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Multiphase Wet Oxidation Method for Industrial Wastewater Treatment

A technology for industrial wastewater and wet oxidation, applied in the direction of oxidized water/sewage treatment, chemical instruments and methods, chemical/physical processes, etc., can solve the problems of low COD removal rate and poor stability, and achieve COD removal rate improvement, good technology effect of effect

Active Publication Date: 2017-10-27
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The technical problem to be solved by the present invention is the problem of low COD removal rate and poor stability in the heterogeneous catalytic wet oxidation reaction in the prior art, and a new method for the treatment of industrial wastewater by heterogeneous wet oxidation is provided, which is used for heterogeneous catalysis In the wet oxidation reaction, it has the advantages of high COD removal rate and high catalyst stability in high-concentration industrial wastewater

Method used

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  • Multiphase Wet Oxidation Method for Industrial Wastewater Treatment
  • Multiphase Wet Oxidation Method for Industrial Wastewater Treatment
  • Multiphase Wet Oxidation Method for Industrial Wastewater Treatment

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0035] Catalyst preparation

[0036] Prepare 0.8mol / l Ti(SO 4 ) 2 , 0.4mol / l ZrOCl 2 ·8H 2 O and 0.2mol / l Ce(NO 3 ) 3 ·6H 2 O mixed solution 1000ml and 0.6mol / l ammonia water 500mL. The mixed solution of cerium salt, zirconium salt and titanium salt is co-precipitated with ammonia water to form a gel substance, which is vacuum filtered, washed, dried, and roasted at 800°C for 4 hours to make TiO 2 -ZrO 2 -CeO 2 carrier.

[0037] 19.8g TiO 2 -ZrO 2 -CeO 2 The support was impregnated with 0.526g RuCl 3 in aqueous solution. Impregnated at room temperature for 15 h, then dried in an oven at 110 °C for 8 h, then calcined in a muffle furnace at 450 °C for 5 h to obtain a catalyst precursor, and finally reduced with hydrogen at 400 °C for 3.5 h to obtain catalyst C1. The catalyst composition is shown in Table 1, and the preparation conditions are shown in Table 2.

[0038] evaluation test

[0039] The bed volume is 120 milliliters, the lower layer is a ring-shaped cera...

Embodiment 2

[0041] Catalyst preparation

[0042] Prepare 0.8mol / l Ti(SO 4 ) 2 , 0.4mol / l ZrOCl 2 ·8H 2 O and 0.2mol / l Ce(NO 3 ) 3 ·6H 2 O mixed solution 1000ml and 0.6mol / l ammonia water 500mL. The mixed solution of cerium salt, zirconium salt and titanium salt is co-precipitated with ammonia water to form a gel substance, which is vacuum filtered, washed, dried, and roasted at 800°C for 4 hours to make TiO 2 -ZrO 2 -CeO 2 carrier.

[0043] 19.8g TiO 2 -ZrO 2 -CeO 2 The carrier was impregnated with 0.333g PdCl 2 in aqueous solution. Impregnated at room temperature for 15 h, then dried in an oven at 110 °C for 8 h, then calcined in a muffle furnace at 420 °C for 6 h to obtain a catalyst precursor, and finally reduced with hydrogen at 450 °C for 3 h to obtain catalyst C2. The catalyst composition is shown in Table 1, and the preparation conditions are shown in Table 2.

[0044] evaluation test

[0045] The bed volume is 120 milliliters, the lower layer is a ring-shaped cera...

Embodiment 3

[0047] Catalyst preparation

[0048] Prepare 0.8mol / l Ti(SO 4 ) 2 , 0.4mol / l ZrOCl 2 ·8H 2 O and 0.2mol / l Ce(NO 3 ) 3 ·6H 2 O mixed solution 1000ml and 0.6mol / l ammonia water 500mL. The mixed solution of cerium salt, zirconium salt and titanium salt is co-precipitated with ammonia water to form a gel substance, which is vacuum filtered, washed, dried, and roasted at 800°C for 4 hours to make TiO 2 -ZrO 2 -CeO 2 carrier.

[0049] 19.8g activated carbon was impregnated with 0.513g H 2 PtCl 6 ·6H 2 O solution. Impregnated at room temperature for 15 h, then dried in an oven at 110 °C for 8 h, then calcined in a muffle furnace at 500 °C for 4 h to obtain a catalyst precursor, and finally reduced with hydrogen at 350 °C for 4 h to obtain catalyst C3. The catalyst composition is shown in Table 1, and the preparation conditions are shown in Table 2.

[0050] evaluation test

[0051] The bed volume is 120 milliliters, the lower layer is a ring-shaped ceramic packing, th...

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Abstract

The invention relates to a method for multiphase wet oxidation treatment of industrial waste water, which mainly solves the problems of low COD removal rate and poor stability in the prior art. The present invention adopts the method for treating industrial wastewater by heterogeneous wet oxidation. The wastewater and oxygen-containing oxidant flow into a fixed bed reactor to react and remove reducing substances in the wastewater. The fixed bed layer includes at least one inert filler A composite wet reaction bed composed of layer and catalyst layer; in the composite wet reaction bed, the inert packing layer is positioned at the upstream of the wastewater inflow direction, and the catalyst layer is positioned at the downstream technical scheme of the wastewater inflow direction, preferably It solves this problem effectively and can be used in the treatment of industrial wastewater.

Description

technical field [0001] The invention relates to a method for multiphase wet oxidation treatment of industrial waste water. Background technique [0002] In the late 1970s, on the basis of wet oxidation technology, catalytic wet oxidation was developed to decompose organic matter and harmful substances containing N and S in sewage into CO 2 , N 2 , SO 4 = and H 2 O and other harmless substances. Catalytic wet oxidation technology can treat wastewater alone or as a pretreatment of biochemical treatment. Through wet oxidation, the COD of wastewater can be reduced, toxic and harmful substances to biochemical bacteria can be removed, and the biodegradability of wastewater can be improved. On the other hand, with the increasing pressure of energy saving and consumption reduction, environmental protection control is becoming more and more stringent. Wastewater with high concentration of organic matter will be incinerated by incinerators, which will cause double pressure on ener...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F1/72B01J23/83B01J32/00
Inventor 郑育元陈航宁郭宗英汪国军
Owner CHINA PETROLEUM & CHEM CORP