JP5119989B2 - Storage method of solid-liquid separation membrane - Google Patents

Description

  The present invention relates to a method for storing a separation membrane used in an apparatus that separates activated sludge and treated water from a solid-liquid membrane after operation is stopped.

  The membrane separation activated sludge method in which activated sludge and treated water are separated into solid and liquid by a membrane has been used in facilities for purifying sewage and wastewater. Although facilities that perform such a membrane separation activated sludge process have facilities that operate throughout the year, they operate only for a few months during a specific period of the year, such as when used for wastewater treatment in resort areas. There are also such facilities. However, depending on the type of separation membrane to be used, once it is placed in water, it may be necessary to keep it in a wet state after that in order to maintain solid-liquid separation performance. That is, in the case of such a separation membrane, the membrane surface structure is adversely affected by making it dry, and membrane performance is degraded. Therefore, in the membrane treatment equipment as described above, it is desirable to store the membrane processing equipment in such a state that it does not damage the membrane or the like when the equipment is not in operation and can exhibit high membrane performance at the time of restart. ing.

  Therefore, as an actual storage method, it can be considered that water is stored in the tank even after the operation is stopped, and the separation membrane element is stored therein. However, in winter, the water in the tank freezes due to low temperatures, and there is a concern that the separation membrane itself may be adversely affected by water expansion during freezing. As another storage method, it is also conceivable to store the entire membrane element in a sealed non-permeable polymer bag or the like so as not to dry the membrane surface of the separation membrane. However, the preparation and packing of the sealed bag are complicated and not practical.

In addition, as a preservation solution for storing the separation membrane in a wet state for a long time,
Patent Document 1 proposes an aqueous solution containing benzoic acid and / or benzoate in a range of 0.05 to 0.5% by mass. This preservation solution is highly safe and has a high bactericidal effect against bacteria and sputum, but it must be stored by immersing the separation membrane, and it is installed in a solid-liquid separation device for activated sludge treated water. It is difficult to apply to storage of used separation membranes.

  Further, as a method for producing a wet semipermeable membrane made of polyamide, polyimide, polysulfone, and drying and storing it, a method of treating it with an aqueous solution of a polyhydric alcohol such as glycerin and then drying and storing the patent document. 2 is disclosed. However, this dry storage method is intended to store unused reverse osmosis membranes after production, and it is difficult to apply this method as it is to dry storage of used solid-liquid separation membranes. It is.

JP 2007-63222 A JP 58-156307 A

  Therefore, the present invention provides a membrane performance without damaging the separation membrane when storing the separation membrane used in the apparatus for separating the activated sludge and the treated water in a solid-liquid membrane, in a dry state after the operation is stopped. An object of the present invention is to provide a film storage method that does not lower the temperature.

In order to achieve this object, the storage method of the solid-liquid separation membrane of the present invention is specified as follows.
1. When storing activated sludge and installed treated water to solid-liquid membrane separation to the device isolation film used in a dry state, washing the membrane secondary side of the solid-liquid membrane separation device separating film is placed Kiyoshi liquid was allowed to flow by static置洗 Kiyoshi and then a hydrophilic membrane surface by injecting aqueous solution from the membrane secondary side comprising at least one parent water agent selected from the group consisting of surfactant and a polyhydric alcohol A method for storing a solid-liquid separation membrane, wherein the separation membrane is dried and stored after conversion .

  When the method of the present invention is applied, raw water such as organic sewage such as sewage and factory wastewater is treated with activated sludge in a biological treatment tank, and a treatment liquid mixture containing activated sludge is subjected to membrane separation treatment with a submerged separation membrane in the treatment tank. Then, when suspending the membrane separation activated sludge treatment equipment that takes the form of aeration from the bottom of the submerged separation membrane, the separation membrane installed and used in the solid-liquid membrane separation device of activated sludge treated water is dried. It can be stored in a dry state, and it can be stored in a state that does not damage the surface of the separation membrane during drying storage and can exhibit high membrane performance during re-operation. Become.

  The separation membrane dry storage method of the present invention is to treat raw water such as organic sewage such as sewage and factory wastewater in the biological treatment tank, and treat the mixed liquid containing the activated sludge in the treatment tank. This is applied to a separation membrane that has been used by being immersed in water in a facility for membrane separation activated sludge treatment in which the membrane is subjected to a membrane separation treatment and aerated from the lower part of the submerged separation membrane.

  An example of a wastewater treatment apparatus to which the method of the present invention can be applied is shown in FIG. This waste water treatment apparatus includes an aeration tank (biological treatment tank) 2 for performing biological treatment by introducing activated sludge, a raw water supply pump 3 for supplying raw water (waste water) 1 to the aeration tank 2, and biologically treated activated sludge. There are provided a membrane separation device 4 for solid-liquid separation of the mixed liquid, a suction pump 5 for sucking the membrane permeate separated by the membrane separation device, and a sludge extraction pump 6 for extracting excess sludge in the aeration tank. . The membrane separation device 4 is immersed in the liquid in the aeration tank 2, and air is supplied below the membrane separation device to advance the aerobic treatment and fine bubbles for cleaning the membrane surface. An air diffuser 8 is provided, and air is supplied to the air diffuser by an air supply device 7.

  As the aeration tank 2, if the activated sludge is stored and the membrane separation device 4 can be immersed in the mixed liquid of the water to be treated and the activated sludge, the size and material are not particularly limited. For example, a concrete tank, A fiber reinforced plastic tank or the like is preferably used. Moreover, the tank structure by which the inside of the aeration tank was divided | segmented into plurality may be sufficient, and you may decide to immerse the membrane separation apparatus 4 in the one part tank among the tank divided | segmented into the plurality.

  The raw water supply pump 3 is not particularly limited as long as the raw water (waste water) 1 can be fed to the aeration tank 2, and is not limited to a vortex pump, a diffuser pump, a vortex mixed flow pump, a mixed flow pump, a piston. A pump, plunger pump, diaphragm pump, gear pump, screw pump, vane pump, cascade pump, jet pump, or the like can be used.

  The membrane separation device 4 is a device in which a solid-liquid separation membrane is disposed, and the separation membrane includes a hollow fiber membrane type and a flat membrane type. In order to improve the handleability and physical durability of the filtration membrane (separation membrane), for example, a flat membrane element having a structure in which a flat membrane is adhered to both sides of the frame with a filtrate channel material sandwiched between them is provided. desirable. The structure of the flat membrane element is not limited to the above.

  The suction pump 5 is a pump that sucks the membrane permeated permeated water in order to give a suction force necessary for the membrane filtration solid-liquid separation by the membrane separation device 4 and is not particularly limited in shape, but is usually decompressed. A pump that is operated at 300 kPa or less from the state is used. Further, instead of the suction pump, it is also possible to perform membrane filtration using the natural water head difference as a driving force.

  The sludge extraction pump 6 is a pump for periodically extracting excess sludge in order to keep the MLSS concentration in the aeration tank constant. There is no particular limitation as long as sludge with high viscosity can be fed. The MLSS concentration in the membrane separation activated sludge method is about 3,000 to 20,000 mg / L, but the MLSS concentration for maintaining a more stable membrane filtration flux is about 5,000 to 15,000 mg / L.

  The air supply device 7 is a device that blows compressed air, and generally a blower, a compressor, or the like is used. The blown air is sent out as bubbles from the diffuser 8 into the tank, and the bubbles clean the separation membrane surface of the membrane separator, and oxygen necessary for biological treatment (aerobic treatment) in the liquid. Supplied. The air diffuser 8 is not particularly limited as long as the air diffuser can generate bubbles for cleaning the membrane surface, but an air diffuser having an air discharge hole in a PVC or stainless steel pipe is used. Usually used. In addition, a porous rubber, ceramic, a diffuser tube using a membrane, and the like can be used.

  The cleaning agent storage tank 9 is a tank for storing a medicine for cleaning the separation membrane, and the material is not particularly defined as long as it is resistant to the medicine to be used. For example, plastics such as polyethylene can be used.

  The hydrophilizing agent storage tank 10 is a tank for storing a chemical for hydrophilizing the membrane surface of the separation membrane, and the material is not particularly defined as long as it is resistant to the chemical used. . For example, plastics such as polyethylene can be used.

  According to the method of the present invention, when the separation membrane installed and used in an apparatus for separating activated sludge and treated water into a solid-liquid membrane is stored in a dry state, the separation membrane is washed with a washing liquid, and then contains a hydrophilizing agent. After hydrophilizing the membrane surface with an aqueous solution, the separation membrane is dried and stored.

  Specifically, the separation membrane cleaning and hydrophilization treatment are performed by allowing the cleaning liquid to flow from the membrane secondary side of the solid-liquid separation apparatus in which the separation membrane is installed, and then allowing the hydrophilizing agent to flow. What is necessary is just to carry out by the method of inject | pouring the aqueous solution containing from the film | membrane secondary side and hydrophilizing a film surface. When this method is carried out in the apparatus shown in FIG. 1, the cleaning liquid is separated from the cleaning agent storage tank 9 while the activated sludge mixed liquid remains in the immersion tank. It inject | pours into the film | membrane secondary side of the apparatus 4, and the stain | pollution | contamination adhering to the film | membrane secondary side and the film | membrane surface is wash | cleaned and removed. This cleaning may be performed, for example, with an aqueous solution containing sodium hypochlorite at a concentration of about 1,000 mg / L to 5,000 mg / L for contamination of organic substances. In addition, for contamination with inorganic substances, washing may be performed with an aqueous solution containing oxalic acid at a concentration of about 0.1% to 10%. Washing may be usually performed by leaving the solution for 2 to 3 hours in a state where the cleaning liquid is allowed to flow into the membrane secondary side. In addition, you may employ | adopt methods other than the above about the washing | cleaning method. The type, concentration, temperature, and the like of the cleaning agent contained in the cleaning liquid are preferably selected in consideration of the degree and type of dirt adhering to the membrane, the material of the separation membrane, and the like. After immersion cleaning with cleaning agent-containing water, if necessary, the cleaning agent may be removed by rinsing with water.

  Next, an aqueous solution containing a hydrophilizing agent is injected from the hydrophilizing agent storage tank 10 to the secondary side of the separation membrane, and the separation membrane is hydrophilized. As a chemical | medical agent used for a hydrophilization process, surfactant (for example, fatty acid ester solution and a product: TRITON X-100 (Dow Chemical) etc.) and a polyhydric alcohol (for example, glycerol solution) should just be used. It is preferable to select an optimum concentration and an optimum concentration for the material of the separation membrane used. Then, after the hydrophilic treatment, it is dried by natural drying or the like and then stored.

  When storing, it is desirable to store it in an environment that does not damage the separation membrane as much as possible, such as storing it in a cool and dark place avoiding direct sunlight.

  In the above embodiment, the method of injecting the cleaning agent from the secondary side of the film and further injecting the hydrophilizing agent has been described. However, cleaning and hydrophilization treatment may be performed by other methods.

  For example, the separation membrane element taken out from the solid-liquid membrane separation apparatus after the operation stop may be immersed in a cleaning solution for cleaning, and then immersed in an aqueous solution containing a hydrophilicizing solution to perform a hydrophilic treatment. Specifically, an aqueous solution containing a cleaning agent is stored in the tank after discharging the activated sludge treated water in the aeration tank in which the solid-liquid membrane separation apparatus using the separation membrane was installed, and then the tank is washed. The inside may be replaced with an aqueous solution containing a hydrophilizing agent and subjected to a hydrophilic treatment. Separately, a tank in which the cleaning liquid is stored and a tank in which the liquid of the hydrophilizing agent is stored are prepared, and the separation membrane element removed from the solid-liquid separation device is sequentially immersed therein to thereby form a membrane. The membrane may be washed and the membrane may be hydrophilized.

Hereinafter, the present invention will be described more specifically with reference to examples. In addition, this invention is not limited to the aspect as described in an Example.
In this example, the separation membrane element was taken out from the solid-liquid membrane separation apparatus used for the membrane separation activated sludge treatment, and the following three conditions were carried out for comparison.

(Condition 1) Cleaning with chemicals (2 hours) → Hydrophilization (2 hours) → Dry storage (6 months) → Operation restart (Condition 2) Cleaning with chemicals (2 hours) → Dry storage (6 months) → Operation restart (Condition 3) Cleaning with chemicals (2 hours) → Dry storage (6 months) → Hydrophilization treatment (2 hours) → Resumption of operation

  The specific operation procedure when Condition 1 is implemented is shown in the flowchart of FIG. The specifications at that time are shown in Table 1.

The water permeability of the separation membrane was measured immediately after cleaning with chemicals and immediately after restarting operation under each condition.
Measurement of water permeability: The separation membrane element is immersed in the water in the immersion tank, and a constant water pressure is applied to the surface of the separation membrane by giving a constant water head difference to the filtered water outlet, and the water permeability at a predetermined time is measured.

  The obtained water permeation value was expressed as a ratio to the water permeation amount after chemical cleaning, and the water permeation performance was compared. The results are shown in FIG.

  As shown in FIG. 3, when the product was dried and stored as it was after chemical cleaning as in Condition 2, the water permeability after restarting the operation was reduced to about half of the original. Even if the hydrophilization treatment was performed again after dry storage as in Condition 3, the water permeation performance recovered only to about 80%. On the other hand, by performing the operation under Condition 1 according to the method of the present invention, the water permeation performance was 95%, which was almost restored to the original state.

  The method of the present invention is a membrane separation activated sludge method that treats sewage such as sewage in a biological treatment tank and performs membrane separation treatment with a submerged separation membrane in a treatment tank. It can be applied to store the separation membrane in a dry state when the operation is suspended seasonally or periodically.

It is an apparatus schematic diagram which shows an example of the apparatus for implementing the membrane separation activated sludge processing method using a solid-liquid separation membrane. It is the flowchart which showed the operation procedure in an Example. It is a figure which shows the water-permeable performance ratio of the separation membrane in an Example.

Explanation of symbols

1: Raw water (waste water)
2: Aeration tank (biological treatment tank)
3: Raw water supply pump 4: Membrane separation device 5: Suction pump 6: Sludge extraction pump 7: Air supply device 8: Air diffuser 9: Cleaning agent storage tank 10: Hydrophilizing agent storage tank

Claims (1)

When storing activated sludge and installed treated water to solid-liquid membrane separation to the device isolation film used in a dry state, washing the membrane secondary side of the solid-liquid membrane separation device separating film is placed Kiyoshi liquid was allowed to flow by static置洗 Kiyoshi and then a hydrophilic membrane surface by injecting aqueous solution from the membrane secondary side comprising at least one parent water agent selected from the group consisting of surfactant and a polyhydric alcohol A method for storing a solid-liquid separation membrane, wherein the separation membrane is dried and stored after conversion.

Images