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Composite flocculant for quick treatment of coke quenching wastewater and use method thereof

A coagulant and wastewater technology, which is applied in water/sewage treatment, natural water treatment, neutralized water/sewage treatment, etc. It can solve the problems of high system operation risk, high toxicity and long processing time.

Inactive Publication Date: 2018-12-21
上海优帛环境技术有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0009] The main problems of the coke quenching wastewater used in the wet coke quenching process of coking enterprises are complex water quality, high concentration and high toxicity, especially CODCr, NH3-N and volatile phenols are indicators that are difficult to control and quickly reduce the concentration. If the traditional biochemical method is used for treatment, there are problems such as complicated treatment process and long treatment time (more than 8 hours). If various advanced oxidation technologies (such as Fenton, ozone oxidation, photocatalytic oxidation, etc.) are used, it is easy to reach the standard, but There are problems such as high one-time investment, high cost per ton of water, easy generation of secondary pollutants, and high risk of system operation

Method used

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  • Composite flocculant for quick treatment of coke quenching wastewater and use method thereof
  • Composite flocculant for quick treatment of coke quenching wastewater and use method thereof
  • Composite flocculant for quick treatment of coke quenching wastewater and use method thereof

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] The waste water from the quenching tank of a coking plant in Shandong has a pH of 7.18, and the volume of water entering the reaction tank with stirring is 1m3. The pH meter in the reaction tank is linked to adding alkali. After adjusting to pH 8.0, the wastewater concentration of the quenching tank is medium (CODcr is close to 500mg / l), so the total amount of coagulant is added according to 2 thousandths of the water volume, so the oxidant is added to contain 10% 1.67L of available chlorine sodium hypochlorite solution, 0.34L of 10% polymeric ferric sulfate solution, 1L of 1‰ polyacrylamide solution, and reaction for 30 minutes. The measurement data of the supernatant is shown in the table below.

[0026] Test Data

Embodiment 2

[0028] The wastewater from the quenching tank of a coking plant in Xuzhou has a pH of 7.8, and the amount of water entering the stirred reaction tank is 2m3. The pH meter in the reaction tank is linked with alkali and adjusted to pH 8.3. Since the wastewater concentration of the quenching tank is higher (CODcr is higher than 500mg / l), the total amount of coagulant is added according to 3 parts per thousand of the water, so the oxidant is added 5L / h of sodium hypochlorite solution containing 10% of available chlorine, 1L of 10% polyferric sulfate solution, 2L of 1‰ polyacrylamide solution, and reaction for 50 minutes. The measurement data of the supernatant is shown in the table below.

[0029] Test Data

Embodiment 3

[0031] The coking wastewater of the coke oven supporting system of a branch of Shanxi Iron and Steel Group needs to be treated for greening. The water volume is 140 tons / hour. The three coagulation sedimentation tanks after the secondary sedimentation tank are used as three reaction tanks, and the effluent of the secondary sedimentation tank is ph7. 5. Adjust the pH of the three reaction tanks to 8.0. Since the concentration of the coking wastewater is low, the total amount of coagulant is added according to 1 / 1000 of the water volume.

[0032] The reaction tank 1 is based on the catalyst: oxidant ratio of 1:5, that is, 2.8 tons / day of sodium hypochlorite solution containing 10% of available chlorine in the oxidizer, 560kg / day of 10% polymeric ferric sulfate solution, and 3.4 of 1‰ polyacrylamide solution are added. Tons / day, the residence time of the reaction tank is 30 minutes.

[0033] Reaction tank 2 is based on the catalyst: oxidant ratio of 1:4, that is, 2.24 tons / day of sodi...

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Abstract

The invention discloses a composite flocculant for quick treatment of coke quenching wastewater and a use method thereof. The composite flocculant consists of a catalyst main body and an oxidant mainbody, wherein the catalyst main body is a trivalence iron ion, the oxidant main body is a hypochlorite ion, and the molar ratio of the trivalence iron ion to the hypochlorite ion is 1:5; the trivalence iron ion is selected from one of polyferric sulfate, ferric oxide and the like; the hypochlorite ion is selected from chloride gas and deriavative thereof, and one of hypochlorite, chlorate, chlorine dioxide and the like. The composite flocculant has the advantages that the catalytic oxidation function is utilized, the oxidative reduction reaction is generated with the wastewater, and the organic matters are quickly oxidized and decomposed; the prepared composite flocculant can be used for quickly treating the coke quenching wastewater, the supernatant of the treated coke quenching wastewater can meet the requirements of 4.1.5 in national Emission Standard of Pollutants for Coking Chemical Industry (GB 16171-2012), and be used for the repeated dosage quick treatment process after coke quenching, and the purpose of recycling of the coke quenching wastewater is realized.

Description

Technical field [0001] The invention specifically relates to a composite coagulant for rapid treatment of coke quenching wastewater and a method of use thereof. It belongs to the field of coking wastewater treatment. Background technique [0002] Coke quenching is an important process in coke production. Different coke quenching methods directly affect the emission of pollutants in coke production. At present, the widely used coke quenching processes include wet quenching and dry quenching. In In actual production, most coking companies use wet quenching. [0003] In wet coke quenching, the water vapor generated during coke quenching is discharged into the atmosphere from the top outlet of the coke quenching tower, and air pollutants such as coke dust are entrained in the water vapor, and the pollutants are discharged in an organized and intermittent manner. In the quenching process, 0.5 tons of water needs to be evaporated per ton of coke. The harmful gases contained in the stea...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F1/52C02F1/56C02F1/70C02F1/76C02F9/04C02F103/34
CPCC02F1/5236C02F1/56C02F1/66C02F1/70C02F1/725C02F1/766C02F2103/34
Inventor 苗向阳
Owner 上海优帛环境技术有限公司
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