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Rich oil de-benzene process

An oil-rich and debenzene technology is applied in the field of distillation and de-benzene of the rich oil from the final cold-washing benzene section of a coking enterprise, which can solve the problems of environmental pollution, consumption of steam resources, and difficulty in handling crude benzene separation water, etc. Productivity, the effect of saving steam resources

Active Publication Date: 2012-05-23
JIGANG INT ENG & TECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In the production process, since steam is used as the heat source of distillation, a large amount of difficult-to-handle crude benzene separation water will be produced, which not only consumes precious steam resources, but also easily causes serious environmental pollution. far from

Method used

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  • Rich oil de-benzene process
  • Rich oil de-benzene process

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Embodiment Construction

[0013] A kind of oil-rich debenzene process step of the present invention is as follows:

[0014] The rich oil sent from the final cooling and washing benzene section is sent to the oil-gas heat exchanger 8, and the heat-exchanged rich oil enters the lean-rich oil heat exchanger 11 for heat exchange, and the rich oil temperature reaches about 160-180°C and then enters the debenzene tower Tube furnace 2, debenzene tower Tube furnace 2 further heats the oil-rich temperature to 190-200°C and then sends it to debenzene tower 1 for distillation and debenzene removal; light benzene, refined heavy benzene and The naphthalene oil is extracted from the top and side line of the debenzene tower 1 respectively, and the rich oil debenzene becomes lean oil and then enters the debenzene tower 1 tower kettle, and the first part of the lean oil in the tower kettle enters the debenzene tower tubular furnace 2 for heating , after heating, send back to the debenzene tower 1 from the top of the to...

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Abstract

The invention discloses a rich oil de-benzene process, comprising the following steps: the rich oil from the final cooling benzol scrubbing unit is sent into a gas and oil exchanger to heat, then the oil is sent into a heat exchanger between lean oil and rich-oil to heat; the rich oil is heated to 160-180 DEG C and introduced to a de-benzene pipe tower type furnace to further heat to 190-200 DEG C, then the oil is sent to a de-benzene tower to remove benzene by distillation; the light benzene, fine heavy benzene and naphthalene oil produced by distillation de-benzene are extracted respectively from the overhead and side line of the de-benzene tower; after removing benzene, the rich oil is converted to lean oil and then sent to the tower pot; the first part of the lean oil in the tower potis sent to the de-benzene pipe tower type furnace to heat and then sent back to the de-benzene tower from the upside of the tower pot of the de-benzene tower to provide energy for the distillation ofrich oil; the second part of lean oil in the tower pot flows through the heat exchanger between lean oil and rich-oil, lean oil first chiller and lean oil second chiller to cool to 25-30 DEG C, and then the lean oil is sent back to the final cooling benzol scrubbing unit to recycle. The process can meet the demand of the final cooling benzol scrubbing recycling, has no out-emission of exhaust gasand waste water, simpler procedures, environmental friendliness and higher de-benzene rate.

Description

technical field [0001] The present invention relates to a technology for distilling and removing benzene from rich oil from the final cold washing benzene section in a coking enterprise, to be exact, a technology for removing benzene from rich oil Background technique [0002] At present, the final cold washing benzene section of domestic coking plants uses tar washing oil or petroleum washing oil to wash the benzene in the gas. The washing oil absorbs benzene and becomes rich oil. Oil. In order to ensure the recycling of the washing oil, the benzene in the rich oil must be removed to turn it into a lean oil that can be sent to the final cold washing benzene section for further benzene washing. Various existing processes use steam blowing to remove crude benzene in rich oil, and use single-tower process or double-tower process under normal pressure to obtain one kind of benzene, two kinds of benzene or three products . In the production process, since steam is used as the...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G53/02
Inventor 温燕明汤志刚刘同清刘卫国罗时政蒋升华于民桂玉明贺西娟王蕾周长华
Owner JIGANG INT ENG & TECH CO LTD
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