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Treatment method of wastewater containing ammonia nitrogen and cod

A treatment method and technology for wastewater are applied in the field of treatment of wastewater containing ammonia nitrogen and COD, and can solve problems such as low efficiency

Active Publication Date: 2021-11-30
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] The technical problem to be solved by the present invention is the low efficiency of the wet oxidation catalyst in the prior art for removing ammonia nitrogen and COD, and a new wet oxidation treatment method for wastewater containing ammonia nitrogen and COD is provided, which has the ability to simultaneously remove ammonia nitrogen and the advantages of high COD efficiency

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0051] 1. Catalyst preparation

[0052] In terms of weight ratio, ZrO 2 :Ru:Sn is 97:1:2 to prepare the catalyst.

[0053] 97 parts of ZrO 2 The catalyst support is impregnated with RuCl equivalent to 1 part Ru at room temperature 3 and 2 parts Sn of SnCl 4 RuCl 3-SnCl 4 100 parts of the mixed aqueous solution were dried overnight at 80° C. for 12 hours, and then reduced for 4 hours at 300° C. under a hydrogen atmosphere (hydrogen-nitrogen mixture with a hydrogen content of 4%) to obtain a catalyst. The formulation of the catalyst is shown in Table 1.

[0054] 2. Catalyst evaluation

[0055] Using industrial acrylonitrile wastewater as raw material, the COD value of the wastewater is 29,700mg / L, and the ammonia nitrogen is 1,735mg / L. Wastewater mixed with oxygen passes through a 125mL fixed-bed reactor filled with 150g of catalyst. The reaction temperature in the reactor was 260° C., the pressure was 8.5 MPa, and the residence time was 60 minutes. The reaction result...

Embodiment 2

[0057] 1. Catalyst preparation

[0058] In terms of weight ratio, ZrO 2 :Rh:Sn is 97:1:2 to prepare the catalyst.

[0059] 97 parts of ZrO 2 The catalyst support is impregnated with RhCl equivalent to 1 part Rh at room temperature 3 and 2 parts Sn of SnCl 4 RhCl 3 -SnCl 4 100 parts of the mixed aqueous solution were dried overnight at 80° C. for 12 hours, and then reduced for 4 hours at 300° C. under a hydrogen atmosphere (hydrogen-nitrogen mixture with a hydrogen content of 4%) to obtain a catalyst. The formulation of the catalyst is shown in Table 1.

[0060] 2. Catalyst evaluation

[0061] Using industrial acrylonitrile wastewater as raw material, the COD value of the wastewater is 29,700mg / L, and the ammonia nitrogen is 1,735mg / L. Wastewater mixed with oxygen passes through a 125mL fixed-bed reactor filled with 150g of catalyst. The reaction temperature in the reactor was 260° C., the pressure was 8.5 MPa, and the residence time was 60 minutes. The reaction resul...

Embodiment 3

[0063] 1. Catalyst preparation

[0064] In terms of weight ratio, ZrO 2 :Pt:Sn is 97:1:2 to prepare the catalyst.

[0065] 97 parts of ZrO 2 The catalyst support was impregnated with 1 part of Pt in H at room temperature 2 PtCl 6 and 2 parts Sn of SnCl 4 H 2 PtCl 6 -SnCl 4 100 parts of the mixed aqueous solution were dried overnight at 80° C. for 12 hours, and then reduced for 4 hours at 300° C. under a hydrogen atmosphere (hydrogen-nitrogen mixture with a hydrogen content of 4%) to obtain a catalyst. The formulation of the catalyst is shown in Table 1.

[0066] 2. Catalyst evaluation

[0067] Using industrial acrylonitrile wastewater as raw material, the COD value of the wastewater is 29,700mg / L, and the ammonia nitrogen is 1,735mg / L. Wastewater mixed with oxygen passes through a 125mL fixed-bed reactor filled with 150g of catalyst. The reaction temperature in the reactor was 260° C., the pressure was 8.5 MPa, and the residence time was 60 minutes. The reaction re...

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PUM

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Abstract

The invention relates to a treatment method for wastewater containing ammonia nitrogen and COD. The method is used to solve the problem of low efficiency of reducing ammonia nitrogen and COD in waste water in the existing method. The present invention adopts the method for treating waste water containing ammonia nitrogen and COD, comprising reacting the waste water and an oxygen-containing oxidant in a reactor in the presence of a wet oxidation heterogeneous catalyst to remove ammonia nitrogen and COD in the waste water. The oxidation heterogeneous catalyst comprises the following components in parts by weight: (1) 90 to 99.5 parts of a catalyst carrier; (2) 0.1 to 5 parts of a technical solution of at least one precious metal selected from the platinum group, preferably This problem is solved, and it can be used to rapidly degrade ammonia nitrogen and COD in wastewater.

Description

technical field [0001] The invention relates to a treatment method for wastewater containing ammonia nitrogen and COD. [0002] technical background [0003] The COD value in industrial wastewater is often higher than 2000 mg / L, some even as high as hundreds of thousands mg / L, and some wastewater also contains high concentrations of ammonia nitrogen. This type of wastewater contains toxic and harmful compounds such as aldehydes, phenols, amines, acids, etc., has low biodegradability and is extremely harmful to the environment. Catalytic wet oxidation is a platform technology for treating medium and high concentration organic wastewater. Its characteristic is that the organic wastewater is oxidized to CO in the liquid phase under the condition of high temperature (125-320°C) and high pressure (0.5-20MPa), using air or pure oxygen as the oxidant, and under the action of the catalyst. 2 and water and other inorganic substances or small molecular organic substances. This proce...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F1/72B01J23/62B01J23/89B01J23/44B01J23/14B01J23/72B01J37/02B01J37/18C02F101/16C02F101/38
CPCB01J23/14B01J23/44B01J23/626B01J23/72B01J23/8926B01J23/8966B01J37/0201B01J37/18C02F1/72C02F2101/16C02F2101/38C02F2209/08
Inventor 陈航宁郭宗英郑育元许丹丹吴粮华
Owner CHINA PETROLEUM & CHEM CORP