 630°C, and the reaction pressure is 0.1MPa. The inlet temperature of the fluidized bed reactor is 630°C, the outlet temperature is 600°C, and the reaction pressure is 0.1MPa, the mass flow rate of the second catalyst in the third regeneration inclined tube and the mass flow rate of the second catalyst in the fourth regeneration inclined tube and The mass flow ratio of methanol entering the fluidized be...

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Abstract

The invention discloses a methanol and light hydrocarbon coupling cracking device and method, and belongs to the technical field of petrochemical engineering. The device comprises a riser reactor anda fluidized bed reactor, a light hydrocarbon feed port and a catalyst inlet are arranged at one end of the riser reactor, the other end of the riser reactor is communicated with the fluidized bed reactor, and a methanol feed port is arranged at the end, communicated with the riser reactor, of the fluidized bed reactor. According to the device, a series reactor combining the riser and the fluidizedbed is used, so that the coupling of light hydrocarbon cracking reaction and methanol cracking reaction can be realized, the gas-solid contact time required by light hydrocarbon cracking is ensured,and the one-way yield of low-carbon olefin is improved. The device is adopted, light hydrocarbon and a first catalyst are contacted in the riser reactor and are subjected to cracking reaction, generated low-carbon olefin and the reacted first catalyst enter the fluidized bed reactor to contact methanol for reaction, and the two reactions share one catalyst and one reactor, so that the coupling ofenergy and reaction is realized, and the purpose of increasing the yield of low-carbon olefin is achieved.

Description

technical field [0001] The invention relates to the field of petrochemical technology, in particular to a methanol and light hydrocarbon coupled cracking device and method. Background technique [0002] Low-carbon olefins such as ethylene and propylene are important raw materials for the petrochemical industry. The production technologies of low-carbon olefins include steam cracking, catalytic cracking, propane dehydrogenation, methanol-to-olefins, olefins disproportionation and catalytic cracking of light hydrocarbons. At present, the production of light olefins mainly adopts steam cracking process, and its raw materials are usually straight run naphtha, hydrocracked naphtha, hydrogenated light wax oil and top oil from reforming unit. After decades of development, steam cracking has become a very mature technology, but there are still the following problems: high reaction energy consumption and low yield of low-carbon olefins. [0003] In view of this, the present inventi...

Claims

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Application Information

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IPC IPC(8): C07C1/20C07C11/04C07C11/06C07C4/08
CPCC07C1/20C07C4/08C07C2529/40C07C11/04C07C11/06Y02P20/52Y02P30/20Y02P30/40
Inventor 孙世源孟凡东闫鸿飞张亚西武立宪张瑞风杨鑫
Owner CHINA PETROLEUM & CHEM CORP
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