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Treatment method of high-concentration waste water during methanol-to-olefin process

A technology of methanol to olefins and a treatment method is applied in the field of treatment of high-concentration methanol to olefins process wastewater, which can solve the problems of reducing the total amount of MTO pollutants, and achieve the effects of stable treatment effect, simple operation and low treatment cost.

Active Publication Date: 2013-11-06
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0008] In view of the defects in the prior art, the purpose of the present invention is to provide a treatment method for high-concentration methanol-to-olefin process wastewater, which can significantly reduce the total amount of pollutants discharged from MTO production to the environment, so as to make up for the deficiencies of the prior art

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  • Treatment method of high-concentration waste water during methanol-to-olefin process

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Experimental program
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Effect test

Embodiment 1

[0075] The high-concentration MTO process wastewater undergoes homogenization treatment with an average residence time of 24 hours in the homogeneous adjustment unit, and the pH is adjusted by adding sodium hydroxide solution. The main water quality indicators of the effluent are as follows: water temperature is 35°C, pH is 6.5, and COD is 45500mg / L, the content of methanol is 9500mg / L, the content of acetic acid is 4050mg / L, the content of acetone is 6650mg / L, the content of petroleum is 900mg / L, the content of SS is 2300mg / L, and the conductivity is 3560μS / cm.

[0076] In the oil separation coagulation sedimentation unit, polyaluminum chloride and polyacrylamide are used as coagulants, wherein the dosage of polyaluminum chloride is 50mg / L, and the dosage of polyacrylamide is 5mg / L. After the oil separation coagulation sedimentation treatment, the petroleum in the wastewater dropped to 20mg / L, and the SS dropped to 50mg / L.

[0077] In the high-efficiency anaerobic treatment ...

Embodiment 2

[0081] The high-concentration MTO process wastewater is homogenized in the homogeneous adjustment unit with an average residence time of 12 hours, and the pH is adjusted by adding sodium hydroxide solution. The main water quality indicators of the effluent are as follows: water temperature is 25°C, pH is 7.0, and COD is 50500mg / L, the content of methanol is 10100mg / L, the content of acetic acid is 4500mg / L, the content of acetone is 7200mg / L, the content of petroleum is 1050mg / L, the content of SS is 5200mg / L, and the conductivity is 4560μS / cm.

[0082] In the oil separation coagulation sedimentation unit, polyaluminum chloride and polyacrylamide are used as coagulants, wherein the dosage of polyaluminum chloride is 80mg / L, and the dosage of polyacrylamide is 5mg / L. After the oil separation coagulation sedimentation treatment, the petroleum in the wastewater dropped to 35mg / L, and the SS dropped to 65mg / L.

[0083] In the high-efficiency anaerobic treatment unit, anaerobic gr...

Embodiment 3

[0087] The high-concentration MTO process wastewater is homogenized in the homogeneous adjustment unit with an average residence time of 12 hours, and the pH is adjusted by adding sodium hydroxide solution. The main water quality indicators of the effluent are as follows: the water temperature is 40°C, the pH is 7.5, and the COD is 55500mg / L, the content of methanol is 11000mg / L, the content of acetic acid is 4950mg / L, the content of acetone is 8000mg / L, the content of petroleum is 1450mg / L, the content of SS is 7800mg / L, and the conductivity is 5960μS / cm.

[0088] In the oil separation coagulation and sedimentation unit, polyaluminum chloride and polyacrylamide are used as coagulants, and the dosage of polyaluminum chloride is 120mg / L, and no polyacrylamide is added. After the oil separation coagulation sedimentation treatment, the petroleum in the wastewater dropped to 45mg / L, and the SS dropped to 70mg / L.

[0089] In the high-efficiency anaerobic treatment unit, anaerobic ...

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Abstract

The invention relates to a treatment method of high-concentration waste water during methanol-to-olefins (MTO) process, wherein after MTO high-concentration process waste water is treated by the treatment flow of homogeneous regulation, oil-removing coagulating sedimentation, high-efficient anaerobic treatment and post-precipitation, and corresponding condition, the COD of the waste water is reduced to be less than 2000 mg / L from about 50000 mg / L, and the removal rate is more than 96%. The treatment method of high-concentration waste water during methanol-to-olefin process has stable treatment effect, simple and convenient operation and low treatment cost, is easy to commercially produce and can be used for pre-treating MTO high-concentration process waste water before entering the normal sewage treatment plant to be treated aerobically and biologically.

Description

technical field [0001] The invention relates to a treatment method for organic chemical wastewater in the technical field of wastewater treatment, in particular to a treatment method for high-concentration methanol-to-olefin process wastewater. Background technique [0002] With the development of the national economy, especially the increasing demand for low-carbon olefins such as ethylene and propylene, which are basic organic chemical raw materials, resources such as naphtha and light diesel oil, which are traditional raw materials for low-carbon olefins, are facing increasing shortages. Therefore, accelerating the application of relevant alternative production technologies has attracted widespread attention from all aspects of society. [0003] In recent years, the technology development of methanol-to-olefins (MTO) from coal or natural gas has become increasingly mature in the world, and has obvious competitive potential. In the current form of increasing shortage and ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F9/14C02F3/28
CPCY02E50/30Y02W10/37
Inventor 莫馗程学文李正琪万国晖高凤霞张宾
Owner CHINA PETROLEUM & CHEM CORP