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Condensation-type gas-liquid separation apparatus

A gas-liquid separation device and condensing technology, which is applied in the direction of separation method, dispersed particle separation, steam condensation, etc., can solve the problems that cannot meet the technical conditions of the wet complexation absorption method denitrification process, so as to improve the efficiency of gas-liquid separation and improve The effect of heat transfer efficiency

Inactive Publication Date: 2016-05-25
江西金林化工有限公司
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  • Description
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Problems solved by technology

[0009] The purpose of the present invention is to overcome the defect that ordinary gas-liquid separators cannot meet the technical conditions of the wet complexation absorption denitrification process, and provide a high-efficiency gas-liquid separation that is suitable for the wet complexation absorption denitrification process device

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  • Condensation-type gas-liquid separation apparatus
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Embodiment Construction

[0034] The present invention is further described below in conjunction with accompanying drawing.

[0035] refer to figure 1 , figure 2 with image 3 , a condensing type gas-liquid separation device is mainly composed of a lower head part 1, a tank body part 2, an upper head part 3, a diaphragm part, a flange pad one 27, a flange pad two 29, a flange pad Three 20, wire mesh bar part 11, fixed plate part 31, heat pipe heat exchanger part 19 are formed. The upper head part 3 is installed on the upper end of the tank part 2, the diaphragm part is installed on the lower end of the tank part 2, the lower head part 1 is installed on the lower end of the diaphragm part, and there is a porous plate 22 in the middle of the tank part 2, The porous plate 22 divides the inner cavity of the tank body part 2 into two parts. The inner cavity from the upper end surface of the porous plate 22 to the inner surface of the upper head part 3 is the upper cavity of the tank body, and the inner ...

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Abstract

The invention relates to a gas-liquid separation device, and more specifically discloses a condensation-type gas-liquid separation apparatus. The condensation-type gas-liquid separation apparatus is mainly composed of a lower shell cover part, a tank body part, an upper shell cover part, a transverse separating plate part, metal wire mesh strip parts, fixing plate parts, and heat pipe heat exchanger parts. When a refrigerant flows through a tank body upper chamber, heat energy of condensation sections of the heat pipe heat exchanger parts is absorbed by the refrigerant, so that the temperature of the condensation sections of the heat pipe heat exchanger parts is reduced; when a mixed gas flows through a tank body lower chamber, heat energy of the mixed gas is absorbed by the metal wire mesh strip parts, metal felt sleeves, and the condensation sections of the heat pipe heat exchanger parts together, so that gas in the mixed gas to be separated is changed into liquid drops via condensation, the liquid drops come together to become a condensate, and the condensate is discharged via a liquid outlet pipe; heat transfer efficiency is increased by the liquid drops absorbed by the metal felt sleeves, and the metal wire mesh strip parts take part in entire condensation and despumation processes of the mixed gas; reblending of a high concentration gas obtained via removing of the condensate with the mixed gas is not caused, so that gas liquid separation efficiency is increased.

Description

technical field [0001] The invention relates to a condensation type gas-liquid separation device, which relates to a gas-liquid separation device, in particular to a condensation type gas-liquid separation device which adopts a condensation method to separate gas that can be condensed into liquid droplets in a mixed gas. Background technique [0002] Wet complexation absorption method is a new research progress of flue gas denitrification technology. In 1993, under the funding of the U.S. Department of Energy, Benson et al. conducted a pilot study on simultaneous desulfurization and denitrification of Fe(II) EDTA at Dravo Lime Company. The absorbent was 6% magnesium oxide enhanced lime, with a desulfurization rate of 99% and a denitrification rate of 99%. Greater than 60%. [0003] The full name of Fe(Ⅱ)EDTA in Chinese is "ferrous ethylenediaminetetraacetate", which is a chelate compound. The nitrogen oxides in the flue gas are mainly NO. The Chinese name is "nitrogen mono...

Claims

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Application Information

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IPC IPC(8): B01D53/00B01D5/00
Inventor 赵晓东
Owner 江西金林化工有限公司
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