Method for high temperature wastewater treatment and reuse in MTO process

A high-temperature wastewater treatment method technology, applied in natural water treatment, neutralized water/sewage treatment, water/sewage multi-stage treatment, etc. To achieve the effect of good effluent water quality, good effluent water quality and strong adaptability

Active Publication Date: 2011-02-02
CHINA PETROLEUM & CHEM CORP +1
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Problems solved by technology

[0010] Chinese patent application CN101139117A and CN101139118A disclose a kind of wastewater treatment process containing methanol and dimethyl ether, the specific method is: the wastewater containing methanol and dimethyl ether is pressurized to exchange heat with the purified water at the bottom of the stripping tower, Then enter the stripping tower, the gas mixture such as methanol produced at the top of the stripping tower enters the reflux tank after heat exchange, and part of it returns to the top of the stripping tower as reflux; the other part is sent to the outside of the device or used as a raw material for the MTO device; The purified water in the stripping tower after heating is exchanged with the wastewater containing methanol and dimethyl ether, and then sent to the outside of the device. The total content of methanol and dimethyl ether in the purified water after stripping is not more than 100ppm, which can meet the requirements of sewage treatment. According to the requirements of influent water quality, biochemical treatment is used as the main process to discharge and treat process wastewater up to standard. However, the patent does not directly treat the high-temperature process wastewater discharged from the stripping tower kettle to recover low-grade heat and reduce waste water for reuse. make specific reports
[0011] The above-mentioned foreign patents mainly consider the reuse of the process itself at the point of water demand from the process itself, but since the MTO process itself is a process in which olefins and water are continuously produced, when the water cycle of the process itself reaches a stable level, a large amount of water will still be discharged , the above-mentioned patents have no reports on the treatment and reuse of the remaining process wastewater; while the Chinese patent application mainly adopts the steam stripping method to recycle a large amount of organic matter in the process wastewater, so that the process wastewater can be purified to reach the water quality of the sewage treatment plant As for the direct treatment, indirect treatment and detailed recycling method of the high-temperature process wastewater in the tower kettle after stripping, there is no report in the patent application
[0012] In addition, although patent applications CN101088922A and CN101092258A respectively disclose a method for membrane separation and purification of high-temperature condensate water and a method for membrane integration process to treat high-temperature condensate water, they use inorganic ceramic microfiltration or ultrafiltration membranes and nanofiltration membranes from different angles. Methods to remove impurities such as suspended solids, oil, colloids, soluble small molecular organics and some inorganic ions in steam condensate water, but neither of them has been studied and reported on the treatment of high-temperature wastewater related to MTO process
Therefore, there are currently no data reports on the advanced treatment and reuse of high-temperature wastewater from the MTO process.

Method used

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Examples

Experimental program
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Effect test

Embodiment 1

[0039] The high temperature wastewater treatment process of the stripper kettle figure 1 As shown, the purified water A from the 70°C MTO process stripping tower is discharged into the sedimentation separation tank 1. The main water quality parameters include: wastewater temperature of 70°C, pH of 5.5, turbidity of 86.9NTU, and oil content of 8.9mg / L , The total iron content is 45.2mg / L, SiO 2 The content is 8.9μg / L.

[0040] First, the stripping purified water is adjusted to pH 8.0 and then mixed by a pipeline mixer and then discharged into the sedimentation separation tank 1. At the bottom of the sedimentation separation tank, the microporous aeration device B is used for aeration operation, and the aeration flow is 50L / min. The hydraulic retention time of alkali-adjusted aeration is 20min. The precipitated colloidal substances are discharged through sludge discharge port C. The mixed wastewater after alkali-adjusted aeration is separated by sedimentation and discharged into th...

Embodiment 2

[0044] High temperature wastewater treatment process such as figure 1 As shown, the purified water A from the stripping tower of the 80°C MTO process is discharged into the sedimentation separation tank 1. The purified water quality of the stripping tower is as described in Example 1. The same pretreatment process in Example 1 is used. The quality of the water produced by the process is as described in Example 1.

[0045] The pretreated stripped purified water is sent to the ultrafiltration system 3 through the centrifugal pump 2. The ultrafiltration membrane pore size is 0.1μm high temperature resistant organic ultrafiltration membrane Duratherm HWS UF 2540, and the effective membrane area is 2.3m 2 , The filtration flux of ultrafiltration membrane is 200L / m 2 h. The feed water pressure of the ultrafiltration membrane system is 0.2bar, the recovery rate of the ultrafiltration system is adjusted to 95%, the ultrafiltration concentrated water is circulated to the sedimentation tank...

Embodiment 3

[0048] High temperature wastewater treatment process such as figure 1 As shown, the purified water A from the stripping tower of the 80°C MTO process is discharged into the precipitation separation system 1, wherein the water quality of the bottom of the stripping tower is as described in Example 1. The same pretreatment process as in Example 1 is used. The quality of the water produced by the process is as described in Example 1.

[0049] The pre-treated wastewater is sent to the ultrafiltration system 3 through the centrifugal pump 2. The pore size of the ultrafiltration membrane is a 19-channel tubular ceramic ultrafiltration membrane of 0.02μm, and the effective membrane area is 1m. 2 , Membrane filtration flux is 100L / m 2 h, the feed water pressure of the ultrafiltration membrane system is 0.15MPa, the recovery rate of the ultrafiltration system is 90%, the ultrafiltration concentrated water is circulated to the sedimentation tank 1, the ultrafiltration water quality is ultra...

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Abstract

The invention relates to a method for treating and reusing high-temperature stripping purified wastewater produced in the process of transferring oxygenated compounds into olefins by using a high-temperature separation membrane. The combination process can effectively remove the impurities such as metal ions and organic micro-molecules and the like in stripping purified water, and the treated purified water in a tower kettle can meet the quality requirements of makeup water for middle and low-pressure boilers or the quality requirements of the makeup water in the MTO process. The invention effectively overcomes the defects exiting in the method for treating and reusing the stripping purified water without condensation in the MTO process, and lowers or reduces the consumption of circulating cooling water in the process of cooling firstly and then treating, thereby saving a large amount of boiler water and recycling the thermal energy of produced high temperature wastewater, and providing a stable and efficient way for high temperature wastewater treatment and reuse of relevant enterprises.

Description

[Technical Field] [0001] The invention relates to the field of wastewater treatment, in particular to a method for treating high-temperature wastewater of an MTO process by using membrane separation technology. [Background technique] [0002] Low-carbon olefins such as ethylene and propylene are important organic chemical raw materials and play a very important role in modern petroleum and chemical industries. Traditionally, the source of ethylene and propylene was mainly steam cracking of hydrocarbons, and the raw material was mainly naphtha. The research and development of methanol production of low-carbon olefins (MTO) is a brand-new process route to produce chemical products from non-petroleum resources. As the technology for producing methanol from coal or natural gas via synthesis gas matures, MTO has become a production route that has attracted much attention. [0003] The chemical reaction equation and thermal effect of using methanol as raw material to produce ethylene a...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F1/44C02F1/52C02F9/04C02F103/36C02F1/66
Inventor 杨永强王娟张新妙李井峰
Owner CHINA PETROLEUM & CHEM CORP
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