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A method and device for recovering NO2 and SO2 in flue gas by rectification

A technology of SO2 and rectification, which is applied in the field of rectification to recover NO2 and SO2 in flue gas, which can solve the problems of low income, high concentration of main components in rectification, and high cost

Active Publication Date: 2020-04-10
UNIV OF SCI & TECH BEIJING
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Therefore, in terms of cryogenic gas distillation, there is currently no NO 2 and SO 2 In terms of flue gas pollutant treatment, the main idea of ​​existing flue gas resource utilization is transformation and removal rather than recovery. For example, SCR denitrification removes NO by spraying ammonia X react to N 2 and H 2 0, to achieve pollution-free treatment, but can not recover NO X Resources; the calcium method, magnesium method, sodium method, ammonia method and organic alkali method of FGD flue gas desulfurization technology are also converted into corresponding sulfates and sulfites by adding other substances, and converted from gas resources to solid resources, but low yield and high cost
[0005] In addition, there are the following technical problems in the prior art: (1) The separation of gases in the current rectification tower is mainly to separate some common gases such as air, hydrocarbon gas, natural gas to remove acid gas, and to separate isotopes, etc., and there are almost no rectification towers that can deal with NO 2 and SO 2 This acidic corrosive gas system; (2) The current low-temperature rectification is either pure low-pressure rectification such as air separation, or pure high-pressure rectification such as natural gas removal of CO 2 , the requirements for the component concentration of the feed gas are relatively high, and generally require a high concentration of the main components of the rectification; (3) Most of the current low-temperature rectification devices are continuous rectification, with continuous feed and output

Method used

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  • A method and device for recovering NO2 and SO2 in flue gas by rectification
  • A method and device for recovering NO2 and SO2 in flue gas by rectification

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0083] This embodiment proposes a rectification recovery of NO in flue gas 2 and SO 2 devices such as figure 1 As shown, the device includes:

[0084] A cooling heat exchanger for precooling high-temperature flue gas;

[0085] a first rectification column for high-pressure rectification;

[0086] One is used for the second rectification tower of atmospheric rectification;

[0087] a SO 2 liquid storage tank;

[0088] The cooling heat exchanger, the first rectification tower, the second rectification tower and the SO 2 The liquid storage tanks are connected in turn, and the SO 2 The liquid storage tank is connected with the condenser of the second rectification column.

[0089] The device also includes:

[0090] A gas storage tank for storing the tail gas obtained after treatment in the first rectification tower and the tail gas obtained after treatment in the second rectification tower for circulation and separation;

[0091] A gas mixing tank for mixing the gas in t...

Embodiment 2

[0135] A rectification recovery of NO in the flue gas proposed in this embodiment 2 and SO 2 The device is basically the same as in Example 1, except that:

[0136] The specific data of the test are: the inlet flow rate of high-temperature mixed gas (simulated flue gas) is 5L / miI, and the mixed gas component is NO 2 / SO 2 / CO 2 =21.6% / 61.1% / 17.3%, compressor outlet pressure 1.5bar, condenser condensing temperature 0°C; first rectification column pressure 1.1bar, reflux ratio 1.28, theoretical plate number 27, feed plate number 13; The pressure of the second rectifying column is 1.05 bar, the reflux ratio is 3.78, the number of theoretical plates is 7, and the number of feed plates is 3.

[0137] After steady state distillation, NO 2 and SO 2 The purities are 0.999 (volume fraction) and 0.99 (volume fraction) respectively.

Embodiment 3

[0139] This embodiment proposes a rectification recovery of NO in flue gas 2 and SO 2 method, such as figure 2 As shown, the method adopts the device described in Embodiment 1, and the method comprises the steps of:

[0140] Step 1, pressurizing and cooling the high-temperature flue gas to cool the high-temperature flue gas to 0-20°C;

[0141] Step 2, the flue gas cooled in step 1 enters the first rectification tower for one-stage high-pressure rectification, and the NO of heavy components 2 and SO 2 After the mixed liquid is condensed, it enters the tower kettle, and the light component gas is distilled from the top of the tower;

[0142] The light gases include N 2 , CO 2 and NO;

[0143] Step 3, the mixed liquid that enters the tower kettle in step 2 is pumped into the second rectification tower by a metering pump, and the atmospheric pressure rectification separates NO 2 and SO 2 , the tower kettle gets high-purity NO 2 , high-purity SO is obtained at the top of...

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Abstract

The invention mainly belongs to the field of rectification and separation of low-temperature chemical gas, and particularly relates to a method and device for rectifying and recovering NO2 and SO2 influe gas. The method combines a high-pressure rectification operation process and a low-pressure rectification operation process, high-pressure rectification of a first rectification tower can reducea relatively low boiling point caused by relatively low partial pressure of NO2 and SO2, and normal-pressure rectification of a second rectification tower ensures the relatively low separation difficulty of NO2 and SO2; by using the semi-continuous rectification method, the liquid holdup in the tower bottom of a first rectification column reaches 50-90%, then liquid enters the second rectificationtower for rectification, and the second rectification tower is controlled well; and meanwhile, the device has an anti-corrosion function.

Description

technical field [0001] The invention mainly belongs to the field of rectification and separation of low-temperature chemical gas, and specifically relates to a rectification recovery of NO in flue gas. 2 and SO 2 methods and devices. Background technique [0002] my country is a big coal-burning country in the world. Coal accounts for about 75% of my country's energy. Coal-burning can produce a lot of NO X and SO 2 . Currently SO 2 The treatment mainly includes three categories: wet method, semi-dry method and dry method. In recent years, electron beam flue gas desulfurization technology, pulse corona discharge flue gas desulfurization technology, membrane absorption method, microbial desulfurization technology, etc. have been developed. But they are all in the experimental stage. At present, flue gas denitrification technologies are mainly put into production, such as selective catalytic reduction (SCR), selective non-catalytic reduction (SNCR), and SNCR-SCR combined ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): F25J3/02
Inventor 刘应书李子宜孙宁起杨雄彭兆丰邢奕吴倩倩刘文海田京雷
Owner UNIV OF SCI & TECH BEIJING