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Process method for drying cracking gas

A process method and cracking gas technology, applied in the field of cracking gas drying, to achieve the effects of saving production costs, reasonable drying and purification process, and improving purity

Inactive Publication Date: 2016-06-29
SHENYANG PARAFFIN CHEM
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  • Abstract
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  • Claims
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Problems solved by technology

[0003] The purpose of the present invention is to provide a process for cracking gas drying in the production process of catalytic thermal cracking to ethylene, so as to solve the problem of cracking gas drying and purification in catalytic thermal cracking ethylene production

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  • Process method for drying cracking gas

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Embodiment Construction

[0013] according to figure 1 The specific situation of the present invention will be described in detail.

[0014] Specific process operation steps: cracked gas GI comes from the upstream unit, first enters the dryer separation tank (V-4445) for gas-liquid separation, after separation, the liquid phase hydrocarbon is sent to the gas unit for subsequent processing, and the cracked gas GI continues to move forward from The upper part flows into the cracked gas first dryer (D-4450A / B). The first dryer of cracked gas uses 3A molecular sieve desiccant to remove moisture. After drying, the cracked gas GI is supplied to the depropanizer (T-4460) as feed, and after removing propane and heavy components below C4 from the bottom of the tower, components such as propylene, ethylene, ethane, acetylene, and methane at the top of the tower enter The cracked gas compressor (C-4400) has 4 sections. The compressed cracked gas GI enters the feed tank of the cracked gas secondary dryer (V-4447...

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Abstract

A process method for drying cracking gas is provided; the cracking gas passes through a dryer separation tank and then enters a first dryer from the top of the first dryer, wherein the dryer adopts a 3A molecular sieve drying agent to remove moisture; the cracking gas after drying is supplied to a depropanization tower, propane and heavy components with the carbon number of 4 or less are removed from the tower bottom, and propylene, ethylene, ethane, acetylene and methane light components of the tower top enter a compressor section 4 and then enter a second-stage dryer feed tank; cracking gas coming out of the top of the second-stage dryer feed tank flows into a reactor to remove COS, sulfur alcohol, ammonia, H2S and CO2 impurities, and then enters a dearsenication reactor; a dearsenication agent and a catalyst in the dearsenication reactor remove arsenic and mercury impurities, and the cracking gas after treatment enters an acetylene hydrogenation reactor, next enters a second dryer, is dried, and then enters a separation system. The problems of poor drying and purification effects of cracking gas produced by a conventional device for preparing ethylene through catalytic thermal cracking are solved, freezing and blocking of the cryogenic separation system of a CPP device subsequent unit can be effectively prevented, and the economic benefits are improved.

Description

technical field [0001] The invention relates to the technical field of petrochemical technology, in particular to a process method for drying cracked gas in the production process of ethylene production by catalytic thermal cracking. Background technique [0002] Catalytic thermal cracking ethylene unit is a production unit that produces ethylene and propylene from atmospheric residual oil. The cracked gas produced in the production process is a mixed gas, including fuel gas, ethylene, propylene, carbon four, etc., in addition to a certain amount of impurities such as acid gas, tribute, nitrides, water, etc. A series of drying and purification treatments can separate it into qualified fuel gas, ethylene, propylene, carbon four and other products. Ethylene is an important basic raw material of organic chemical industry and the most basic raw material of petrochemical industry. According to the statistics of relevant departments, ethylene products account for more than 75% of...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10K1/00C10K1/32C10K1/34
Inventor 洪华姜立辉窦春光王明伟孙章谢毅
Owner SHENYANG PARAFFIN CHEM
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