CN211111507U - MCR membrane chemical separation device - Google Patents

Abstract

The utility model discloses a MCR membrane chemical separation device, including the MCR reactor, the MCR reactor includes the cell body, the cell body is the cavity seal groove, be equipped with MCR membrane module and perforation aeration pipe in the cell body, the cell body top is equipped with and extends to electrode level gauge in the cell body, MCR membrane module upper end is equipped with and extends to the product water pipe in the cell body outside, be equipped with flushing pipe and manometer on the product water pipe, be equipped with the washing solenoid valve on the flushing pipe, product water pipe one end with MCR membrane module upper end is connected, the product water pipe other end is equipped with the product water pump, the cell body lower extreme is equipped with the mud pipe, be equipped with the sludge pump on the mud pipe. The utility model discloses a MCR reactor is with mud-water separation, through the separation of the muddy water mixed liquid that produces behind the chemical reaction, can separate the mud particle diameter of micron level like this, also can all separate most colloidal state material to can reach fine separation effect.

Description

MCR membrane chemical separation device

Technical Field

The utility model relates to a mud-water separation technical field, in particular to MCR membrane chemical separation device.

Background

In the field of traditional mud-water separation, sedimentation tanks are adopted in the general water treatment industry, and have various forms, such as inclined plate sedimentation tanks, radial flow sedimentation tanks, vertical flow sedimentation tanks, horizontal flow sedimentation tanks and the like. There are also techniques or equipment for separating fine particles with relatively small particle size, such as sand filters, common filters, cloth bag filters, etc. The processing technology in the fields has the defects of large equipment, common effect and the like. In the process of technical development, an air flotation machine is used for replacing precipitation, a disc type filter is used for replacing sand filtration and the like, but still, the method has a plurality of undesirable effects.

SUMMERY OF THE UTILITY MODEL

The to-be-solved technical problem of the utility model is to provide a MCR membrane chemical separation device, solved the not good problem of mud-water separation effect.

In order to solve the technical problem, the utility model discloses a technical scheme does:

the utility model provides a MCR membrane chemical separation device, includes the MCR reactor, the MCR reactor includes the cell body, the cell body is the cavity seal groove, be equipped with MCR membrane module and perforation aeration pipe in the cell body, the cell body top is equipped with and extends to electrode level gauge in the cell body, MCR membrane module upper end is equipped with and extends to the product water pipe in the cell body outside, be equipped with flushing pipe and manometer on the product water pipe, be equipped with on the flushing pipe and wash the solenoid valve, product water pipe one end with MCR membrane module upper end is connected, the product water pipe other end is equipped with produces the water pump, the cell body lower extreme is equipped with the mud pipe, be equipped with the sludge pump on the mud pipe.

Furthermore, a back flushing pipe extending into the tank body is arranged above the tank body, and the back flushing pipe is connected with the perforated aeration pipe.

Further, the perforated aeration pipe is arranged below the MCR membrane module.

Furthermore, a water outlet pipe is connected to the water production pump.

Furthermore, a water outlet flow meter is arranged on the water outlet pipe.

Furthermore, a water outlet valve is arranged on the water outlet pipe.

Furthermore, the number of the water outlet valves is two, and the two water outlet valves are respectively arranged on two sides of the water outlet flow meter.

Furthermore, a water production valve is arranged on the water production pipe between the pressure gauge and the water production pump.

Further, the lower end of the tank body is provided with a sludge collection funnel, and one end of the sludge discharge pipe is arranged at the lower end of the sludge collection funnel.

Further, a dosing system is arranged on one side of the groove body.

By adopting the technical scheme, the mud and water are separated through the MCR reactor, and the mud and water mixed liquor generated after the chemical reaction is separated, so that the particle size of the micron-level sludge particles can be separated, most colloidal substances can be uniformly separated, and a good separation effect can be achieved.

Drawings

Fig. 1 is a schematic plan view of an embodiment of the MCR membrane chemical separation apparatus of the present invention.

Figures and their description:

1. an MCR membrane module; 2. a trough body; 3. perforating an aeration pipe; 4. a sludge collection funnel; 5. a dosing system; 6. back flushing the pipe; 7. an electrode level gauge; 8. a recoil valve; 9. flushing the electromagnetic valve; 10. a flush tube; 11. a pressure gauge; 12. a water production pipe; 13. a water outlet pipe; 14. a water outlet valve; 15. a water outlet flow meter; 16. a water production pump; 17. a sludge pump; 18. a water production valve; 19. a sludge discharge pipe.

Detailed Description

The following describes the present invention with reference to the accompanying drawings. It should be noted that the description of the embodiments is provided to help understanding of the present invention, but the present invention is not limited thereto. In addition, the technical features related to the embodiments of the present invention described below may be combined with each other as long as they do not conflict with each other.

Referring to fig. 1, the utility model provides a pair of MCR membrane chemical separation device, including the MCR reactor, the MCR reactor includes cell body 2, cell body 2 is the cavity seal groove, be equipped with MCR membrane module 1 and perforation aeration pipe 3 in the cell body 2, 2 tops of cell body are equipped with and extend to electrode level gauge 7 in the cell body 2, 1 upper ends of MCR membrane module are equipped with and extend to the product water pipe 12 in the 2 outsides of cell body, be equipped with flushing pipe 10 and manometer 11 on the product water pipe 12, be equipped with washing solenoid valve 9 on the flushing pipe 10, produce water pipe 12 one end with 1 upper end of MCR membrane module is connected, the product water pipe 12 other end is equipped with product water pump 16, 2 lower extremes of cell body are equipped with mud pipe 19, be equipped with sludge pump 17 on the mud pipe 19.

This technical scheme passes through the MCR reactor with mud-water separation, through the separation of the muddy water mixed liquor that produces behind the chemical reaction, can separate the mud particle diameter of micron level like this, also can all separate most colloid state material to can reach fine separation effect.

The inside of the tank body 2 is a hollow fiber membrane, the center is a hollow structure, the periphery of the hollow structure is formed by drawing PVDF material, and therefore sealing protection is performed through the PVDF material, the overall toughness can be increased, the friction coefficient is reduced, the corrosion resistance, the aging resistance, the weather resistance and the irradiation resistance are improved, and the use performance of a product is guaranteed.

A back flushing pipe 6 extending into the tank body 2 is arranged above the tank body 2, and the back flushing pipe 6 is connected with the perforated aeration pipe 3. A recoil valve 8 is arranged on the recoil pipe 6. The aeration of the perforated aeration pipe 3 is controlled by a recoil valve 8.

The perforated aeration pipe 3 is arranged below the MCR membrane module 1. This can improve the sludge-water separation effect.

The water producing pump 16 is connected with a water outlet pipe 13. And a water outlet flowmeter 15 is arranged on the water outlet pipe 13. Thus, the discharge amount after sewage treatment can be counted.

And a water outlet valve 14 is arranged on the water outlet pipe 13. The number of the water outlet valves 14 is two, and the two water outlet valves 14 are respectively arranged on two sides of the water outlet flow meter 15. This reduces the failure rate of the water production flow meter 15.

A water production valve 18 is arranged on the water production pipe 12 between the pressure gauge 12 and the water production pump 16. This reduces the rate of failure of the water producing pump.

The lower end of the tank body 2 is provided with a sludge collecting funnel 4, and one end of the sludge discharge pipe 19 is arranged at the lower end of the sludge collecting funnel 4. Thus facilitating the sedimentation, collection and discharge of the sludge.

A dosing system 5 is arranged on one side of the tank body 2. The medicine adding system 5 can automatically add medicine into the tank body 2 according to the use requirement.

To sum up, the utility model discloses a MCR reactor is with mud-water separation, through the separation of the muddy water mixed liquid that produces behind the chemical reaction, can separate micron level's sludge particle diameter like this, also can all separate most colloid attitude material to can reach fine separation effect.

In the description of the present invention, it is to be understood that the terms "center", "longitudinal", "lateral", "length", "width", "thickness", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", "clockwise", "counterclockwise", "axial", "radial", "circumferential", and the like, indicate the orientation or positional relationship indicated based on the drawings, and are only for convenience of description and simplicity of description, and do not indicate or imply that the device or element referred to must have a particular orientation, be constructed and operated in a particular orientation, and therefore, should not be construed as limiting the present invention.

Furthermore, the terms "first", "second" and "first" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance or implicitly indicating the number of technical features indicated. Thus, a feature defined as "first" or "second" may explicitly or implicitly include at least one such feature. In the description of the present invention, "a plurality" means at least two, e.g., two, three, etc., unless specifically limited otherwise.

In the present invention, unless otherwise expressly stated or limited, the terms "mounted," "connected," and "fixed" are to be construed broadly and may, for example, be fixedly connected, detachably connected, or integrally formed; can be mechanically or electrically connected; they may be directly connected or indirectly connected through intervening media, or they may be connected internally or in any other suitable relationship, unless expressly stated otherwise. The specific meaning of the above terms in the present invention can be understood according to specific situations by those skilled in the art.

In the present application, unless expressly stated or limited otherwise, the first feature may be directly on or directly under the second feature or indirectly via intermediate members. Also, a first feature "on," "over," and "above" a second feature may be directly or diagonally above the second feature, or may simply indicate that the first feature is at a higher level than the second feature. A first feature being "under," "below," and "beneath" a second feature may be directly under or obliquely under the first feature, or may simply mean that the first feature is at a lesser elevation than the second feature.

In the description herein, references to the description of the term "one embodiment," "some embodiments," "an example," "a specific example," or "some examples," etc., mean that a particular feature, structure, material, or characteristic described in connection with the embodiment or example is included in at least one embodiment or example of the invention. In this specification, the schematic representations of the terms used above are not necessarily intended to refer to the same embodiment or example. Furthermore, the particular features, structures, materials, or characteristics described may be combined in any suitable manner in any one or more embodiments or examples. Furthermore, various embodiments or examples and features of different embodiments or examples described in this specification can be combined and combined by one skilled in the art without contradiction.

Although embodiments of the present invention have been shown and described, it is understood that the above embodiments are exemplary and should not be construed as limiting the present invention, and that variations, modifications, substitutions and alterations can be made to the above embodiments by those of ordinary skill in the art without departing from the scope of the present invention.

Claims (10)

1. The utility model provides a MCR membrane chemical separation device, a serial communication port, including the MCR reactor, the MCR reactor includes the cell body, the cell body is the cavity seal groove, be equipped with MCR membrane module and perforation aeration pipe in the cell body, the cell body top is equipped with and extends to electrode level gauge in the cell body, MCR membrane module upper end is equipped with and extends to the product water pipe in the cell body outside, be equipped with flushing pipe and manometer on the product water pipe, be equipped with on the flushing pipe and wash the solenoid valve, product water pipe one end with MCR membrane module upper end is connected, the product water pipe other end is equipped with the product water pump, the cell body lower extreme is equipped with the mud pipe, be equipped with the sludge pump on the mud pipe.

2. An MCR membrane chemical separation device according to claim 1, wherein a back flushing pipe extending into the tank body is arranged above the tank body, and the back flushing pipe is connected with the perforated aeration pipe.

3. An MCR membrane chemical separation device according to claim 1 wherein the perforated aeration pipe is provided below the MCR membrane module.

4. An MCR membrane chemical separation device according to claim 1, wherein the water production pump is connected with a water outlet pipe.

5. An MCR membrane chemical separation device according to claim 4, wherein the water outlet pipe is provided with a water outlet flow meter.

6. An MCR membrane chemical separation device according to claim 5, wherein the water outlet pipe is provided with a water outlet valve.

7. An MCR membrane chemical separation device according to claim 6, wherein the number of the water outlet valves is two, and the two water outlet valves are respectively arranged on two sides of the water outlet flow meter.

8. An MCR membrane chemical separation device according to claim 1, wherein a water production valve is arranged on the water production pipe between the pressure gauge and the water production pump.

9. The MCR membrane chemical separation device as claimed in claim 1, wherein a sludge collection funnel is arranged at the lower end of the tank body, and one end of the sludge discharge pipe is arranged at the lower end of the sludge collection funnel.

10. The MCR membrane chemical separation device of claim 1, wherein a dosing system is arranged on one side of the tank body.

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