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Treatment method for high-salt high-organic-matter waste water by evaporation concentration coupling thermocatalytic carbon crystallization

A thermal catalytic carbon, evaporative concentration technology, used in water/sewage treatment, natural water treatment, chemical instruments and methods, etc., can solve the problems of high COD in wastewater, high salt content and high COD treatment in wastewater, high investment and treatment costs , to achieve the effect of increasing the carbonization crystallization rate, reducing the reaction temperature and reducing the processing cost

Active Publication Date: 2018-08-24
DONGHUA UNIV
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  • Abstract
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  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Thermal technology (evaporation), electrochemical method, membrane technology, deep oxidation method, chemical flocculation, ion exchange method and other physical and chemical methods have good treatment effects on some high-salt and high-concentration organic wastewater, but their scope of application is limited, and they cannot be recycled. The investment and disposal costs are high when the useful substances are available, which limits the scope of engineering applications of such methods
Biological method (CN 105084677A) is widely used to treat wastewater due to its economical and harmless characteristics, but the salinity in high-salt and high-organic wastewater will inhibit the microbial activity in the sewage treatment system (Ye Wenfei. High-salt organic wastewater Research progress in biological treatment [J]. Sichuan Environment, 2008, 27(3): 89-92.), and some refractory organic matter is difficult to be degraded by microorganisms, which has certain limitations
Therefore, this type of wastewater generally adopts the method of desalination and pretreatment followed by biochemical treatment (CN 101293721A). However, due to the high COD of wastewater, a large amount of mother liquor is produced in the evaporation process, and the proper treatment of these mother liquors has become a difficult problem for enterprises.
The characteristics of high salt content and high COD of this type of wastewater have brought great obstacles to its treatment. In the face of increasingly stringent sewage discharge standards, a single treatment method has certain economic and technical problems.

Method used

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  • Treatment method for high-salt high-organic-matter waste water by evaporation concentration coupling thermocatalytic carbon crystallization

Examples

Experimental program
Comparison scheme
Effect test

Embodiment

[0025] A treatment method for high-salt and high-organic-matter wastewater coupled with thermocatalytic carbon crystallization by evaporation and concentration:

[0026] (1) Take 2.5L of waste water from a certain chemical plant (mass fraction of total salt=6.1%, COD is 52706mg / L, B / C is 0.14, pH=9.5), add 5mg propionic acid, 7.5mg succinic acid, 20mg of glutaric acid, 17.5mg of oxalic acid and 25mg of citric acid, and stir (200rpm) to mix evenly.

[0027] (2) Pour it into an evaporator, and carry out evaporation and desalination under the conditions of 80° C. and a pressure of -0.2 MPa at a temperature, and separate 0.116 kg of inorganic salt and clear liquid of the evaporation liquid (mass fraction of total salt=0.46%, 2.20 L , COD concentration 370mg / L, pH=8.6) and 240mL high-concentration evaporation dope (mass fraction=10.99% of total salt, COD is 522400mg / L, B / C is 0.10, pH=10.3). The evaporated liquid and clear liquid are reused or discharged after physical and chemica...

Embodiment 2

[0031] A treatment method for high-salt and high-organic-matter wastewater coupled with thermocatalytic carbon crystallization by evaporation and concentration:

[0032] (1) Take 2.5L of certain pharmaceutical wastewater (mass fraction of total salt=5.2%, COD is 45706mg / L, B / C is 0.16, pH=9.7), add 2.5mg propionic acid, 5mg succinic acid, 20mg Glutaric acid, oxalic acid 17.5mg and citric acid 25mg, and stir (200rpm) mix well.

[0033] (2) Pour it into an evaporator, and carry out evaporation and desalination at a temperature of 85° C. and a pressure of -0.2 MPa to separate 0.097 kg of inorganic salt and clear liquid of the evaporated liquid (mass fraction of total salt=0.45%, 2.23 L , COD concentration 350mg / L, pH=8.8) and 220mL high-concentration evaporation dope (mass fraction=10.45% of total salt, COD is 451300mg / L, B / C is 0.11, pH=10.5). The evaporated liquid and clear liquid are reused or discharged after physical and chemical and biochemical treatment.

[0034] (3) Add...

Embodiment 3

[0037] A treatment method for high-salt and high-organic-matter wastewater coupled with thermocatalytic carbon crystallization by evaporation and concentration:

[0038] (1) Take 2.5L of certain pesticide wastewater (mass fraction of total salt=5.7%, COD is 68542mg / L, B / C is 0.12, pH=10.2), add 5mg propionic acid, 9mg succinic acid, 20mg valeric acid to it Diacid, oxalic acid 17.5mg and citric acid 25mg, and stir (200rpm) to mix well.

[0039] (2) Pour it into an evaporator, and carry out evaporation and desalination at a temperature of 85° C. and a pressure of -0.2 MPa to separate 0.112 kg of inorganic salt and clear liquid of the evaporation liquid (mass fraction of total salt=0.43%, 2.18 L , COD concentration 420mg / L, pH=9.7) and 230mL high-concentration evaporation dope (mass fraction=9.19% of total salt, COD is 677200mg / L, B / C is 0.10, pH=11.1). The evaporated liquid and clear liquid are reused or discharged after physical and chemical and biochemical treatment.

[0040] ...

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Abstract

The invention discloses a treatment method for high-salt high-organic-matter waste water by evaporation concentration coupling thermocatalytic carbon crystallization. The method comprises the following steps: firstly pre-treating the high-salt high-organic-mater waste water by adopting an organic acid, performing multi-effect evaporation desalination, performing separation to form an evaporation clear liquid and a high-concentration evaporation concentrated liquid, and enabling an inorganic salt to be crystallized and separated; performing physicochemical and biochemical treatment on the evaporation clear liquid, performing recycling or discharging the clear liquid, adding a carbonized crystallization catalyst into the high-concentration evaporation concentrated liquid, performing a thermocatalytic carbon crystallization reaction, and after the reaction is completed, performing solid-liquid separation on the formed solid-liquid mixture to obtain a solid carbonized product and a carbonized supernatant. The method disclosed by the invention combines concentration salt extraction, organic-matter thermocatalytic carbon crystallization and biochemical treatment, removes the inorganic salt and organic matter step by step, significantly improves a salt removing rate and COD removing rate of the waste water, and has the advantages of a simple process, mild conditions and low treatmentcosts.

Description

technical field [0001] The invention belongs to the technical field of environmental protection, and in particular relates to a treatment method for high-salt and high-organic-matter wastewater coupled with thermocatalytic carbon crystallization by evaporation and concentration. Background technique [0002] High-salt and high-organic wastewater mainly comes from petrochemical, metallurgy, textile, pharmaceutical, food processing and other industries. The wastewater has high salt content, high COD, dark color, poor biodegradability, and most of them are potentially toxic (Wang Haiping. Fenton oxidation Application in the treatment of "three high" wastewater [J]. Silicon Valley, 2014, 160(16): 110-111.). With the rapid development of my country's industry, the discharge of high-salt and high-organic waste water shows a trend of increasing year by year, which brings great pressure to the ecological environment. If these high-salt, high-organic-matter wastewater is discharged ...

Claims

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Application Information

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IPC IPC(8): C02F9/14C02F103/34C02F101/30C02F101/10
CPCC02F1/02C02F1/04C02F1/66C02F1/725C02F3/02C02F9/00C02F2101/10C02F2101/30C02F2103/343
Inventor 薛罡游继光李响陈红钱雅洁刘振鸿张文启方庭玕安婧刘云帆汪钟凝
Owner DONGHUA UNIV
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