Zero discharge treatment system of high salt wastewater

A treatment system, zero-discharge technology, applied in multi-stage water treatment, water/sewage treatment, heated water/sewage treatment, etc., can solve the problems of large steam consumption, high treatment cost, high investment cost and operating cost

Active Publication Date: 2016-05-04
BGT GRP CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Although the patented technology achieves zero-discharge treatment of heavy metal wastewater with high salt content, the patent adopts the third solution, which has high treatment costs, consumes a large amount of steam during the treatment process, and only separates one kind of salt or directly forms a mixed Salt
The mixed salt needs special treatment as a hazardous waste, further increasing the cost
The investment cost and operating cost of this patented technology for the treatment of large volumes of high salt water are very high, and it is difficult for enterprises to accept and use it.

Method used

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  • Zero discharge treatment system of high salt wastewater
  • Zero discharge treatment system of high salt wastewater
  • Zero discharge treatment system of high salt wastewater

Examples

Experimental program
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Effect test

Embodiment 1

[0097] Such as figure 2 The schematic diagram of the process flow is shown. This integrated process is used to treat industrial salty wastewater with complex components. The wastewater comes from industrial sewage treatment and reuse of reclaimed water drainage, sewage from circulating water system, production process drainage, desalinated water station and secondary reverse osmosis concentrated water and backwash water etc.

[0098] Firstly, the wastewater 1 sent from various channels is adjusted in homogeneity and quantity through the adjustment tank 2 . The raw water is sent to the high-density pool 4 through the lift pump 3 . Here, the first dosing device 65 and the second dosing device 66 sequentially add lime or sodium hydroxide, sodium carbonate, PAC, and PAM. Sodium hydroxide is prepared into a solution of 20% concentration, and the dosage is 1.5g / L, and it is prepared into a 15% concentration of sodium carbonate solution. The dosage is 3g / L raw water concentration...

Embodiment 2

[0106] This embodiment is an improved embodiment of the first embodiment, and is a preferred implementation mode of the present invention. This embodiment only describes system parts that are different from those in Embodiment 1, and the same system parts are not described again.

[0107] An electrocoagulation device is connected between the regulating pool 2 and the high-density pool 4 . Electrocoagulation device consisting of a cylindrical acrylic housing and metal electrodes. Six medium-carbon steel electrodes with a size of 110mm×90mm×2mm were used as anodes, and six stainless steel (SS316) electrodes with a size of 110mm×90mm×1mm were used as cathodes in the electrocoagulation device. The anode and cathode electrodes were assembled in an alternating sequence with a 6mm gap between electrodes. A DC power supply was used to apply DC current to the electrocoagulation device. The DC current was varied from 1.5 amps to 3.5 amps with a dwell time of 30 minutes. Saline waste...

Embodiment 3

[0111] The present invention is an embodiment improved on the basis of the first embodiment and / or the third embodiment. This embodiment only describes system parts that are different from those in Embodiment 1 and Embodiment 2, and the same system parts are not repeated here.

[0112] Both the first electrically driven ionic membrane device 23 and the second electrically driven ionic membrane device 26 of the present invention include an anode and a cathode arranged at intervals. There is a filled chamber between the anode and cathode. The filling chamber is insulated from the anode and the cathode, respectively, by a diaphragm. The material of anode and cathode is activated carbon fiber. The diaphragm is an ion exchange membrane or an insulating porous diaphragm. The filling chamber is filled with a plurality of activated carbon particles, carbon fibers or carbon nanotubes with particle diameters ranging from 0.1 to 5.0 mm. Preferably, the filling chamber is filled with ...

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Abstract

The invention relates to a zero discharge treatment system of high salt wastewater. The zero discharge treatment system comprises a cycle pretreatment unit, a cycle reduction unit and a zero discharge unit, and is characterized in that the cycle pretreatment unit is used for discharging contributing water after reaction of the high salt wastewater and pretreatment agentia to the cycle reduction unit after the contributing water is filtered by a tube-type microstrainer, the cycle reduction unit performs preliminary reduction treatment on the contributing water treated by the cycle pretreatment unit by a reverse osmosis device, and performs deep concentration treatment by a multi-level electrically-driven ionic membrane device composed of at least one electrically-driven ionic membrane device, so as to further perform reduction to separate water in the high salt wastewater to a water tank of fresh water for reuse, a concentrated mixed salt solution obtained by deep concentration is discharged to the zero discharge unit, the zero discharge unit recycles nitrate and sodium salt in the concentrated mixed salt solution by heating, steaming and crystallizing the concentrated mixed salt solution. According to the zero discharge treatment system provided by the invention, the separated final mixed salt accounts for 5 percent or less than 5 percent of the total salt content, the contributing water is completely recycled, and zero discharge of wastewater is realized.

Description

technical field [0001] The invention relates to the field of zero-discharge treatment of high-salt wastewater, in particular to a zero-discharge treatment system of high-salt wastewater. Background technique [0002] In recent years, with the rapid development of petrochemical, electric power, metallurgy, coal chemical industry and other industries, the amount of reverse osmosis concentrated water, industrial sewage, recycled sewage and some process sewage produced in the industrial production process has increased year by year. The final disposal and utilization of these complex sewage has received extensive attention. [0003] At present, there are mainly the following methods for the treatment of high-salt and complex wastewater containing refractory organic matter: [0004] First, use strong oxidizing substances (mainly ozone, hydrogen peroxide, etc.) to catalyze and oxidize the refractory organic substances in the wastewater, so that the refractory organic substances i...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/10C02F11/12
CPCC02F1/001C02F1/04C02F1/32C02F1/441C02F1/444C02F1/463C02F1/4693C02F1/4698C02F1/52C02F5/00C02F5/06C02F9/00C02F11/122C02F2301/08
Inventor 权秋红张建飞元西方石维平
Owner BGT GRP CO LTD
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