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Separation process for preparing low-carbon olefin gas through methanol conversion

A low-carbon olefin and methanol conversion technology, applied in the field of separation technology, can solve the problems of inability to obtain purity and ineffective removal

Active Publication Date: 2014-06-18
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0020] The present invention aims at the disadvantages that the method disclosed in CN1833017A cannot obtain products such as hydrogen, methane, ethane and propane with higher purity and does not effectively remove oxygen and carbon monoxide in dimethyl ether and flue gas impurities. The components and composition characteristics of the production of low-carbon olefin gases, and a new and highly effective separation process for the separation of polymer-grade ethylene and propylene from low-carbon olefin gases

Method used

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  • Separation process for preparing low-carbon olefin gas through methanol conversion
  • Separation process for preparing low-carbon olefin gas through methanol conversion
  • Separation process for preparing low-carbon olefin gas through methanol conversion

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Embodiment Construction

[0092] Such as figure 2 as shown, figure 2The fourth and fifth stages 25 of the middle compressor are arranged between the second separation tank 23 and the third separation tank 29 . The fourth and fifth stages of the compressor 25 can also be arranged between the first separation tank 20 and the second separation tank 23, or between the third separation tank 29 and the fourth separation tank 31, or in the fourth separation tank 31 and the fifth separation tank 33, or between the fifth separation tank 33 and the sixth separation tank 35. In addition to ethylene and propylene, it also includes one or more of hydrogen, oxygen, nitrogen, carbon monoxide, carbon dioxide, methane, ethane, acetylene, propane, cyclopropane, propyne and propadiene as methanol conversion Production of low-carbon olefins gas removal of oxygenates, water and C 4 and C 4 The low-carbon olefins stream after the above hydrocarbons passes through the first dryer 2 (built-in) through the low-carbon ole...

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Abstract

The invention discloses a separation process for preparing low-carbon olefin gas through methanol conversion, aiming at overcoming the defects that products such as high-purity hydrogen, methane, ethane and propane cannot be obtained, dimethyl ether and oxygen and carbon monoxide in flue gas impurities are not effectively removed and the like in the prior art. A carbon monoxide and oxygen removal step is added in the process. Methanol-to-olefin gas with the carbon monoxide and the oxygen being removed passes through six separation tanks and then enters a high-pressure demethanation tower, a deethanization tower, an acetylene hydrogenation reactor, an ethylene rectifying tower, an allylene hydrogenation reactor, a propylene rectifying tower and the like for separation, wherein liquid which comes out from the bottoms of the first five separation tanks sequentially enters the middle-to-upper part of the demethanation tower. By adopting the separation process, polymer-grade ethylene and propylene products can be obtained and products such as high-purity hydrogen, methane, ethane and propane can also be obtained.

Description

Technical field: [0001] The invention relates to a separation process for preparing low-carbon olefin gas by converting methanol. In particular, the present invention relates to a mixture of materials comprising one or more of hydrogen, oxygen, nitrogen, carbon monoxide, carbon dioxide, methane, ethane, ethylene, acetylene, propane, propylene, cyclopropane, propyne and propadiene Process for recycling ethylene and propylene. Background technique: [0002] Olefins, especially light olefins (light olefins) such as ethylene and propylene, are required as raw materials for the production of higher olefins, polyethylene and polypropylene. The tube furnace cracking unit that uses naphtha as raw material to produce ethylene and propylene through steam cracking is currently the most important industrial production unit of ethylene and propylene. The cracked gas produced by cracking hydrocarbons is a mixture containing hydrogen, methane, ethane, ethylene, propane, propylene, mixed ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C11/04C07C11/06C07C7/11C10G3/00
CPCY02P30/40F25J3/0219F25J2230/30F25J2215/62F25J3/0252F25J2200/40F25J3/0242F25J2210/12F25J2270/60F25J3/0233F25J2205/04F25J2270/12F25J3/0238F25J2200/74F25J2270/04F25J2210/06
Inventor 熊献金
Owner CHINA PETROLEUM & CHEM CORP
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