Method for vinyl chloride synthesis waste treatment and control

A technology of waste treatment and control method, applied in combustion product treatment, separation method, gas treatment and other directions, can solve problems such as affecting the absorption of falling film absorbers, affecting quality, polluting hydrochloric acid, etc., to meet environmental protection requirements and save operating costs , the effect of reducing poison

Active Publication Date: 2017-11-03
QINGDAO HAIWAN CHEM CO LTD
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  • Abstract
  • Description
  • Claims
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Problems solved by technology

[0003] In this process, since the quenching tower cools the flue gas tail gas by adding water, it cannot be guaranteed that the amount of water matches the amount of hydrogen chloride in the flue gas, so that only low-concentration hydrochloric acid (18%) can be produced; at the same time, in In the quench tower, the exchange of flue gas and cooling liquid is generally not sufficient, and the temperature is still high when leaving the quench tower, which also affects the absorption of the subsequent falling film absorber.
In addition, the incinerator itself and the waste heat boiler are made of steel and the heavy components contain iron. The high-temperature exhaust gas may bring iron ions to the absorption system, and it is difficult to ensure The products of complete combustion and incomplete combustion will pollute hydrochloric acid and affect its quality

Method used

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  • Method for vinyl chloride synthesis waste treatment and control

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Effect test

Embodiment 1

[0030] Such as figure 1 As shown, this embodiment provides a waste treatment device for vinyl chloride synthesis, including an incineration device, a quenching device 1 and a falling film absorption device 2. The incineration device incinerates waste to generate flue gas, and the flue gas passes through the quenching device 1 and enters the falling film absorption device. absorption in the device 2, and a cooling device 3 is provided between the quenching device 1 and the falling film absorption device 2.

[0031] At present, the waste produced after the synthesis of vinyl chloride is burned in the incineration device at a temperature above 1100°C to produce water vapor, carbon dioxide, hydrogen chloride, and a small amount of nitrogen oxides and chlorine gas. After passing through the waste heat device, the temperature drops to about 550°C. The quenching tower cools down, and at the same time, part of the hydrogen chloride gas and water vapor in the flue gas are absorbed by t...

Embodiment 2

[0048] Such as figure 1 As shown, the present embodiment is a further limitation of embodiment one. The quenching device 1 of the present embodiment is a quenching tower, and the quenching tower is provided with an acid liquid circulation line 7 for cooling the flue gas of combustion products, and the acid liquid circulation line One end of 7 is connected with the bottom of the quenching tower, and the other end is connected with the top of the quenching tower.

[0049] The general quenching tower cools the flue gas tail gas produced by the incinerator by adding water, so it cannot ensure that the amount of water matches the amount of hydrogen chloride in the flue gas, so only low-concentration hydrochloric acid can be produced, and its concentration is lower than 15%. The quench tower in this embodiment is provided with an acid liquid circulation pipeline 7 for cooling the flue gas of combustion products. The acid liquid circulation line 7 is provided with a circulation pump...

Embodiment 3

[0064] This embodiment is a further limitation of Embodiment 1 and Embodiment 2. This embodiment provides a waste treatment control method for vinyl chloride synthesis, which includes the following steps:

[0065] (1) Incineration: Incineration of waste after vinyl chloride synthesis produces high-temperature flue gas;

[0066] (2) Quenching: high-temperature flue gas enters the quenching tower and contacts with circulating acid liquid to cool down;

[0067] (3) Condensation: the cooled flue gas enters the condenser to cool down again;

[0068] (4) Absorption: The flue gas after cooling down again enters the falling film absorber for absorption, and the tail gas after absorption enters the alkali washing tower for treatment.

[0069] In step (1), the temperature of the high-temperature flue gas generated by incineration of waste is 1100°C-1200°C; the high-temperature flue gas passes through the waste heat furnace for heat exchange, and the temperature drops to 550°C-600°C, an...

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Abstract

The invention discloses a method for vinyl chloride synthesis waste treatment and control. High-temperature flue gas generated by waste incineration enters a quench tower and contacts with circulating acid fluid to be cooled; the cooled flue gas enters a condenser to be cooled again; the flue gas cooled once again enters a falling film absorber to be absorbed, and absorbed tail gas enters an alkaline tower to be treated. A waste treatment device can stably generate high-concentration and pure hydrochloric acid, the quality of the byproduct hydrochloric acid is ensured, the device can run by adopting different control methods according to different working conditions, the running cost can be reduced, and flue gas generated by incineration can also meet environmental protection requirements.

Description

technical field [0001] The invention belongs to the field of waste gas and liquid treatment, and in particular relates to a waste treatment control method for vinyl chloride synthesis. Background technique [0002] The main task of the incineration unit in the existing vinyl chloride (VCM) production and synthesis process is to incinerate the light and heavy component wastes produced by vinyl chloride (VCM), and also incinerate the exhaust gas from each process. These wastes are burned at a temperature above 1100°C to produce water vapor, carbon dioxide, hydrogen chloride, and of course a small amount of nitrogen oxides and chlorine gas. After the combustion products leave the incinerator, they pass through the waste heat boiler for heat exchange, and the temperature drops to 550°C. Then, water is used in the quenching tower. Absorb cooling. In the gas phase from the quench tower, there is still a small part of hydrogen chloride gas, which is absorbed in the falling film ab...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/78B01D53/68F23J15/00F23J15/04F23J15/06
CPCB01D53/002B01D53/1456B01D53/68B01D53/78B01D2257/2045B01D2257/80F23J15/006F23J15/04F23J15/06F23J2215/30Y02E20/30
Inventor 高自建郎需霞刘珍玉张清亮王凯纪业姜瑞霞
Owner QINGDAO HAIWAN CHEM CO LTD
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