CN212504207U

CN212504207U - Membrane lotus root up-flow anaerobic sludge bed reactor system

Info

Publication number: CN212504207U
Application number: CN202020714321.9U
Authority: CN
Inventors: 靖朝森; 邵婷
Original assignee: Shanghai Fushen Environmental Technology Development Co ltd
Current assignee: Shanghai Fushen Environmental Technology Development Co ltd
Priority date: 2020-04-30
Filing date: 2020-04-30
Publication date: 2021-02-09
Anticipated expiration: 2030-04-30

Abstract

The utility model discloses a membrane lotus root up-flow anaerobic sludge bed reactor system, which comprises a tempering tank, an anaerobic reactor and a water inlet pipeline, wherein the anaerobic reactor comprises a shell, the shell is sequentially provided with a water distributor system, a sludge expansion area, a composite membrane fixed bed reaction area, a triphase separator and a methane collection chamber from bottom to top, the composite membrane fixed bed reaction area is arranged along the ascending water flow direction, the overall hydraulic flow state of the whole anaerobic reactor cannot be influenced, a large amount of anaerobic sludge can be attached to the composite membrane fixed bed reaction area, the methane generated by the anaerobic reaction can generate strong local turbulence in the process of ascending through a fixed membrane gap, the contact and mass transfer effects of the waste water and anaerobic microorganisms attached to a membrane bed are enhanced, thereby ensuring the degradation effect of organic pollutants in the fixed membrane bed area, and simultaneously slowing down the ascending flow rate of the sludge in the sludge expansion area and changing the, has certain effect of stopping the sludge from rising, thereby ensuring the sludge concentration in the sludge expansion area.

Description

Membrane lotus root up-flow anaerobic sludge bed reactor system

Technical Field

The utility model relates to a water pollution deals with the field, especially relates to a membrane lotus root up-flow anaerobic sludge bed reactor system.

Background

In recent years, the development speed of chemical industry, pharmaceutical industry and other industries in China is continuously accelerated, particularly the chemical industry and the pharmaceutical industry, the sewage discharge amount is large, the treatment difficulty is high, the environment is seriously influenced, and the development of enterprises is also seriously influenced under the situation that the environmental protection requirement is increasingly strict. At present, China highly attaches importance to environmental protection, the emission requirements of waste water, waste gas and the like discharged by industrial enterprises are stricter and stricter, and the investment of the enterprises in the aspect of environmental protection is larger and larger. However, most of the systematic solutions for wastewater treatment in the pharmaceutical and chemical industry fields in China cannot meet the requirements of enterprises in the national team, and many enterprises cannot find the optimal solution, so that many enterprises often cannot obtain the optimal systematic treatment solution when selecting the wastewater treatment process, and the problems of high investment cost, high running cost and the like of environmental protection treatment of most pharmaceutical and chemical enterprises are caused.

The anaerobic biological treatment technology is a preferred pretreatment process for treating high-concentration organic wastewater at present, and the process is a low-energy-consumption sewage treatment mode in which organic pollutants in sewage are decomposed, metabolized and digested by anaerobic microorganisms under an anaerobic condition so as to purify the wastewater. In recent years, anaerobic sewage treatment processes have been developed rapidly, and various new processes and new methods have been developed, but basically, attention has been paid to high-load anaerobic reactors such as internal circulation anaerobic reactors (IC). High-speed anaerobic reactors basically achieve good treatment effects based on anaerobic granular sludge, but not all industrial wastewater can form granular sludge which is relied on by high-speed anaerobic reactors, especially wastewater in pharmaceutical and most chemical industries, because the wastewater components are complex, the water quality and water quantity change is large, granular sludge can hardly form, flocculent anaerobic sludge is taken as a main part, and the up-flow anaerobic sludge bed (UASB) process generally adopted in the market at present has the difficulties of poor treatment effect, large operation and maintenance difficulty and the like of an anaerobic system due to serious sludge loss, non-uniform water distribution and the like due to design problems. Therefore, most of domestic upflow anaerobic sludge blanket processes are provided with a large sedimentation tank in the subsequent stage so as to return the lost anaerobic sludge to the anaerobic reactor to maintain the normal operation of the anaerobic reactor, but because the anaerobic lost sludge and water mixture also contains tiny methane bubbles attached to the sludge, the sedimentation effect of the anaerobic sludge is not ideal, and the addition of the vacuum lifting device not only increases the complexity of operation and maintenance, but also is difficult to achieve the expected effect.

As is well known, industrial wastewater in the chemical and pharmaceutical industries and the like has high concentration and generally weak biodegradability, and the UASB, EGSB or IC anaerobic process which is generally adopted is difficult to normally operate under the feasible condition of the anaerobic process. In addition, UASB anaerobic reactors have other disadvantages, such as: the suspended matters in the inlet water need to be properly controlled and are not too high, generally controlled at 500mg/l, the water distribution of a conventional perforated pipe causes a short flow phenomenon in a sludge bed, the treatment effect of the system is influenced, and the system is sensitive to the change of water quality and load and has poor impact resistance. Although the conventional UASB anaerobic process remains the primary pretreatment process of choice for most businesses, the problems with this process have not been improved or enhanced for many years.

SUMMERY OF THE UTILITY MODEL

An object of the utility model is to provide a membrane lotus root up-flow anaerobic sludge bed reactor system that suitability is strong.

The utility model adopts the technical proposal that:

a membrane-lotus root upflow anaerobic sludge blanket reactor system, comprising:

the tempering tank comprises a tank body, a sewage inlet is formed in the tank body, and a jet mixer and a jet ejector are arranged on the inner wall of the tank body;

the anaerobic reactor comprises a closed shell, and the shell is sequentially provided with a water distributor system, a sludge expansion area, a double-film fixed bed reaction area, a three-phase separator and a methane collection chamber from bottom to top;

the bottom of the tempering tank is communicated with the bottom of the anaerobic reactor through a water inlet pipeline, a feed pump is arranged on the water inlet pipeline, and the feed pump lifts the wastewater after being tempered by the tempering tank into a water distributor system;

the three-phase separator comprises a main body, wherein a degassing precipitation area, a mud-water separation area, a sludge precipitation area and a submerged water collection system are arranged in the main body, and an opening is formed in the bottom of the main body.

Further as the utility model discloses technical scheme's improvement, the water-locator system adopts double-line pulse water distribution system.

Further as the utility model discloses technical scheme's improvement, anaerobic reactor's bottom still is provided with row mud system.

Further conduct the utility model discloses technical scheme's improvement, be provided with flowmeter, temperature sensor, pH sensor on the inlet channel.

Further conduct the utility model discloses technical scheme's improvement, be provided with the manhole on the anaerobic reactor, the manhole includes first manhole and second manhole, first manhole is located the lateral wall of anaerobic reactor bottom, the second manhole is located anaerobic reactor's top.

Further conduct the utility model discloses technical scheme's improvement still includes the circulation system, the circulation system is with anaerobic reactor effluent and the waste water mixed cycle of quenching and tempering pond.

Further conduct the utility model discloses technical scheme's improvement, the main part is leaks hopper-shaped, the bottom toper district of main part sets up the sludge settling zone, the top in sludge settling zone sets up the degasification settling zone and the muddy water disengagement zone of left and right partition setting, submerged play water collecting system sets up under anaerobic reactor's water line.

Further as the utility model discloses technical scheme's improvement, the submerged play water collecting system adopts the submerged outlet pipe.

Further as the utility model discloses technical scheme's improvement still includes the backwash pipe, the backwash pipe sets up respectively in mud sedimentation district and compound membrane fixed bed reaction zone.

Further as the utility model discloses technical scheme's improvement still includes marsh gas communicating pipe, marsh gas communicating pipe intercommunication marsh gas collection chamber and quenching and tempering pond, the top in quenching and tempering pond is provided with the marsh gas export.

The utility model has the advantages that: the membrane coupling up-flow anaerobic sludge bed reactor system comprises a conditioning tank, an anaerobic reactor and a water inlet pipeline, wherein the anaerobic reactor comprises a closed shell, the shell is sequentially provided with a water distributor system, a sludge expansion area, a composite membrane fixed bed reaction area, a three-phase separator and a methane collection chamber from bottom to top, the composite membrane fixed bed reaction area is arranged along the ascending water flow direction, the total hydraulic flow state of the whole anaerobic reactor cannot be influenced, a large amount of anaerobic sludge can be attached to the composite membrane fixed bed reaction area, the methane generated by anaerobic treatment can generate strong local turbulence in the ascending process through a fixed membrane gap, the contact and mass transfer effects of waste water and anaerobic microorganisms attached to a membrane bed are enhanced, the degradation effect of organic pollutants in the fixed membrane bed area is ensured, meanwhile, the ascending flow rate of the sludge in the sludge expansion area can be slowed down and the ascending way can be changed due to the configuration of the composite membrane fixed, the anaerobic sludge reactor has a certain blocking effect on the sludge rising, so that the sludge concentration of the sludge expansion zone is ensured, and meanwhile, the three-phase separator arranged above the reaction zone of the composite membrane fixed bed can effectively realize the separation of flocculent anaerobic sludge from biogas and water, so that high-concentration anaerobic sludge can be reserved in the anaerobic reactor.

Drawings

The present invention will be further explained with reference to the accompanying drawings:

fig. 1 is a schematic structural diagram of an embodiment of the present invention.

Detailed Description

This section will describe in detail the embodiments of the present invention, preferred embodiments of the present invention are shown in the attached drawings, which are used to supplement the description of the text part of the specification with figures, so that one can intuitively and vividly understand each technical feature and the whole technical solution of the present invention, but they cannot be understood as the limitation of the protection scope of the present invention.

In the description of the present invention, it should be understood that the orientation or positional relationship indicated with respect to the orientation description, such as up, down, front, rear, left, right, etc., is based on the orientation or positional relationship shown in the drawings, and is only for convenience of description and simplification of description, and does not indicate or imply that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and thus, should not be construed as limiting the present invention.

In the description of the present invention, a plurality of means are one or more, a plurality of means are two or more, and the terms greater than, less than, exceeding, etc. are understood as not including the number, and the terms greater than, less than, within, etc. are understood as including the number. If the first and second are described for the purpose of distinguishing technical features, they are not to be understood as indicating or implying relative importance or implicitly indicating the number of technical features indicated or implicitly indicating the precedence of the technical features indicated.

In the description of the present invention, unless there is an explicit limitation, the words such as setting, installation, connection, etc. should be understood in a broad sense, and those skilled in the art can reasonably determine the specific meanings of the above words in combination with the specific contents of the technical solution.

Referring to fig. 1, a membrane coupling upflow anaerobic sludge blanket reactor system comprises a conditioning tank 1, an anaerobic reactor 2 and a water inlet pipeline 3. The membrane lotus root up-flow anaerobic sludge bed reactor system has no maintenance requirement, and the problem of filler blockage of other filler anaerobic reactors can be avoided.

Wherein, the tempering tank 1 comprises a tank body 11, a sewage inlet 12 is arranged on the tank body 1, and a jet mixer 13 and a jet ejector 14 are arranged on the inner wall of the tank body 11; external sewage enters the tempering tank 1 through the sewage inlet 12 to balance the water quality and the water quantity, the jet mixer 13 can quickly moderate water inlet, circulating water, added medicaments and the like in the tempering tank 1 in a short time, and the steam ejector 14 heats the wastewater in the tempering tank 1.

With reference to the drawings, the anaerobicThe oxygen reactor 2 comprises a closed shell 21, and the shell 21 is sequentially provided with a water distributor system 22, a sludge expansion area 23, a double-membrane fixed bed reaction area 24, a three-phase separator 25 and a methane collection chamber 26 from bottom to top. The closed housing 21 does not generate waste gas to be treated, does not risk biogas leakage, and can optimally collect biogas as a usable energy source without generating process waste gas to be treated. The volume load designed by the anaerobic reactor 2 can reach 5-30 kg/m according to the water quality of the wastewater³·d。

Specifically, the housing 21 may be made into a civil structure, a circular metal tank structure or an FRP glass fiber reinforced plastic integrated device according to practical application. The biogas collection chamber 26 collects biogas generated by the anaerobic reactor 2, the biogas collection chamber 26 is communicated to the top of the tempering tank 1 through a biogas communication pipe 6, and the biogas collected in the biogas collection chamber 26 at the top of the anaerobic reactor 2 is conveyed to the top of the tempering tank 1. The anaerobic sludge concentration of the sludge expansion area 23 is higher, and the wastewater containing high-concentration organic pollutants is uniformly distributed by the water distributor system, then is mixed with a large amount of anaerobic microorganism sludge in the area, is subjected to mass transfer, is primarily degraded and purified, and simultaneously generates a large amount of methane.

In this embodiment, the water distributor system 22 employs a two-line pulse water distribution system, and the two-line pulse water distribution system with a customized design can effectively avoid the phenomena of uneven water distribution and short flow caused by the water distribution of a conventional perforated pipe.

In some embodiments, a backwashing pipe 5 can be further arranged, the backwashing pipe 5 is arranged in the double-film fixed bed reaction zone 24, the double-film biological filler in the double-film fixed bed reaction zone 24 can be periodically backwashed, and aged anaerobic biological films on the film bed can be periodically washed to keep the activity of anaerobic microorganisms attached to the film bed. A large amount of anaerobic microorganisms are attached to a membrane bed of the composite membrane fixed bed reaction zone 24, wastewater subjected to degradation and purification treatment in the sludge expansion zone 23 can be further purified when passing through the zone, and during the process that biogas generated in the sludge expansion zone 23 rises through a gap between standardized modules of the composite membrane fixed bed, strong local turbulence can be generated, so that the contact and mass transfer effects of the wastewater and the anaerobic microorganisms attached to the membrane bed are enhanced, further deep purification of organic pollutants in the composite membrane fixed bed reaction zone 24 is guaranteed, meanwhile, the rising flow rate of sludge and biogas mixed liquor in the sludge expansion zone 23 is slowed down, and the total anaerobic sludge concentration of the anaerobic reactor 2, the stability of an anaerobic system and the removal efficiency of pollutants are guaranteed.

It can be understood that, in order to achieve better treatment effect of the anaerobic reactor 2, the bottom of the anaerobic reactor 2 is also provided with a sludge discharge system 27, and the residual anaerobic sludge is discharged.

The water inlet pipeline 3 conveys the wastewater after the tempering in the tempering tank 1 to the subsequent flow, the bottom of the tempering tank 1 is communicated with the bottom of the anaerobic reactor 2 through the water inlet pipeline 3, the water inlet pipeline 3 is provided with a feed pump 31, and the feed pump 31 lifts the wastewater after the tempering in the tempering tank 1 to the water distributor system 22. The water inlet pipe 3 is provided with a flow meter 32, a temperature sensor 33 and a pH sensor 34. The flow meter 32 monitors the influent flow rate to the anaerobic reactor 2. The temperature sensor 33 monitors the temperature of the inlet water in the tempering tank 1, and the pH sensor 34 monitors the pH of the inlet water of the anaerobic reactor 2 in the tempering tank 31.

The three-phase separator 25 comprises a main body 251, a degassing precipitation zone 252, a mud-water separation zone 253, a sludge precipitation zone 253 and a submerged effluent collection system 255 are arranged in the main body 251, the degassing precipitation zone, the mud-water separation zone, the sludge precipitation zone 253 and the submerged effluent collection system 255 jointly form a high-efficiency methane, sludge and effluent separation device, and after sludge-water mixed liquid is separated by the three-phase separator 25, anaerobic sludge with methane bubbles released falls back to the anaerobic reactor 2 from a sludge hopper of the three-phase separator 25. The sludge settling area 253 is provided with a backwashing pipe 5 for backwashing the sludge settling area 253, so that the problem of sludge blockage of the sludge settling area 253 is effectively prevented. The treated wastewater, anaerobic sludge and dissolved part enter a degassing and settling zone 252, biogas is released into a biogas collection chamber 26 at the top of the anaerobic reactor 2, and the sludge and degassed wastewater mixed liquid enters a subsequent sludge-water separation zone 253.

The three-phase separator 25 can effectively achieve separation of the flocculent anaerobic sludge (or granular sludge) from the biogas and the effluent, so that high-concentration anaerobic sludge (granular sludge or flocculent sludge) can be retained in the anaerobic reactor.

It will be appreciated that the submerged effluent collection system 255 employs a submerged outlet pipe. The submerged water outlet pipe is arranged below the water level line of the anaerobic reactor 2, the effluent of the three-phase separator 25 is conveyed to the conditioning tank 1, the submerged water outlet pipe is adopted to replace a conventional overflow weir to realize an effluent mode, the problem of uneven effluent caused by the fact that the overflow weir is installed out of level is effectively solved, and the stability and uniformity of the effluent are greatly improved.

The sludge-water separation zone 253 enters the sludge-water separation zone 253 from the degassed sludge-water mixture in the degassing and settling zone 252, and because the lifting action of the methane micro-bubbles is eliminated, the flow state of the settled water flow is laminar flow, the flow velocity is gradually reduced in the rising process, so that the sludge is settled and falls back to the anaerobic reactor 2 along the inner wall surface. After the sludge-water mixture in the sludge settling zone 253 is degassed and subjected to sludge-water separation, the sludge is flocculated, settled and concentrated in the settling zone and then falls back to the anaerobic reactor 2.

Be provided with manhole 28 on anaerobic reactor, manhole 28 includes first manhole 281 and second manhole 282, and first manhole 281 is located the lateral wall of anaerobic reactor 2 bottom, and second manhole 282 is located the top of anaerobic reactor 2, and convenient maintenance person gets into and carries out maintenance and installation tectorial membrane fixed membrane piece in anaerobic reactor 2 when the system overhauls.

The compound film fixed bed reaction zone 24 comprises a support and a plurality of compound film fixed bed standardized modules fixed on the support at intervals. The standard module of the compound film fixed bed is a standard compound film anaerobic biological filler module which is easy to install and maintain, and the module is provided with a back flushing system which can regularly flush aged biological films and is convenient for the growth and the attachment of new anaerobic biological films. The dimension of the standardized membrane block of the compound membrane fixed bed arranged in the embodiment of the scheme is 400 multiplied by 1000mm, six membranes are contained, the interval between the membranes is 60mm, the membrane block is a standardized compound membrane anaerobic biological filler module, the installation and the daily maintenance are easy, a large amount of time cost and labor cost can be saved, and the reasonable height and area of the reaction zone 24 of the compound membrane fixed bed can be conveniently built according to the characteristics of waste water and the specification of a reactor; a back-flushing pipe 5 is arranged below the fixed membrane reactor, and is used for back-flushing the membrane bed in the reaction zone 24 of the double-membrane fixed bed, so that the aged biological membrane on the membrane bed can be periodically flushed, and the growth of a new biological membrane is accelerated.

The membrane block adopts independently developed high-strength non-woven fabric fiber filler, the non-woven fabric fiber filler mainly uses a modified polymer material as a base material, is alkali-resistant and acid-resistant, has good degradation effect and degradation effect on organic matters which are difficult to degrade, such as hydrocarbons, benzenes and the like, is strong in milk corrosivity, and has a service life of 5-10 years.

The system also comprises a circulating system 4, the effluent of the anaerobic reactor 2 is connected with the conditioning tank 1 through the circulating system 4, and the effluent of the anaerobic reactor 2 and the wastewater in the conditioning tank 1 are mixed and circulated so as to fully utilize the alkalinity of the effluent of the anaerobic reactor 2. Through the circulation of outside, can effectively control the invariable inflow flow of reactor, ensure the good anti impact load ability of system and the stability of operation.

The embodiments of the present invention have been described in detail with reference to the accompanying drawings, but the present invention is not limited to the above embodiments, and various changes can be made without departing from the spirit of the present invention within the knowledge of those skilled in the art.

Claims

1. A membrane lotus root up-flow anaerobic sludge bed reactor system, comprising:

2. The membrane-coupled upflow anaerobic sludge blanket reactor system of claim 1, wherein: the water distributor system adopts a double-line pulse water distribution system.

3. The membrane-coupled upflow anaerobic sludge blanket reactor system of claim 1, wherein: and a sludge discharge system is also arranged at the bottom of the anaerobic reactor.

4. The membrane-coupled upflow anaerobic sludge blanket reactor system of claim 1, wherein: and the water inlet pipeline is provided with a flow meter, a temperature sensor and a pH sensor.

5. The membrane-coupled upflow anaerobic sludge blanket reactor system of claim 1, wherein: be provided with the manhole on anaerobic reactor, the manhole includes first manhole and second manhole, first manhole is located the lateral wall of anaerobic reactor bottom, the second manhole is located anaerobic reactor's top.

6. The membrane-coupled upflow anaerobic sludge blanket reactor system of claim 1, wherein: the anaerobic reactor effluent treatment system further comprises a circulating system, and the circulating system mixes and circulates the anaerobic reactor effluent and the wastewater in the conditioning tank.

7. The membrane-coupled upflow anaerobic sludge blanket reactor system of claim 1, wherein: the main part is hourglass hopper-shaped, the bottom toper district of main part sets up sludge settling zone, sludge settling zone's top sets up the degasification settling zone and the muddy water separation zone of left and right separation setting, submerged water collection system sets up under anaerobic reactor's water line.

8. The membrane-coupled upflow anaerobic sludge blanket reactor system of claim 7, wherein: the submerged water outlet collecting system adopts a submerged water outlet pipe.

9. The membrane-coupled upflow anaerobic sludge blanket reactor system of claim 7, wherein: the device also comprises a backwashing pipe, wherein the backwashing pipe is respectively arranged in the sludge settling zone and the composite membrane fixed bed reaction zone.

10. The membrane-coupled upflow anaerobic sludge bed reactor system as in any of claims 1-9, wherein: the biogas conditioning device is characterized by further comprising a biogas communicating pipe, wherein the biogas communicating pipe is communicated with a biogas collection chamber and a conditioning tank, and a biogas outlet is formed in the top of the conditioning tank.