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Treatment method for alkali liquor oxidation regeneration tail gas containing mercaptide

A treatment method and technology for saline-alkali liquid, which are applied in chemical instruments and methods, separation methods, dispersed particle separation, etc., can solve the problems of substandard discharge, long process, pollute the environment, etc., and achieve recycling, simple and reliable process. Effect

Active Publication Date: 2015-05-20
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This type of organic sulfur belongs to the oil phase, which has high relative volatility and is relatively easy to enter the oxidation tail gas phase. If it is discharged directly or after incineration, the discharge will not meet the standard and cause serious environmental pollution.
[0003] Patent CN101940872B provides a water washing-membrane separation-oxidation lye oxidation regeneration tail gas desulfurization method. This method has a long process, and both membrane separation components and adsorbent consumption will lead to increased desulfurization costs.
Patent CN201210174207.1 invented a desulfurization device and method for waste gas containing disulfide, which can reduce disulfide to 200mg / Nm 3 , it is difficult to meet the requirements of future emission standards
Patent CN201110433220.X proposes a treatment and utilization method of oxidative desulfurization tail gas. The tail gas to be treated is absorbed by the absorbent of the desulfurization tower, and then goes to the adsorption tank to remove organic hydrocarbons after desulfurization. Since the adsorbent is replaced regularly, the absorption effect is unstable and replaced at the same time The final absorbent also presents new disposal problems

Method used

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  • Treatment method for alkali liquor oxidation regeneration tail gas containing mercaptide
  • Treatment method for alkali liquor oxidation regeneration tail gas containing mercaptide

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0015] like figure 1 As shown, the oxidative regeneration tail gas 1 containing mercaptan alkali solution to be treated enters from the bottom of the water washing tank (2), passes through the gas distribution plate 3, and exits from the top of the water washing tank after washing and removing alkali, enters the dehydration tank 4 from the bottom, passes through the desiccant 11 After drying and dehydration, it enters the supergravity separator 5, and after being fully contacted with the absorbent diesel oil 6, the exhaust gas enters the absorbed exhaust diesel oil separation and recovery tank 10, and after oil and gas separation, the exhaust gas 8 is purified and discharged up to the standard, and the absorbed rich diesel oil 7, 9 Sent to hydrogenation unit for desulfurization. The tail gas diesel oil separation and recovery tank 10 is filled with wire mesh or microsphere particles 12 .

Embodiment 2

[0017] like figure 2 As shown, the oxidative regeneration tail gas 1 containing mercaptan alkali solution to be treated enters from the bottom of the water washing tank 2, passes through the gas distribution plate 3, and exits from the top of the water washing tank after washing and removing alkali, enters the supergravity separator 5, and is mixed with the absorbent diesel oil 6 After full contact, the tail gas enters the absorbed tail gas diesel oil separation and recovery tank 10, and after oil and gas separation, the exhaust gas 8 is purified and discharged up to the standard, and the absorbed rich diesel oil 7, 9 is sent to the hydrogenation device for desulfurization.

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Abstract

The invention relates to a treatment method for an alkali liquor oxidation regeneration tail gas containing mercaptide. The treatment method comprises the following steps: feeding a to-be-treated alkali liquor oxidation regeneration tail gas containing mercaptide from the bottom of a washing tank, penetrating though a gas distribution plate in the tank, discharging from an exhaust gas pipe at the top of the washing tank, and feeding to an air inlet in the bottom of a dewatering tank; drying through a drying agent in the dewatering tank, feeding into a supergravity separator, contacting diesel oil fed from a liquid-phase inlet of the supergravity separator, and feeding into a gasoline and diesel oil separation recovery tank from a gas-phase outlet of the supergravity separator, wherein a crane of the supergravity separator is a rotary packing bed which is operated in a gas-liquid countercurrent, cocurrent flow or baffle flow form; and the operation ranges of the supergravity separator are as follows: the gas-liquid ratio is (5-2,000) to 1, the operation gage pressure is 0-0.3MPa and the operation temperature is 10-60 DEG C. According to the method, ultra-low sulphur emission of a liquefied gas alkali liquor oxidation regeneration tail gas is reached; desulfurization treatment can be carried out on absorbent diesel oil in a hydrogenation device; and the total sulfur emission in three wastes of factories is effectively reduced.

Description

technical field [0001] The invention belongs to the field of oil refining and chemical industry, and relates to a treatment method for oxidation regeneration tail gas of alkaline solution containing mercaptan. Background technique [0002] Since crude oil contains sulfides to varying degrees, during the refining process of crude oil, sulfur in different forms of light and heavy will enter the corresponding products according to the difference in boiling point. According to the characteristics of the distillation range of liquefied gas products, the sulfur form entering into it is mainly hydrogen sulfide , Methanethiol and Ethanthiol. At present, the demercaptan process of liquefied petroleum gas mainly adopts alkali washing. Under certain temperature, pressure and sufficient contact conditions, mercaptan contained in liquefied petroleum gas reacts with sodium hydroxide solution to form sodium mercaptide, which becomes inorganic sulfur and enters the alkali solution. , so as...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/14B01D53/26
Inventor 董卫刚高飞李玮李文琦周华群何涛波王苑李潇胡雪生白跃华
Owner PETROCHINA CO LTD
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