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A Method for Efficiently Removing Chemical Oxygen Demand in Pulping Wastewater

A chemical oxygen demand, pulping wastewater technology, applied in chemical instruments and methods, processing wastewater treatment, water pollutants and other directions, can solve no help; Liu Xiyang et al (patent application number, Fenton dosage cannot be effectively reduced , unfavorable business operation control and other problems, to achieve the effect of improving complicated steps, saving equipment investment and low cost

Active Publication Date: 2019-11-08
广东鼎丰纸业有限公司
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AI Technical Summary

Problems solved by technology

[0004] In the design of Fenton reactor for treating pulping wastewater, fluidized bed system is often used. After vigorous stirring, Fenton agent and wastewater are fully mixed to improve the oxidation efficiency of Fenton reaction, but the power consumption is relatively large.
[0005] In order to improve the oxidation efficiency of Fenton, an auxiliary unit can be added before or after the Fenton fluidized bed. For example, Tian Binghui et al. (patent application number: 201101021014.X) invented "a catalytic oxidation-composite flocculation integrated wastewater treatment process" , add a catalytic oxygen tank before the Fenton oxidation reaction tank to improve the oxidation efficiency of the Fenton reaction, and achieve better results for the treatment of chemical industry wastewater, but it is necessary to add another catalytic oxidation reaction tank; Wu Xiaoyi et al. (patent application No.: 201610789935.1) A method to improve the COD degradation efficiency and biochemical performance of wastewater. The wastewater undergoes steps such as Fenton oxidation, ozone oxidation, and electrocatalytic oxidation to obtain a better COD removal rate for ultra-high concentration wastewater, but the treatment After the wastewater COD is still very high; Wang Xiaojun et al. (patent application number: 200710027102.2) invented the "Fenton and air flotation integrated water treatment method", adding an air flotation device after the Fenton oxidation reaction tank to replace the general flocculation sedimentation tank , can improve the flocculation efficiency after the Fenton reaction, but it is not helpful to improve the Fenton reaction efficiency and reduce the dosage of drugs; Liu Xiyang et al. (patent application number: 201510954688.1) invented "A method for treating dye production wastewater by using magnesium oxide coagulation combined with Fenton oxidation" , Before the Fenton oxidation reaction, flocculate with magnesium oxide at pH 12, and then perform Fenton reaction on the treated wastewater, which has a certain effect on dye production wastewater
[0006] Such methods have a certain effect on wastewater treatment, but they are more or less complex in process and cumbersome in operation, and require multiple sets of independent equipment to operate in series, which consumes a lot of energy and occupies a large space, which is not conducive to the operation control and operation of enterprises. Fenton dosage can not be effectively reduced and other problems

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] Take 1000ml of biochemical wastewater treated with microbial aerobic aeration and with a COD of 278ppm, and test in 2 groups: Group A: Add flocculant [polymeric ferric sulfate (11% total iron, 10% basicity)] 0.6ml, 0.1 % cationic polyacrylamide 2ml, the system was stirred for 2 min under the condition of pH 5, and then Fenton reagent (6.5% Fe 2+ 1.16ml of ferrous sulfate, 0.20ml of 27.5% hydrogen peroxide), stir for 1min, let stand for 15min, then add liquid caustic soda to the standing wastewater to adjust the pH to 6-9, add anionic polyacrylamide for flocculation and sedimentation, and discharge after treatment. The COD is 42ppm, the COD removal rate is 84.9%, and it meets the requirements of the national GB3544-2008 "Water Pollutant Discharge Standard for Pulp and Paper Industry" on the discharge limit of 100ppm for pulping enterprises and 80ppm for papermaking enterprises; Group B: no flocculant is added, Directly add an equal amount of Fenton's reagent (6.5% Fe 2+...

Embodiment 2

[0032] Take 1000ml of biochemical wastewater treated by microbial aerobic aeration with a COD of 290ppm, and divide it into 2 groups for testing: Group A, add flocculant [polymeric ferric sulfate (11% of total iron, 10% of salinity) 0.6ml, 0.1% cationic polymer Acrylamide 2ml], the system was stirred for 5min under the condition of pH 5, and then Fenton reagent (6.5% Fe 2+ 1.16ml of ferrous sulfate, 0.20ml of 27.5% hydrogen peroxide), stir for 5min, let stand for 15min, then add slaked lime to the standing wastewater to adjust the pH to 6-9, add anionic polyacrylamide for flocculation and sedimentation, and then discharge, the treated wastewater COD It is 42ppm, and the COD removal rate is 87.9%, and it meets the requirements of the national GB3544-2008 "Water Pollutant Discharge Standard for Pulp and Paper Industry" on the discharge limit of 100ppm for pulping enterprises and 80ppm for papermaking enterprises; Group B: no flocculant, direct Add Fenton's reagent (6.5% Fe 2+ 1...

Embodiment 3

[0034] Take 1000ml of biochemical wastewater with a COD of 189ppm after microbial aerobic aeration treatment, add flocculant [polymeric ferric sulfate (11% total iron, 10% basicity) 0.4ml, 0.1% cationic polyacrylamide 2ml], the system is in The reaction was stirred at pH 6 for 5 min, and then Fenton reagent (6.5% Fe 2+1.16ml of ferrous sulfate, 0.05ml of 27.5% hydrogen peroxide), stir for 1min, let stand for 20min, then add slaked lime to the treated wastewater to adjust the pH to 6-9, add anionic polyacrylamide for flocculation and sedimentation, and discharge after treatment. The COD of the wastewater is 71ppm, the COD removal rate is 62.4%, and it meets the requirements of the national GB3544-2008 "Water Pollutant Discharge Standard for Pulp and Paper Industry" on the discharge limit of 100ppm for pulping enterprises and 80ppm for papermaking enterprises, and then adds 27.5% hydrogen peroxide 0.15 ml, stirring at a speed of 150r / min for 2min under the condition of pH 4, and...

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Abstract

The invention provides a method for efficiently removing chemical oxygen demand of pulping wastewater, comprising the following steps: (1) sequentially adding an acidic inorganic polymer flocculant and an organic polymer flocculant to the wastewater, controlling the pH of a reaction system between 5 to 7 during the adding process, and stirring fully for a short time to complete flocculation; (2) adding Fenton agent to the flocculated wastewater in the same container, controlling the pH of the reaction system between 3 to 5 during the adding process, stirring fully for a short time, mixing themedicinal liquid evenly, and standing for reaction; and (3) adjusting the pH of the reacted wastewater, adding a small amount of high-molecular flocculant for turbidity separation and discharging. According to the invention, a flocculation method and the Fenton oxidation method are used in the same container for improving the complexity of the existing Fenton flocculation auxiliary unit and the Fenton oxidation process combination, saving equipment investment, improving reaction efficiency, and effectively removing organic matter content and chemical oxygen demand in wastewater.

Description

technical field [0001] The invention relates to the technical field of wastewater treatment, in particular to a method for efficiently removing chemical oxygen demand from pulping wastewater. Background technique [0002] Due to the complex composition of pulping wastewater, high pollutant load, and high content of water-soluble lignin that is difficult to decompose by biology, it is one of the main pollution sources of water bodies. At present, the more common wastewater treatment process generally adopts the first-level physical precipitation, the second-level biochemical treatment, and the third-level Fenton advanced oxidation process. [0003] The essence of the Fenton oxidation reaction is a chain reaction in which hydrogen peroxide is decomposed to generate hydroxyl radicals with high oxidative activity through ferrous ions. Wastewater with high COD and difficult biochemical degradation. [0004] In the design of the Fenton reactor for pulping wastewater treatment, a...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F9/04C02F103/28C02F101/30
CPCC02F1/5245C02F1/56C02F1/722C02F2101/30C02F2103/28C02F2209/06C02F2209/08C02F2305/026
Inventor 王在梅秦昀昌
Owner 广东鼎丰纸业有限公司
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