发明名称 |
SEPARATION AND PURIFICATION OF THERMALLY CRACKED GAS OF HYDROCARBON |
摘要 |
PURPOSE:To eliminate the necessity or memarkably reduce of the amount of a refrigerant, by using, a stream of a gas-liquid mixed phase formed by depressurizing and expanding ethylene . ethane fraction separated in a demethanization step as a refrigerant, compressing the stream and introducing the compressed stream into an ethylene separation step. CONSTITUTION:A thermal cracked gas of a hydrocarbon is cooled in a cooling step 1 and part or all of the resultant condensate is fed to a demethanization step 2. Bottom liquid consisting essentially of ethylene . ethane from a demethanization column (T-1) is fed to plural expanders (V-1)-(V-3), depressurized and expanded to a pressure below the operating pressure in the ethylene separation step to provide a gas-liquid mixed phase stream at a low temperature, normally -80--90 deg.C. The above-mentioned mixed phase stream is then fed to heat exchangers (E-2)-(E-4) for cooling in the cooling step 1 and used until the stream becomes saturated vapor or superheated vapor. The resultant vapor is then compressed in a compressor (C-1) to the operating pressure abnd then introduced into the ethylene separation step 4.
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申请公布号 |
JPS63156732(A) |
申请公布日期 |
1988.06.29 |
申请号 |
JP19860303199 |
申请日期 |
1986.12.19 |
申请人 |
MITSUI ENG & SHIPBUILD CO LTD;MITSUI PETROCHEM IND LTD |
发明人 |
SAITOU OKIYA;OGURA YOSHIO;IWATA RYUICHI;YOSHIDA MASAHIKO;KITAYAMA YUTAKA |
分类号 |
C07C7/04;C07C1/00;C07C9/04;C07C9/06;C07C11/04;C07C67/00 |
主分类号 |
C07C7/04 |
代理机构 |
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代理人 |
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主权项 |
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地址 |
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