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Composite membrane for mabr and preparation method thereof

A composite membrane and fiber membrane technology, applied in the field of MABR composite membrane, can solve the problems of gas flux decline, low oxygen flux, and hydrophobic performance decline.

Active Publication Date: 2021-06-15
SHENYANG ACAD OF ENVIRONMENTAL SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] Membrane materials suitable for membrane aerated biofilm reactors can be roughly divided according to their surface properties and structures: hydrophobic microporous membranes and dense non-porous silica gel membranes. Among them, hydrophobic microporous membranes have the following disadvantages: (1) Due to its low bubble point pressure, the transfer of gas through the membrane pores can easily destroy the biofilm layer formed on the membrane surface; (2) During the growth of the biofilm, some biological debris from cells shed will adhere to the membrane surface, and even further block the pores on the surface, resulting in an increase in the gas mass transfer resistance of the membrane, a decrease in the gas flux, and finally the growth of the biofilm is affected due to insufficient oxygen supply; (3) some proteins and biological debris will make The hydrophobic performance of the membrane surface decreases and the liquid enters the membrane, so this membrane is not suitable for long-term operation
Although the dense non-porous silica membrane has certain advantages in bubble point pressure and pollution prevention, its low oxygen flux limits its application in MABR.

Method used

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Examples

Experimental program
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Effect test

Embodiment 1

[0023] A composite membrane for MABR proposed by the present invention includes a composite hollow fiber membrane and multi-dimensional holes arranged on the composite hollow fiber membrane;

[0024] Its preparation method comprises the following steps:

[0025] S1: Put the polyvinylidene fluoride raw material and the 5% diluent of the polyvinylidene fluoride raw material in the reaction kettle, and melt at a high temperature at the same time, and control the heating temperature at 120°C;

[0026] S2: After complete melting, keep the temperature of the reactor at 60°C, stand in the reactor for defoaming, and start spinning after standing for 3 hours;

[0027] S3: Under the traction of the take-up wheel, the spun membrane filaments are extracted into the 70% mass ratio of polyvinylidene fluoride raw materials for extraction, the take-up speed is 400m / min, the cooling temperature is 30°C, and phase separation occurs during cooling The phenomenon forms pores, and the composite m...

Embodiment 2

[0031] A composite membrane for MABR proposed by the present invention includes a composite hollow fiber membrane and multi-dimensional holes arranged on the composite hollow fiber membrane;

[0032] Its preparation method comprises the following steps:

[0033] S1: Put the polyvinylidene fluoride raw material and the 5% diluent of the polyvinylidene fluoride raw material in the reaction kettle, and melt at a high temperature at the same time, and control the heating temperature at 130°C;

[0034] S2: After complete melting, keep the temperature of the reactor at 65°C, stand in the reactor for defoaming, and start spinning after standing for 3.5 hours;

[0035] S3: Under the traction of the take-up wheel, the spun film filaments are extracted into the 70% mass ratio of polyvinylidene fluoride raw material extraction solution, the take-up speed is 450m / min, the cooling temperature is 35°C, and phase separation occurs after cooling The phenomenon forms pores, and the composite ...

Embodiment 3

[0039] A composite membrane for MABR proposed by the present invention includes a composite hollow fiber membrane and multi-dimensional holes arranged on the composite hollow fiber membrane;

[0040] Its preparation method comprises the following steps:

[0041] S1: Put the polyvinylidene fluoride raw material and the 5% diluent of the polyvinylidene fluoride raw material in the reaction kettle, and melt at a high temperature at the same time, and control the heating temperature at 150°C;

[0042] S2: After complete melting, keep the temperature of the reactor at 70°C, stand in the reactor for defoaming, and start spinning after standing for 4 hours;

[0043] S3: Under the traction of the take-up wheel, the spun film filaments are extracted into the 70% mass ratio of polyvinylidene fluoride raw materials for extraction, the take-up speed is 500m / min, the cooling temperature is 45°C, and phase separation occurs during cooling The phenomenon forms pores, and the composite membr...

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Abstract

The present invention relates to the technical field of MABR composite membranes, in particular to a composite membrane for MABR and a preparation method thereof, including composite hollow fiber membranes and multi-dimensional holes arranged on the composite hollow fiber membranes, and the preparation method thereof comprises the following steps: polyvinylidene fluoride The diluent of 5% mass ratio of ethylene raw material and polyvinylidene fluoride raw material is placed in the reactor and melted at a high temperature at the same time; silk; under the traction of the take-up wheel, the spun film silk enters the extraction solution of 70% mass ratio of the polyvinylidene fluoride raw material for extraction, and the phenomenon of phase separation occurs during cooling to form holes, and the composite film for MABR is obtained. Throughout the experiment, by controlling the content of polyvinylidene fluoride, types of diluent and extractant, heating and standing temperature, winding rate and cooling temperature, etc., the properties of hollow fiber membrane surface pore morphology and membrane wall thickness were controlled.

Description

technical field [0001] The invention relates to the technical field of MABR composite membranes, in particular to a composite membrane for MABR and a preparation method thereof. Background technique [0002] Membrane-aerated biofilm reactor (membrane-aerated biofilmreactor, MABR) is the product of the combination of membrane technology and biofilm technology. This technology supplies oxygen through a gas-permeable membrane. Oxygen enters the outside of the lumen through the micropores on the membrane wall to achieve bubble-free aeration. The mass transfer efficiency of bubble-free aeration is high, and the oxygen utilization rate can be close to 100%, which is 5 to 7 times that of traditional aeration. [0003] The membrane material of MABR can be used as a carrier, and a microbial film can be formed on the surface of the membrane. The oxygen from the inside of the membrane lumen diffuses from the inside of the biofilm to the outside, and the substrate from the sewage diffu...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D67/00B01D69/12B01D69/08B01D69/02C02F3/12
CPCB01D67/0002B01D69/02B01D69/087B01D69/12C02F3/1268Y02W10/10
Inventor 张磊魏春飞赵勇娇王允妹单连斌
Owner SHENYANG ACAD OF ENVIRONMENTAL SCI
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