Resource recovery and utilization treatment system for high-concentration refractory saline organic wastewater
A technology for organic waste water and treatment system, which is applied in water/sewage multi-stage treatment, water/sludge/sewage treatment, general water supply conservation, etc. To achieve the effect of realizing internal circulation and resource recycling, reducing the risk of inorganic salt scaling, and reducing the risk of organic pollution
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Embodiment 1
[0106] Adopt the method of the present invention to attach figure 1 The integrated process in the process treats the saline wastewater of an oil refinery, and the water quality indicators are as follows:
[0107] serial number
[0108] The system includes the following steps:
[0109] a. Pretreatment process
[0110] Wastewater first enters the crystallization defluorination reactor for pretreatment. After pretreatment, part of the suspended solids, organic matter and fluoride ions in the wastewater are removed.
[0111] Pretreatment effluent: turbidity ≤ 130NTU, COD ≤ 1700mg / L, effluent flows into the comprehensive wastewater regulating tank for water quality and quantity regulation.
[0112] b. Biochemical treatment process
[0113] The biochemical treatment process unit adopts anaerobic-anoxic-aerobic (A 2 O) process, COD, nitrogen, and phosphorus are removed from wastewater.
[0114] After the biochemical treatment unit, the COD of the wastewater is ≤170mg / ...
Embodiment 2
[0129] Adopt the method of the present invention to attach figure 2 The integrated process in the process treats wastewater from a coking plant, and the water quality indicators are as follows:
[0130] serial number
project
unit
Influent water quality
1
COD Cr
mg / L
≤3500
2
NH 3 -N
mg / L
≤140
3
mg / L
≤500
4
NTU
≤240
5
Total hardness (as CaCO 3 count)
mg / L
≤280
6
Total Dissolved Solids (TDS)
mg / L
≤3500
7
pH
-
6~9
[0131] The system includes the following steps:
[0132] a. Pretreatment process
[0133] The wastewater first enters the grease trap, the air flotation tank, and the crystallization defluorination reactor for pretreatment. After pretreatment, part of the oil, suspended solids, fluoride ions and organic matter in the wastewater are removed.
[0134] Pretreatment effluent: turbidity ≤ 30NTU, COD ≤ 24...
Embodiment 3
[0153] Adopt the method of the present invention to attach figure 2 The integrated process flow in the paper treats a certain coal gas waste water. The water quality indicators are as follows:
[0154] serial number
project
unit
Influent water quality
1
COD Cr
mg / L
≤5200
2
NH 3 -N
mg / L
≤175
3
mg / L
≤280
4
NTU
≤190
5
Total hardness (as CaCO 3 count)
mg / L
≤330
6
Total Dissolved Solids (TDS)
mg / L
≤3000
7
pH
-
8.0~9.0
[0155] The system includes the following steps:
[0156] a. Pretreatment process
[0157] The wastewater first enters the grease trap, the air flotation tank, and the crystallization defluorination reactor for pretreatment. After pretreatment, part of the oil, suspended solids, fluoride ions and organic matter in the wastewater are removed.
[0158] Pretreatment effluent: turbidity ≤ 25NTU, COD ...
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Abstract
Description
Claims
Application Information
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