High-concentration organic wastewater wet oxidation treatment system and method

A technology of organic wastewater and wet oxidation, applied in the field of water treatment, can solve the problems of difficult to achieve direct discharge of organic wastewater, poor treatment effect of refractory substances, negative impact on the cost of exhaust gas treatment, etc., to reduce the risk of scaling and blockage, Convenient transportation and installation, and the effect of reducing operating costs

Pending Publication Date: 2017-02-08
JIANGSU PROVINCIAL ACAD OF ENVIRONMENTAL SCI +1
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0004] At present, there are a series of problems in the actual industrial application of wet oxidation technology: (1) The oxidant commonly used in the process is air, the oxygen content in the air is about 20%, and the rest is nitrogen that does not participate in the reaction, so a large flow of air needs to be delivered to the reaction Therefore, larger compressors are required, and the investment cost of equipment is high. At the same time, the oxidation effect is not as good as that of pure oxygen, which also has a negative impact on the cost of tail gas treatment; The treatment effect of refractory subst

Method used

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  • High-concentration organic wastewater wet oxidation treatment system and method
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  • High-concentration organic wastewater wet oxidation treatment system and method

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Embodiment 1

[0040] like figure 1 The shown wet oxidation treatment system for high-concentration organic wastewater includes a pretreatment device, a heat transfer oil heating device and a reaction device 6 connected in sequence through pipelines; A heat exchanger 14 is communicated through the inner pipe of the first heat exchanger 14; the inlet of the reaction device 6 is provided with a bypass for introducing oxygen, which is directly connected to the oxygen generator; the bypass for introducing oxygen is provided with a second heat exchange 5, the inlet of the oxygen generator and the reaction device 6 are communicated through the inner pipe of the second heat exchanger 5; the outlet of the reaction device 6 is connected to the outer pipe of the second heat exchanger 5 and the outer Pipe, cooling device, pressure reducing device 20, gas-liquid separation device 21 and exhaust gas treatment device 22. In addition, a bypass pipeline is provided between the inlet and outlet of the heat-...

Embodiment 2

[0052] Utilize the above-mentioned system to carry out the method for wet oxidation treatment of high-concentration organic wastewater:

[0053] When the system is running:

[0054] 1. The air is pressurized to 0.4-0.8MPa by the air compressor 1, and enters the first PSA oxygen generator tank 2 or the second PSA oxygen generator tank 3; wherein, the PSA oxygen generator tank is used for one use and one for preparation , when one oxygen generator is preparing high-purity oxygen, the other is discharging nitrogen for backup. High-purity oxygen with a purity of more than 90% can be produced through the first PSA oxygen generator 2 or the second PSA oxygen generator 3, and the opening of the valve V1 is automatically adjusted to control the oxygen flow into the system to reach the required set value The high-purity oxygen can be pressurized by the oxygen booster 4 to a reaction pressure of 5-12 MPa, and the pressurized high-purity oxygen enters the inner tube of the second heat e...

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Abstract

The invention discloses a high-concentration organic wastewater wet oxidation treatment system, which is integrated by an oxygen generating device, a pretreatment device, a heat conducing oil heating device, a wet oxidation treatment device, a cooling pressure reduction device, a gas-liquid separation device, a tail gas treatment device and the like. The invention also discloses a method for treating high-concentration organic wastewater by the system. Compared with the prior art, the system has the advantages that the transportation and the installation are convenient; the integration performance is good; the system fully recovers and utilizes heat after reaction through a multistage heat exchanger for preheating waste water and oxygen, so that the operation cost can be reduced; through the oxygen generating device, air is used as raw materials for preparing high-purity oxygen on site for wet oxidation reaction, so that the contaminant removing efficiency can be improved; the wet oxidation reaction device made of duplex metal composite materials is used, and a catalyst box is arranged inside the reaction device, so that the corrosion resistant capability of the reaction device is favorably improved, and the reaction conditions are reduced. The system can realize reaction device slag discharging in the operation process, so that the risk of system scale formation and blockage is favorably reduced, and the system can be widely applied to the treatment of high-concentration difficult-to-degrade organic wastewater.

Description

technical field [0001] The invention belongs to the technical field of water treatment, and in particular relates to a wet oxidation treatment system and method for high-concentration organic waste water. Background technique [0002] In recent decades, with the rapid development of industrialization, environmental pollution has become increasingly serious, especially water pollution. In my country, water pollution mainly comes from refractory industrial sewage, especially sewage from petroleum, chemical, pesticide and other industries, which has the characteristics of high concentration, complex composition, toxic and harmful, and poor biodegradability, which makes the traditional biodegradation process suffer. serious challenge. In addition, the large-scale application of membrane technology in recent years has led to the further concentration of high-concentration industrial sewage, and the resulting concentrated solution has a greater threat to humans and the environment...

Claims

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Application Information

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IPC IPC(8): C02F9/04C02F1/72B01D53/02F24H7/00
CPCB01D53/02F24H7/00C02F1/725C02F1/727C02F9/00C02F2301/08C02F1/66C02F1/001B01D2253/102
Inventor 公彦猛姜伟立李爱民周海云范亚民常闻捷刘树洋
Owner JIANGSU PROVINCIAL ACAD OF ENVIRONMENTAL SCI
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