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A catalyst flue gas washing wastewater resource treatment method and system

A treatment method and catalyst technology, applied in the field of water treatment, can solve problems such as high cost and complex components, and achieve the effects of rapid and thorough removal, low operating cost, and significant economic and environmental benefits.

Active Publication Date: 2022-03-04
DATANG ENVIRONMENT IND GRP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] Because the actually produced ammonium sulfate wastewater not only contains a large amount of ammonium sulfate, but also has a variety of heavy metals and other pollutants, especially the composition of the regenerated catalyst gas is more complex, and the concentration of nickel, chromium, fluoride, cyanide, etc. in the generated washing wastewater Higher, the concentration far exceeds the discharge standard. If it is not treated, it can only be disposed of as hazardous waste, and the cost is huge. At the same time, a large amount of ammonia nitrogen contained in the wastewater is itself a resource, so a low-cost, high-efficiency standard treatment of washing wastewater has been developed. technology, and recover resources in wastewater as much as possible, which has important environmental and economic benefits

Method used

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  • A catalyst flue gas washing wastewater resource treatment method and system
  • A catalyst flue gas washing wastewater resource treatment method and system
  • A catalyst flue gas washing wastewater resource treatment method and system

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037] In this example, the actual waste water (referred to as raw water) for flue gas washing of a certain catalyst is treated. The quality of the raw water is shown in Table 1. The treatment method is as follows:

[0038] 1. Restoration

[0039] Send the raw water to the closed reactor, add sulfuric acid solution into the reactor, adjust the pH value of the raw water to 4, and add the reducing agent sodium sulfite to carry out the reduction reaction at the same time, the amount of sodium sulfite added is twice the theoretical value, and the reaction temperature is 25 °C , and the reaction time was 45 minutes.

[0040] 2. Alkali treatment

[0041] Send the effluent of the above reduction reaction to a closed base adjustment system, add lime milk with a mass concentration of 3% to the base adjustment system, adjust the pH value of the reduction reaction effluent to 12, and react for 30 minutes.

[0042] 3. Decalcification, flocculation and precipitation

[0043] Send the ef...

Embodiment 2

[0054] In this embodiment, except that the oxidation treatment steps are different, all the other are basically the same as in Example 1, and the oxidation treatment steps in the present embodiment are as follows:

[0055] Send the effluent from the membrane absorption treatment to the closed oxidation system, at a molar ratio of CN - : ClO - :H 2 o 2 Sodium hypochlorite and hydrogen peroxide were added in an amount of 1:2:1.2 for oxidation treatment. The oxidation treatment time was 30 minutes. After the oxidation treatment, the pH value was adjusted back to 7 to obtain treated effluent.

[0056] The results show that: after being treated by the method of this embodiment, the heavy metals, cyanide, fluoride, ammonia nitrogen, etc. in the waste water all reach the national first-class discharge standard, the cyanide content is 0.1mg / L, and the inorganic fluoride content is 4mg / L , In addition, chromium, Hg, Pb, As, etc. are not detected, the quality of the treated water is ...

Embodiment 3

[0058] In this example, the actual waste water (referred to as raw water) for flue gas washing of a certain catalyst is treated. The quality of the raw water is shown in Table 2. The treatment method is as follows:

[0059] 1. Restoration

[0060] Send the raw water to the closed reactor, add sulfuric acid solution into the reactor, adjust the pH value of the raw water to 3, and add the reducing agent sodium sulfite to carry out the reduction reaction at the same time, the amount of sodium sulfite added is twice the theoretical value, and the reaction temperature is 25 °C , and the reaction time was 45 minutes.

[0061] 2. Alkali treatment

[0062] Send the effluent of the above reduction reaction to the closed alkali adjustment system, first add milk of lime with a mass content of 3% to the alkali adjustment system, the amount of lime milk added is 10000mg / L, and then add mass The content is 10% sodium hydroxide solution, the pH value of the water from the reduction reactio...

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Abstract

The invention provides a catalyst flue gas washing wastewater resource treatment method and system. The method of the present invention comprises the following steps: S1: adjust the pH value of the catalyst flue gas washing wastewater to 3-4 and then perform reduction treatment; S2: use alkali to adjust the pH value of the reduction treatment effluent to above 12 and perform alkali treatment; S3: Add carbonate to the alkali treatment effluent for reaction, and flocculate and precipitate the reaction effluent; S4: Send the flocculated and precipitated effluent to the membrane absorption system for membrane absorption treatment, and recover ammonia nitrogen; S5: Oxidize the membrane absorption treatment effluent, oxidize The treatment is double oxidation treatment with hypochlorite or oxidation treatment with hypochlorite and hydrogen peroxide. The method and system of the present invention can not only efficiently remove heavy metals, fluorides and cyanides in wastewater, but also recover ammonia nitrogen to realize resource utilization, and has the advantages of low operating cost, significant economic and environmental benefits, and the like.

Description

technical field [0001] The invention relates to the technical field of water treatment, in particular to a resource treatment method and system for catalyst flue gas washing wastewater. Background technique [0002] In my country's coal-fired power plants, SCR flue gas denitrification technology is the most widely used, so a large amount of denitrification catalysts are consumed every year. In the production process of SCR denitrification catalyst, ammonia-containing exhaust gas and dust will be generated in the coating drying and calcination process. These exhaust gases will enter the sulfuric acid neutralization scrubber through the exhaust gas collection system for treatment, thereby producing ammonium sulfate wastewater. [0003] Because the actually produced ammonium sulfate wastewater not only contains a large amount of ammonium sulfate, but also has a variety of heavy metals and other pollutants, especially the composition of the regenerated catalyst gas is more compl...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F9/04C02F103/18C02F101/22C02F101/20C02F101/18C02F101/16C02F101/14
CPCC02F9/00C02F1/66C02F1/76C02F1/722C02F1/70C02F1/5236C02F1/56C02F1/44C02F2103/18C02F2101/20C02F2101/22C02F2101/16C02F2101/14C02F2101/18
Inventor 刘海洋王彦文曹书涛谷小兵白玉勇荆亚超杨言高阳李飞麻晓越彭思伟
Owner DATANG ENVIRONMENT IND GRP