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Alternating type cascade treatment method for high-salinity wastewater

A technology for high-salt wastewater and a treatment method, applied in the field of environmental engineering, can solve the problems of increasing initial investment and operating costs, increasing operating costs such as power consumption, and insufficient adsorption effect of adsorbents, and is conducive to mass popularization and application, reducing operation. Cost and human input, the effect of good engineering application prospects

Inactive Publication Date: 2021-09-28
TONGJI UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Biological method is a method of treating wastewater by using the metabolism and reproduction of microorganisms themselves. However, heavy metals and other substances in high-salt wastewater will destroy the life structure of microorganisms, inhibit their growth and reproduction, and even lead to cell inactivation.
The chemical method is to deal with chemicals, which is costly and will cause secondary pollution
The physical method separates some pollutants from the wastewater system by physical means such as adsorption, flocculation, coagulation, etc. Compared with the above two methods, this method is more feasible, but there are still the following problems to be solved: ① existing technology adsorption or After filtration, it needs desorption or backwashing, so it can only run intermittently. Usually, several parallel processes are set to run alternately. The essence is still intermittent operation, which increases the initial investment and operating costs; ②The quality of the adsorbent is large, which increases the total weight of the equipment. Thereby increasing the operating costs such as power consumption; ③The existing adsorbent has insufficient adsorption effect
As a new type of lightweight material, hydrogel has a good adsorption effect on pollutants, but its application in the field of high-salt wastewater treatment has rarely been reported.

Method used

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  • Alternating type cascade treatment method for high-salinity wastewater
  • Alternating type cascade treatment method for high-salinity wastewater
  • Alternating type cascade treatment method for high-salinity wastewater

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0047] Such as figure 1 As shown, the system adopted for the alternate cascading treatment method of the high-salt wastewater provided by the present invention is operated, such as Figure 1-2 As shown, the system includes a pollutant removal system 1 and an alternating cascade system water delivery system 2 nested in the pollutant removal system 1;

[0048] The pollutant removal system 1 includes four partition plates 11, a pollutant removal area 12 of hollow cylindrical structure, a cylindrical water outlet chamber 13 located at the axis of the pollutant removal area 12, and a rotating shaft fixedly connected to the four partition plates 11 14. The motor 18 that drives the rotating shaft 14 to rotate, and the fixed bracket 15 that is fixedly connected with the motor 18 and used to support the system;

[0049] Four partition plates 11 are evenly distributed in the pollutant removal area 12 of the pollutant removal system 1, and the pollutant removal area 12 is evenly divided...

Embodiment 2

[0079] The difference between this embodiment and Embodiment 1 is that in the alternate cascading treatment system for high-salt wastewater used in this embodiment, the diameter of the outlet bin 13 is 200mm, and the diameter of the filter screen 17 is the outlet bin cloth water hole 132 35%, the diameter of the purified water outlet hole 241 is 112% of the diameter of the corresponding water outlet hole 132; the diameter of the purified water outlet hole 241 is 5.5mm, and the diameter of the water inlet delivery pipe 20 is 13 33% of the diameter.

[0080] The thickness of the hydrogel filler in the pollutant removal zone is 750mm, and the filling rate of the built-in hydrogel material is 75%. The outlet casing 131 of the outlet chamber 13 is cylindrical in shape, with a diameter of 1100mm and made of stainless steel.

Embodiment 3

[0082] The difference between this embodiment and Embodiment 1 is that in the alternate cascading treatment system for high-salt wastewater used in this embodiment, the diameter of the outlet bin 13 is 280 mm, and the diameter of the filter screen 17 is the outlet bin cloth water hole 132 55%, the diameter of the purified water outlet hole 241 is 115% of the diameter of the corresponding water outlet hole 132; the diameter of the purified water outlet hole 241 is 8mm, and the diameter of the water inlet delivery pipe 20 is the diameter of the water outlet 13 45%.

[0083] The thickness of the hydrogel filler in the pollutant removal zone is 1000mm, and the filling rate of the built-in hydrogel material is 85%. The water outlet shell 131 of the water outlet chamber 13 is cylindrical, with a diameter of 2000mm, and is made of stainless steel.

[0084] It should be noted that the descriptions in this application such as “first” and “second” are used for description purposes only,...

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Abstract

The invention provides an alternating type cascade treatment method for high-salinity wastewater. The alternating type cascade treatment method comprises the following steps that the high-salinity wastewater enters and fills a first pollutant removal zone; a motor system rotates by 90 degrees, and then high-salinity wastewater filling is carried out on the next pollutant removal zone again; after the rotation is repeated twice, high-salinity wastewater in the first pollutant removal zone is discharged, and cleaning is carried out; and the steps are repeated to complete the uninterrupted removal of the salts and the heavy metal ions in the high-salinity wastewater. According to the method, four pollutant removal subareas sequentially work, and an alternating cascade system water conveying system comprises a water inlet distribution channel and a cleaning water distribution channel which are arranged on the outer wall of the first pollutant removal zone and the outer wall of a third pollutant removal zone correspondingly; a purified water outlet pipe and a cleaning water outlet pipe are located in a water outlet bin and have the same water outlet direction from top to bottom in the axial direction, multi-point water inlet is achieved through cascade water distribution, the water distribution uniformity is improved, and the treatment effect of the system can be greatly improved.

Description

technical field [0001] The invention belongs to the technical field of environmental engineering, and in particular relates to an alternating cascading treatment method for high-salt wastewater. Background technique [0002] As the main component of industrial production wastewater, high-salt wastewater has become a major environmental protection problem faced by industrial development and wastewater treatment at the present stage due to its large discharge volume and high difficulty in treatment. Substandard discharge of high-salt wastewater will not only waste salt and water resources, but also cause serious environmental pollution. Since salinity is an important environmental factor in the water environment, it has a direct or indirect impact on aquatic organisms, growth and reproduction. When the salinity of the water environment increases sharply, it will lead to the osmotic balance between the aquatic species and its living environment, causing dehydration of the cell...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F1/28
CPCC02F1/28C02F2303/16C02F2303/14
Inventor 张亚雷周雪飞杨银川陈家斌王雷张新妙朱沁林
Owner TONGJI UNIV
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