Technology for reclaiming hydrogen chloride tail gas in chemical production

A process technology, chemical production technology, applied in chemical instruments and methods, dispersed particle separation, separation methods, etc., can solve problems such as unfavorable industrialized continuous production, waste of time, waste of energy and environmental pollution, and achieve complete recovery and high-efficiency. The effect of added value utilization, improving economic efficiency and saving water resources

Inactive Publication Date: 2010-02-17
北京格瑞华阳科技发展有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] Can see by comprehensive analysis, existing hydrogen chloride tail gas recovery process mainly has the shortcoming of following four aspects: 1) dilute hydrochloric acid is transferred from an absorption tower to another absorption tower to absorb hydrogen chloride to produce concentrated hydrochloric acid with circulation pump, The transfer amount of dilute hydrochloric acid is very big like this, especially in the second case transfer needs long time, is unfavorable for suitability for industrialized continuous production, promptly wasted time, wasted energy and polluted environment again; The method of using the generated negative pressure to suck the hydrogen chloride tail gas not only needs a large amount of absorbent, but also when water or dilute hydrochloric acid is used as the absorbent, the hydrogen chloride gas is very weak during the high-speed jet movement. Difficult to contact with water or dilute hydrochloric acid in all directions, resulting in slow dissolution of hydrogen chloride gas and poor absorption of hydrogen chloride tail gas. In addition, the jet pump method is not suitable for absorbents with high vapor pressure, such as ethanol, etc. , easy to volatilize and generate mist, and the vacuum produced is small, so the amount of hydrogen chloride gas sucked is also small; 3) in the case of the hydrogen chloride waste gas treatment system shown in the first example ( figure 1 ), there are two unfavorable factors, one is to use the aqueous solution containing high concentration hydrogen chloride as the water absorbent of the last hydrogen chloride gas (wherein the hydrogen chloride content is very low), its absorption effect to the hydrogen chloride tail gas will be very poor, because when When the concentration of hydrochloric acid in the aqueous solution reaches near saturation, the ability to absorb hydrogen chloride will decrease, especially when the concentration of hydrogen chloride tail gas is relatively small, its absorption effect will be even worse. In fact, according to the principle of gas-liquid absorption equilibrium, it

Method used

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  • Technology for reclaiming hydrogen chloride tail gas in chemical production
  • Technology for reclaiming hydrogen chloride tail gas in chemical production
  • Technology for reclaiming hydrogen chloride tail gas in chemical production

Examples

Experimental program
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Example Embodiment

[0008] Example 1:

[0009] Attach absorption towers 1, 2 and 3 (see image 3 ) Load 1 / 2 tower height of deionized water absorbent, load industrial ammonia water into the lower part of the neutralization tower, close check valves 1 and 2, adjust the four-way valve to make the fan 1 communicate with the absorption tower 1, from the absorption tower The outer layer (or inner cooling pipe), along the direction of absorption tower 1-absorption tower 2-absorption tower 3-neutralization tower, is supplied with coolant to control the temperature of the absorbent in the absorption tower to be less than 20 ℃, and hydrogen chloride produced in industry After the exhaust gas passes through the cooler and the dryer (the current dryer does not need to install desiccant), the fan 1 enters the absorption tower 1 through the four-way valve. After the hydrogen chloride gas passes through the sand core plate, a lot of gradually rising water is formed in the water The tiny bubbles of hydrogen chlor...

Example Embodiment

[0010] Example 2:

[0011] When the concentration of hydrogen chloride from tower 1 reaches 38%, adjust the four-way valve, connect absorption tower 2 and fan 1, open fan 2 and check valve 1, close fan 3 and check valve 3, and set the absorption tower After the hydrochloric acid in 1 is put into the concentrated hydrochloric acid storage tank, add deionized water absorbent, so that the way for hydrogen chloride gas to be absorbed: absorption tower 2-absorption tower 3-absorption tower 1-neutralization tower is opened. The process of absorbing hydrogen chloride continues until the concentration of hydrogen chloride in the absorbent water is sampled and checked from the tower 2 to reach 38%.

Example Embodiment

[0012] Example 3:

[0013] When the concentration of hydrogen chloride sampled from tower 2 reaches 38%, adjust the four-way valve, connect absorption tower 3 to fan 1, open fan 3 and check valve 2, close fan 4, and release the hydrochloric acid in absorption tower 2 After the concentrated hydrochloric acid storage tank, add deionized water absorbent, so that the way for hydrogen chloride gas to be absorbed: absorption tower 3-absorption tower 1-absorption tower 2-neutralization tower is opened. The process of absorbing hydrogen chloride continues until the concentration of hydrogen chloride in the absorbent water is sampled from the tower 3 to reach 38%.

[0014] In Example 1, the way that hydrogen chloride gas is absorbed is: absorption tower 1-absorption tower 2-absorption tower 3-neutralization tower. In Example 2 the way that hydrogen chloride gas is absorbed is: absorption tower 2-absorption tower 3 Absorption tower 1-neutralization tower, the way in which hydrogen chloride ...

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Abstract

The invention discloses technology for reclaiming hydrogen chloride tail gas in chemical production, which overcomes the defects of large transfer amount of absorbent between absorption towers, disadvantage of industrialized continuous production, poor effect of absorbing the hydrogen chloride tail gas, waste of time, energy and water resources, environment pollution, low byproduct gains and the like in the prior process for reclaiming the hydrogen chloride tail gas. The technology (attached drawing) achieves simple hydrogen chloride reclaiming process operation, low engineering manufacturingcost, little energy consumption, little industrial water, high hydrogen chloride reclaiming efficiency, high byproduct gains, environmental protection and advantage of industrialized continuous production by optimizing and combining exchange circulating technology in hydrogen chloride absorption sequence through a bubble absorption tower, technology for controlling the tower temperature to between10 and 30 DEG C according to the order of sequence, technology for matching and using dryer and deionized water and hydrogen chloride absorbent such as anhydrous ethanol, absolute alcohol and the like and series of technology for separating a neutralized product and a neutralizer such as volatile alkali ammonia water, pyridine and the like.

Description

1. Technical field [0001] This patent belongs to the field of fine chemical technology and relates to the recovery process technology of hydrogen chloride tail gas in chemical production. 2. Background technology [0002] At present, the recovery technology of hydrogen chloride tail gas in industry mainly adopts jet pump. The main working principle of the jet pump is to use water to spray out at a certain speed in the jet pump, and the jet flow forms a certain negative pressure in the jet pump, and the negative pressure sucks the hydrogen chloride gas to be treated to travel and contact with the jetted water. . During the contact process between water and hydrogen chloride gas, hydrogen chloride is dissolved in water to achieve the purpose of hydrogen chloride tail gas recovery. Two examples are given below to illustrate the current status of hydrogen chloride tail gas recovery technology. see the first example figure 1 , which is a flow chart of the treatment system for...

Claims

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Application Information

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IPC IPC(8): B01D53/18B01D53/68
Inventor 陈洁华
Owner 北京格瑞华阳科技发展有限公司
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