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Device and method for in-situ multistage treatment of high-salinity wastewater

A technology for high-salt wastewater and secondary wastewater, which is applied in the fields of water/sewage multi-stage treatment, chemical instruments and methods, reduced water/sewage treatment, etc., and can solve problems such as the difficulty of high-salt wastewater treatment

Inactive Publication Date: 2020-06-16
INST OF PROCESS ENG CHINESE ACAD OF SCI +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0011] In order to solve the problem of difficult treatment of high-salt wastewater in the prior art, the present invention provides a device and method for multi-stage treatment of low-temperature dynamic high-salt wastewater, which treats wastewater by grading and sub-units, based on the difference in the composition and concentration of the treated wastewater , realize the alternation of dominant bacteria and abundance of each unit in each classification device, and recover metal resources while degrading organic waste

Method used

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  • Device and method for in-situ multistage treatment of high-salinity wastewater
  • Device and method for in-situ multistage treatment of high-salinity wastewater

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Effect test

Embodiment 1

[0074] like figure 1 and figure 2 As shown, a device and method for in-situ multi-stage treatment of low-temperature dynamic high-salt wastewater based on deep-sea cold spring microorganisms is used to treat organic high-salt heavy metal composite wastewater produced in mineral processing, metallurgy, and chlor-alkali industries. Wastewater mainly contains Cl - , SO 4 2- Such as inorganic salt ions, macromolecular organic substances and heavy metal ions such as copper, lead, zinc, iron, chromium, vanadium, among which COD is as high as 1000-10000mg / L, NH 4 + The concentration is 500mg / L, V 5+ The concentration is 600mg / L, Cu 2+ The concentration is 300mg / L, the salinity range is 5-8%, the pH is 5-7, and the treatment temperature is 0-30°C. There are 8, 6, and 4 processing units in the primary, secondary, and tertiary processing devices of the processing system, respectively.

[0075] S1: The organic high-salt heavy metal composite wastewater is pumped from the buffer ...

Embodiment 2

[0080] like figure 1 and figure 2 As shown, a device and method for in-situ multi-stage treatment of low-temperature dynamic high-salt wastewater based on deep-sea cold spring microorganisms is used to treat organic high-salt heavy metal composite wastewater produced in the petrochemical industry. Petrochemical wastewater contains more carcinogenic heavy metal elements, such as vanadium, chromium, molybdenum, etc., and also contains macromolecular organic compounds such as benzene. where V 5+ The concentration is 800mg / L, Cr 6+ The concentration is 400mg / L, Mo 6+ The concentration is 700mg / L, the COD is as high as 12000mg / L, the salinity range is 5-10%, the pH is 6-9, and the treatment temperature is 0-25°C. There are 8, 8, and 4 processing units in the first, second, and third-level processing devices of the processing system, respectively.

[0081] S1: The organic high-salt heavy metal composite wastewater is pumped from the buffer pool 3 to the primary wastewater trea...

Embodiment 3

[0086] like figure 1 and figure 2 As shown, a device and method for in-situ multi-stage treatment of low-temperature dynamic high-salt wastewater based on deep-sea cold spring microorganisms is used to treat coking wastewater generated during coke refining, gas purification and chemical product recovery. COD up to 25000mg / L, Fe 2+ The content is 1100mg / L, Cu 2+ The content is 300mg / L, NH 4 + -N concentration is 400mg / L, NO 2 - - The N concentration is 800mg / L, the salinity range is 6-9%, the pH is 1-3, and the treatment temperature is 1-15°C. There are 8, 8, and 4 processing units in the first, second, and third-level processing devices of the processing system, respectively.

[0087] S1: The organic high-salt heavy metal composite wastewater is pumped from the buffer pool 3 to the primary wastewater treatment area 8 through the vacuum pump 2. This area is composed of 6 graphite felt adsorption treatment units 3, and the gradient increases from the water inlet to the w...

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Abstract

The invention discloses a device and method for in-situ multistage treatment of low-temperature dynamic high-salinity wastewater. The device provided by the invention can realize partitioned multistage treatment of wastewater; according to detection data, wastewater can selectively and automatically return to a grading treatment device corresponding to a wastewater detection value, microorganismscan complete self-replacement of strains and floras in the wastewater treatment process, and high-salinity, high-organic-matter and high-heavy-metal-ion wastewater can be continuously and efficientlytreated in a targeted mode in an energy-saving mode at the low temperature and in the high-salinity environment.

Description

technical field [0001] The invention belongs to the field of environmental protection machinery, and specifically relates to a device and method for multi-stage treatment of low-temperature dynamic high-salt wastewater, and is especially suitable for in-situ multi-stage treatment of low-temperature dynamic high-salt wastewater by bacterial strains domesticated at deep-sea hydrothermal vents. Background technique [0002] In this field, high-salt wastewater refers to wastewater with a total salt content of at least 1%, which mainly comes from chemical plants and the collection and processing of oil and natural gas. This wastewater contains various substances, mainly including salt, oil, and organic heavy metals. and radioactive substances. [0003] With the development of my country's industry and the improvement of environmental standards, the existing water treatment methods are no longer suitable for organic wastewater with a high salinity range, and the cost is extremely ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/14C02F101/30C02F101/16
CPCC02F1/281C02F1/70C02F3/34C02F9/00C02F2001/007C02F2101/16C02F2101/30C02F2201/002C02F2201/007
Inventor 李浩然李海龙
Owner INST OF PROCESS ENG CHINESE ACAD OF SCI