CN213493001U - Full-automatic external-pressure internal-suction type membrane filtration system - Google Patents
Full-automatic external-pressure internal-suction type membrane filtration system Download PDFInfo
- Publication number
- CN213493001U CN213493001U CN202022215267.6U CN202022215267U CN213493001U CN 213493001 U CN213493001 U CN 213493001U CN 202022215267 U CN202022215267 U CN 202022215267U CN 213493001 U CN213493001 U CN 213493001U
- Authority
- CN
- China
- Prior art keywords
- water
- water outlet
- water tank
- treatment
- type membrane
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000005374 membrane filtration Methods 0.000 title claims abstract description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 418
- 239000012528 membrane Substances 0.000 claims abstract description 93
- 238000011001 backwashing Methods 0.000 claims abstract description 64
- 238000011010 flushing procedure Methods 0.000 claims abstract description 15
- 238000012806 monitoring device Methods 0.000 claims abstract description 11
- 238000012545 processing Methods 0.000 claims description 16
- 238000009826 distribution Methods 0.000 claims description 13
- 239000012510 hollow fiber Substances 0.000 claims description 13
- 238000005406 washing Methods 0.000 claims description 10
- 230000009897 systematic effect Effects 0.000 claims description 7
- 238000009434 installation Methods 0.000 claims description 6
- 238000004891 communication Methods 0.000 claims description 3
- 238000007789 sealing Methods 0.000 claims description 3
- 230000000712 assembly Effects 0.000 claims 2
- 238000000429 assembly Methods 0.000 claims 2
- 239000010865 sewage Substances 0.000 abstract description 26
- 235000020188 drinking water Nutrition 0.000 abstract description 17
- 239000003651 drinking water Substances 0.000 abstract description 17
- 238000000746 purification Methods 0.000 abstract description 8
- 238000012986 modification Methods 0.000 abstract description 3
- 230000004048 modification Effects 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 19
- 101100520231 Caenorhabditis elegans plc-3 gene Proteins 0.000 description 18
- 238000001914 filtration Methods 0.000 description 16
- 230000008569 process Effects 0.000 description 16
- 238000004140 cleaning Methods 0.000 description 13
- 238000012423 maintenance Methods 0.000 description 10
- 238000000926 separation method Methods 0.000 description 9
- 239000003814 drug Substances 0.000 description 7
- 238000007599 discharging Methods 0.000 description 5
- 230000002354 daily effect Effects 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 230000004907 flux Effects 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 238000005273 aeration Methods 0.000 description 3
- 230000003203 everyday effect Effects 0.000 description 3
- 230000009885 systemic effect Effects 0.000 description 3
- 239000008399 tap water Substances 0.000 description 3
- 235000020679 tap water Nutrition 0.000 description 3
- 229910000975 Carbon steel Inorganic materials 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 239000010962 carbon steel Substances 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000001471 micro-filtration Methods 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 238000005086 pumping Methods 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 238000002791 soaking Methods 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 230000001131 transforming effect Effects 0.000 description 2
- 238000000108 ultra-filtration Methods 0.000 description 2
- 208000035143 Bacterial infection Diseases 0.000 description 1
- 239000002028 Biomass Substances 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 208000022362 bacterial infectious disease Diseases 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 238000011897 real-time detection Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 238000009287 sand filtration Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Images
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model discloses a full-automatic external pressure internal suction type membrane filtration system, which comprises a case, wherein a treatment water tank and a clean water tank are arranged at least at intervals in the case, at least the treatment water tank is of a closed structure, a pressure water inlet device is arranged through the treatment water tank, an internal suction type membrane component is arranged in the treatment water tank, a water outlet device and a back washing device are connected between the clean water tank and the internal suction type membrane component, and the system also comprises an air water flushing device, a water pressure monitoring device, an exhaust valve and a PLC controller; the system can automatically treat water, clean and maintain the water, can be widely used for sewage purification treatment and direct drinking water treatment, and is particularly suitable for the label lifting, upgrading and modification of municipal sewage treatment plants and the large-water-volume sewage purification treatment of black and odorous water bodies in riverways.
Description
Technical Field
The utility model relates to a water treatment technical field especially relates to a full-automatic external pressure systematic membrane filtration system that can use on a large scale.
Background
The current water treatment comprises sewage treatment and direct drinking water treatment, and the above water treatment processes all use membrane bodies, for example, most of the membrane bodies for sewage treatment are MBR membranes, ultrafiltration membranes and the like, wherein the MBR membranes are microfiltration membranes, and can be divided into three types, namely separation membranes, aeration membranes and three extraction membranes according to the functions of the MBR membranes. A separation membrane is adopted in the sewage treatment process, the aperture of the separation membrane is generally 0.1-0.4 microns, suspended matters in sewage can be effectively intercepted, solid-liquid separation is realized, and an MBR membrane separation technology is formed.
In the actual use process, the MBR membrane separation technology is generally efficiently combined with the biological treatment method, so that the membrane separation technology is used for replacing a secondary sedimentation tank in an activated sludge method to carry out solid-liquid separation, the process not only can effectively achieve the purpose of sludge-water separation, but also has the advantage that the traditional process for three-stage sewage treatment is incomparable. When the MBR membrane is used for forming the bioreactor, the MBR membrane is arranged in the biochemical aeration tank, so that the activated sludge can be concentrated, the biomass of a system can be increased, and the treatment capacity of the system can be improved.
The direct drinking water treatment is a new process formed by increasing the quality requirement of drinking water along with the continuous improvement of the life quality of people, and the water purifier is rapidly developed in recent years and is applied to urban residential districts, villages and the like, so that residents can take water and drink the water, and the water consumption is huge. In the relevant equipment of direct drinking water of domestic production at present, column type milipore filter, column type reverse osmosis membrane have mainly been adopted and have been carried out direct drinking water treatment, and these two kinds of membrane water treatment effeciencies are extremely low, and single membrane only produces the water yield per hour and only has 2 ~ 3 tons, is difficult to realize the large water supply of ten thousand tons level, and the cost is high, washs inconveniently, and the maintenance cost is high, and life is short, causes the ton level direct drinking water treatment cost height.
Therefore, membrane filtration becomes the most reliable water treatment mode in sewage treatment, tap water production and direct drinking water preparation processes, and how to improve membrane flux, remove membrane pollution and realize automatic membrane cleaning is an important factor influencing the cost of the membrane filtration process.
SUMMERY OF THE UTILITY MODEL
The utility model aims to solve the technical problem that a full-automatic external pressure systematic membrane filtration system that membrane flux is big, the commonality is strong, can online self-cleaning, and maintain convenience, long service life is provided.
In order to solve the technical problem, the technical scheme of the utility model is that: full-automatic external pressure internal suction type membrane filtration system, including quick-witted case, quick-witted incasement interval at least is provided with treatment water tank and clean water tank, and at least treatment water tank is the closed structure, runs through treatment water tank installs inward water supply and increases the hydraulic pressurization water installations of incasement, install internal suction type membrane module in the treatment water tank, clean water tank with be connected with water outlet device and back flush system between the internal suction type membrane module, still include air water washing unit, install in water pressure monitoring device and discharge valve on the treatment water tank, air water washing unit's discharge port corresponds internal suction type membrane module sets up, pressurization water intake installation water outlet device back flush system with air water washing unit is connected to the PLC controller respectively.
As an optimized technical scheme, an equipment box is arranged between the treatment water tank and the clear water tank, the water outlet device, the back washing device, the PLC and part of the air-water flushing device are respectively arranged in the equipment box, and a distribution box is further arranged in the equipment box.
As a preferable technical scheme, the internal suction type membrane modules are arranged in groups and at least two groups are arranged in parallel, each internal suction type membrane module in the same group is arranged in series, and each group of internal suction type membrane modules is respectively and correspondingly connected with the water outlet device and the backwashing device.
As a preferred technical scheme, the internal suction type membrane assembly comprises at least one module pipe frame, curtain type hollow fiber membranes are arranged in the module pipe frame in a parallel communication mode, and the module pipe frame is communicated with the water outlet device and the back washing device respectively.
According to a preferable technical scheme, the pressurizing water inlet device comprises a pressurizing water inlet pump, water tank water inlet pipes are arranged at the water outlet end of the pressurizing water inlet pump in parallel, water outlet ports are correspondingly arranged on the water tank water inlet pipes, and the water outlet ports penetrate through the top wall of the treatment water tank in a sealing mode.
As a preferred technical scheme, the water outlet device comprises a water outlet pipe communicated with the treatment water tank and the clear water tank, a universal water pump is connected to the water outlet pipe in series, a first water outlet electromagnetic valve is installed on the water outlet pipe on the water inlet side of the universal water pump, and a second water outlet electromagnetic valve is installed on the water outlet pipe on the water outlet side of the universal water pump.
As a preferred technical scheme, the backwashing device comprises two backwashing pipelines, wherein backwashing electromagnetic valves are respectively installed on the two backwashing pipelines, one backwashing pipeline is communicated between the water outlet side of the first water outlet electromagnetic valve and the water outlet side of the second water outlet electromagnetic valve, and the other backwashing pipeline is communicated between the water inlet side of the first water outlet electromagnetic valve and the water inlet side of the second water outlet electromagnetic valve.
As a preferred technical scheme, the air-water flushing device comprises an air compressor, the air compressor is connected to the PLC, an air outlet end of the air compressor is connected with an air distribution pipe, and air holes are formed in the air distribution pipe;
the side walls of the treatment water tank and the clear water tank are respectively provided with an emptying pipe, the emptying pipe is provided with an emptying electromagnetic valve, and the emptying electromagnetic valve is connected to the PLC.
Since the technical scheme is used, the utility model discloses following beneficial effect has: the pressurized water inlet device conveys water to be treated into the treatment water tank, the water pressure in the water tank keeps a certain positive pressure, the water is filtered in the treatment water tank through the internal suction type membrane component, the internal suction type membrane component discharges the filtered water outwards through the water outlet device, the air water flushing device and the back flushing device can perform back flushing and cleaning on the internal suction type membrane component, the system can perform automatic water treatment and cleaning maintenance in the water treatment process, the treatment process of the water treatment system is more flexible and effective, and the pressurized water inlet device can be widely used for sewage purification treatment and direct drinking water treatment, and is particularly suitable for label improvement, upgrading and reconstruction of municipal sewage treatment plants and large-water-volume sewage purification treatment of black and odorous water bodies in riverways.
Drawings
The drawings are only intended to illustrate and explain the present invention and do not limit the scope of the invention. Wherein:
fig. 1 is a schematic structural diagram of an embodiment of the present invention;
fig. 2 is a schematic view of another directional structure of the embodiment of the present invention;
FIG. 3 is a schematic diagram of the water path for normal drainage and back flushing according to an embodiment of the present invention;
in the figure: 1-a chassis; 101-a treatment water tank; 102-a clear water tank; 103-equipment box; 2-a distribution box; 3-a PLC controller; 4-an exhaust valve; 5-a remote monitor; 6-module pipe frame; 7-curtain hollow fiber membranes; 8-automatic dosing device; 9-water tank inlet pipe; 10-a water outlet port; 11-a water outlet pipe; 12-general water pump; 13-a first water outlet solenoid valve; 14-a second water outlet solenoid valve; 15-backwashing the pipeline; 16-backwashing electromagnetic valves; 17-an air compressor; 18-gas distribution pipe; 19-emptying the pipe; 20-evacuation solenoid valve.
Detailed Description
The invention is further explained below with reference to the drawings and examples. In the following detailed description, certain exemplary embodiments of the present invention have been described by way of illustration only. Needless to say, a person skilled in the art will recognize that the described embodiments can be modified in various different ways without departing from the spirit and scope of the invention. Accordingly, the drawings and description are illustrative in nature and not intended to limit the scope of the claims.
As shown in fig. 1 and 2, the full-automatic external-pressure internal-suction type membrane filtration system comprises a case 1, wherein the case 1 is generally configured into a rectangular structure, and the case plates of the case 1 are all configured into carbon steel plates or stainless steel corrugated plates, so that the assembly is simple, convenient and quick. The PLC controller 3 is arranged in the filtering system, and the automatic operation of the water treatment of the filtering system can be realized by setting the internal control program of the PLC controller 3 during the actual operation of the system without human intervention and monitoring.
At least a treatment water tank 101 and a clean water tank 102 are arranged in the case 1 at intervals, and at least the treatment water tank 101 is of a closed structure, so that external pressure control of the system is realized. The water treatment is performed in the treatment tank 101 and the clean water tank 102 is used for storing treated clean water for subsequent cleaning maintenance or for pumping directly out. Still install water pressure monitoring device and discharge valve 4 on the processing water tank 101, just water pressure monitoring device is connected to PLC controller 3. Specifically, the water pressure monitoring device includes running through the manometer of treatment water tank 101 lateral wall installation, the manometer is connected to PLC controller 3, the manometer real-time detection the pressure of treatment water tank 101 internal water, and carry to PLC controller 3 prestore in PLC controller 3 with the target water pressure scope, when real-time pressure value reached the target water pressure scope, PLC controller 3 control is intake, is gone out relevant parts such as water and is carried out state conversion, thereby realizes the pressure control in the treatment water tank 101.
Run through treatment tank 101 and install the pressurization water installations that inwards send water and increase incasement water pressure, install the systemic membrane subassembly in the treatment tank 101, clear water tank 102 with be connected with water outlet device and back flush unit between the systemic membrane subassembly, the play water end of systemic membrane subassembly is connected to water outlet device, pressurization water inlet device water outlet device with back flush unit is connected to PLC controller 3 respectively. The pressurized water inlet device conveys water to be treated into the treatment water tank 101, and pressurizes the water in the tank, namely, the water is subjected to external pressure, so that the pressure of the water is kept at 2-4 kg, and the quality and the efficiency of water treatment are improved.
In this embodiment, the backwashing device is disposed on the water outlet device, a water outlet end of the water outlet device is also used as a water inlet end of the backwashing device, and a water near end of the water outlet device is also used as a water outlet end of the backwashing device. The water in the treatment water tank 101 is filtered by the internal suction type membrane module and is discharged to the clean water tank 102 from the water outlet device, the backwashing device is used for performing backwashing on the internal suction type membrane module to clean and maintain the internal suction type membrane module, and the water source of the backwashing device is the water in the clean water tank 102.
Specifically, the internal suction type membrane modules may be arranged in the treatment water tank 101 in groups according to the size of the treatment water tank 101, for example, at least two groups of internal suction type membrane modules are arranged in parallel, each internal suction type membrane module in the same group is arranged in series, and each group of internal suction type membrane modules is respectively and correspondingly connected with the water outlet device and the backwashing device. The internal suction type membrane component comprises at least one module pipe frame 6, curtain type hollow fiber membranes 7 are arranged in the module pipe frame 6 in a parallel communication mode, and the module pipe frame 6 is communicated with the water outlet device and the back washing device respectively. The water in the treatment water tank 101 enters the module pipe frame 6 after being filtered by the curtain type hollow fiber membrane 7, and when the water outlet device is used for discharging water outwards, the water in the module pipe frame 6 has a suction force, namely internal suction, and is matched with the external pressure mentioned in the description, so that the membrane flux of the water is greatly increased, and the water yield can reach more than 80 kilograms per square meter per hour, thereby greatly increasing the water yield of the internal suction type membrane module.
The embodiment also comprises a gas-water flushing device, wherein the exhaust end of the gas-water flushing device corresponds to the internal suction type membrane assembly, and the pressurizing water inlet device, the water outlet device, the backwashing device, the gas-water flushing device, the water pressure monitoring device and the exhaust valve 4 are respectively connected to the PLC 3. An equipment box 103 is arranged between the treatment water tank 101 and the clear water tank 102, the water outlet device, the back washing device, the PLC controller 3 and part of the air water flushing device are respectively arranged in the equipment box 103, a distribution box 2 is further arranged in the equipment box 103, and the arrangement of the equipment box 103 enables the appearance of the system to be regular and convenient to arrange.
The pressurizing water inlet device comprises a pressurizing water inlet pump, water tank water inlet pipes 9 are arranged at the water outlet end of the pressurizing water inlet pump in parallel, water outlet ports 10 are correspondingly arranged on the water tank water inlet pipes 9, and the water outlet ports 10 penetrate through the top wall of the treatment water tank 101 in a sealing mode. The PLC controller 3 can control the opening and closing of the pressurizing water inlet pump to realize the control of water feeding into the treatment water tank 101, water enters from the top end of the treatment water tank 101 to flush the curtain type hollow fiber membrane 7, and impurities settled by filtration on the surface of the curtain type hollow fiber membrane 7 are cleaned in a proper manner while the water is fed.
The water outlet device comprises a water outlet pipe 11 communicating the treatment water tank 101 and the clear water tank 102, a universal water pump 12 is connected to the water outlet pipe 11 in series, a first water outlet electromagnetic valve 13 is installed on the water outlet pipe 11 on the water inlet side of the universal water pump 12, and a second water outlet electromagnetic valve 14 is installed on the water outlet pipe 11 on the water outlet side of the universal water pump 12. The back washing device comprises two back washing pipelines 15, back washing electromagnetic valves 16 are respectively installed on the two back washing pipelines 15, one back washing pipeline 15 is communicated with the water outlet side of the first water outlet electromagnetic valve 13 and the water outlet side of the second water outlet electromagnetic valve 14, and the other back washing pipeline 15 is communicated with the water inlet side of the first water outlet electromagnetic valve 13 and the water inlet side of the second water outlet electromagnetic valve 14. The PLC 3 controls different electromagnetic valves to be opened or closed, so that normal drainage treatment of the system or back flushing cleaning maintenance of the internal suction type membrane module is realized.
This system the air water washing unit includes air compressor machine 17, air compressor machine 17 is connected to PLC controller 3, the end of giving vent to anger of air compressor machine 17 is connected with gas distribution pipe 18, it has the gas pocket to arrange on the gas distribution pipe 18. In the embodiment, the air distribution pipe 18 is arranged right below the internal suction type membrane module, the air holes are formed in the top end of the air distribution pipe 18, and when the air compressor 17 is opened, aeration is formed to wash the surface of the curtain type hollow fiber membrane 7 with air water.
In this embodiment, the side walls of the processing water tank 101 and the clean water tank 102 are respectively provided with an evacuation pipe 19, the evacuation pipe 19 is provided with an evacuation solenoid valve 20, and the evacuation solenoid valve 20 is connected to the PLC controller 3. Under the control of the PLC 3, the emptying electromagnetic valve 20 is opened, and the emptying pipes 19 are utilized to empty the treatment water tank 101 and the clean water tank 102 so as to be convenient for repair and maintenance or discharge sewage formed after back washing.
As shown by the solid arrows in fig. 3, the drainage process using the water outlet device of the present embodiment is as follows:
the PLC 3 controls the two backwashing electromagnetic valves 16 to be closed, the first water outlet electromagnetic valve 13 and the second water outlet electromagnetic valve 14 are kept to be opened, the universal water pump 12 is controlled to be started to form suction force, water in the treatment water tank 101 passes through the curtain type hollow fiber membrane 7 and then enters the module pipe frame 6 under the suction effect of the universal water pump 12, then enters the water outlet pipe 11 and sequentially passes through the first water outlet electromagnetic valve 13, the second water outlet electromagnetic valve 14 and the universal water pump 12 to enter the clean water tank 102, and the water in the treatment water tank 101 is transferred to the clean water tank 102.
As shown by the dotted arrows in fig. 3, the backwashing of the curtain type hollow fiber membranes 7 by the backwashing device of this embodiment is performed by:
the PLC controller 3 controls the first water outlet electromagnetic valve 13 and the second water outlet electromagnetic valve 14 to be closed, controls the back washing electromagnetic valve 16 to be opened, controls the general water pump 12 to be started to form suction force, water in the clean water tank 102 enters the two back washing pipelines 15 and passes through the general water pump 12 and the back washing electromagnetic valve 16 to enter the module pipe frame 6 and pass through the curtain type hollow fiber membrane 7 and then enter the treatment water tank 101, and the back washing cleaning of the curtain type hollow fiber membrane 7 is realized.
The embodiment also provides a filtering process of the full-automatic external-pressure internal-suction type membrane filtering system, which comprises the following steps,
step one, respectively connecting each controlled component in the pressurized water inlet device, the water outlet device and the backwashing device and the air compressor 17 to the PLC 3, and setting the working time sequence or/and the continuous working time of the pressurized water inlet device, the water outlet device, the backwashing device and the air compressor 17 in the PLC 3. Namely, the pressurized water inlet pump, the universal water pump 12, the first water outlet electromagnetic valve 13, the second water outlet electromagnetic valve 14, the back flush electromagnetic valve 16, the evacuation electromagnetic valve 20 and the like are respectively connected with the PLC controller 3, and the working time sequence or/and the continuous working time of each pump and each valve are set in the PLC controller 3, so as to automatically control the working process of the filtering system.
Setting a normal water yield range of each water outlet device in the PLC 3, and monitoring the water yield of each water outlet device through the PLC 3 so as to judge whether the water outlet devices need back washing maintenance or not.
The PLC 3 is internally provided with a target water pressure range in the treatment water tank 101, all pressure values in the target water pressure range are positive numbers, generally the target water pressure range is set to be 2-4 kilograms, and the purpose of increasing and improving the quality of the discharged water can be achieved.
And the water pressure monitoring device is connected to the PLC controller 3, the PLC controller 3 receives the water pressure value in the processing water tank 101 detected by the water pressure monitoring device in real time, namely, the pressure gauge is connected to the PLC controller 3 and used for controlling the states of the pumps and the valves according to the water pressure in the processing water tank 101.
And step two, starting the pressurized water inlet device through the PLC 3, injecting water into the processing water tank 101, and discharging air in the processing water tank 101 through the exhaust valve 4 until the PLC 3 judges that the water pressure value in the processing water tank 101 reaches the target water pressure range according to the detection value of the water pressure monitoring device.
And step three, the PLC 3 starts each water outlet device, water in the treatment water tank 101 enters the corresponding water outlet device after being filtered by the internal suction type membrane module, each water outlet device is matched with the clean water tank 102 to pump the water, and in the process, the PLC 3 adjusts the water delivery quantity of the pressurized water inlet device on line in real time according to the comparison result of the detection value of the water pressure monitoring device and the target water pressure range, so that in the process that the water outlet device and the pressurized water inlet device run simultaneously, the water pressure value in the treatment water tank 101 is in the set target water pressure range, namely, the water pressure in the treatment water tank 101 is ensured to be 3 kilograms.
Step four, the PLC 3 compares the water yield information provided by the water outlet device with an internally stored normal water yield range in real time, when the PLC 3 judges that the water yield of the water outlet device is lower than the normal water yield range, the PLC 3 controls the water outlet device to stop pumping water into the clean water tank 102, and opens the exhaust valve 4 to enable the water level in the treatment water tank 101 to drop, for example, the water level is controlled to drop to 100 mm below a top plate; and simultaneously starting the air compressor 17 to perform air-water backwashing on the internal suction type membrane component connected with the water outlet device with low water yield, wherein the backwashing time can be set according to the size of the system, and if the backwashing time is set to be 1 hour. There are various methods for acquiring the water output information of the water outlet device by the PLC controller 3, for example, a flow meter, a flow sensor, etc. are disposed in a pipeline of the water outlet device.
And step five, after the PLC 3 monitors that the backwashing time is up, closing the air compressor 17 and the water outlet device, and discharging the backwashing sewage, for example, discharging the sewage generated by backwashing into an adjusting tank for secondary treatment and recovery.
And step six, injecting water and chemicals into the treatment water tank 101, and soaking the internal suction type membrane assembly for at least 24 hours. In order to add medicine, a PH detector may be disposed in the processing water tank 101, the PH detector is connected to the PLC controller 3, the PLC controller 3 is further connected to an automatic medicine adding device 8, the automatic medicine adding device 8 includes a medicine adding pump, a medicine adding barrel, and the like, and can automatically dispense medicine and add medicine into the processing water tank 101.
And seventhly, after the soaking time is up, controlling the air compressor 17 to start for the second time by the PLC 3, performing secondary air-water backwashing on the internal suction type membrane assembly, wherein the time of the secondary air-water backwashing lasts at least 1 hour, starting the backwashing device after the time of the air-water backwashing washing is up, backwashing the internal suction type membrane assembly twice from inside to outside, and discharging the backwashing sewage for the second treatment.
And step eight, after the backwashing sewage is discharged, skipping to the step two for circulating work.
The PLC controller 3 of this embodiment may also be connected to a remote monitor 5, so as to realize remote viewing or control of water treatment.
Through the technical means, the utility model has the advantages of it is following:
one, wide use
1. Can be connected to various sewage and purified water treatment processes, can replace filtering equipment such as sand filtration, mechanical filtration, medium filtration, fiber filtration and the like, and realizes the water body purification function.
2. Can be used for sewage treatment engineering, water purification treatment engineering, river black and odorous water body treatment and the like.
3. The system is particularly suitable for upgrading, upgrading and transforming municipal sewage treatment plants, the daily treatment capacity of a single machine can reach 50000 square at least, the cost for upgrading, upgrading and transforming the ton water can be as low as about two hundred yuan, and the effluent can reach three types of water of the standard land surface.
4. Can output direct drinking water. When direct drinking water is treated, automatic backwashing can be realized, after known devices such as dosing and the like are added, on-line automatic chemical cleaning can be realized under the control of the PLC, so that the membrane throughput is ensured to operate within the designed maximum range, the service life of the membrane component can be greatly prolonged and the production cost of direct drinking water is reduced through automatic backwashing and on-line automatic chemical cleaning, the direct drinking water amount treated by a single machine per day is large, the direct drinking water amount can reach dozens of ten thousand tons or even millions of tons when the direct drinking water is used in parallel, and the manufacturing cost of each ton of water is reduced to be below 0.1 yuan. In addition, the direct drinking water is processed under the control of the PLC controller, a water storage tank is not arranged, the water is automatically started and stopped, water is instantly supplied, bacterial infection is avoided, and the fresh, pure, safe and reliable water quality is ensured.
Secondly, the treatment capacity is large
1. The single machine which can be transported is manufactured according to the current safe transportation conditions of the automobile road, the daily sewage treatment can reach 50000 tons, the daily tap water treatment can reach 100000 tons, and the combined parallel connection can achieve dozens of thousands of tons or even millions of tons of daily treatment capacity.
2. When the filtering system is used for water treatment, the filtering pressure in the treatment water tank can reach 3 kilograms, and the filtering pressure is matched with the suction of the universal water pump, the membrane flux is more than 5 times of that of a common filtering system, and each square meter can reach more than 80 kilograms per hour.
Thirdly, the effluent quality is good
1. The water yield is large, the water quality of the discharged water is more stable, and the investment cost and the operation cost are greatly reduced.
2. The internal suction type membrane component can replace various membrane components such as a curtain type hollow fiber membrane, an MBR membrane, a microfiltration membrane, an ultrafiltration membrane, an RO membrane and the like according to the water demand, and the ideal water quality demand of water for users is met.
Fourthly, the maintenance and the use are convenient
1. The full-automatic external pressure internal suction type membrane filtration system can realize on-line automatic back flushing, and can automatically clean acid and alkali circularly on line at regular time after being matched with a dosing device, thereby greatly prolonging the service life of a membrane group and reducing the treatment cost.
2. After the side cover of the case is disassembled, the membrane module can be easily taken out of the treatment water tank for cleaning or replacement.
3. The PLC is adopted for automatic control, timing backwashing is realized, multiple machines can be circularly cleaned one by one when connected in parallel, and the machine does not need to be stopped for cleaning and maintenance, so that unattended operation in the true sense is realized; the independently optimized working environment can prolong the cleaning period, prolong the service life of the membrane group and reduce the maintenance cost.
Fifth, the construction period is short
And 6 mm stainless steel corrugated plates or 8 mm carbon steel corrugated plates are adopted for welding, so that the corrugated plate is firm, attractive and durable. A membrane filtration system for treating 50000 tons of sewage every day and a membrane filtration system for treating 100000 tons of tap water every day can be installed in place for 15 days, and the construction time is greatly saved.
Sixthly, the investment is small
1. The occupied area is saved. The membrane filtration system for treating 50000 tons per day is only 3 meters wide, 17.52 meters long and 3.2 meters high, and the floor area is 51.6 square meters, so that the system is particularly suitable for the transformation and use of old water treatment facilities with insufficient space.
2. The cost is saved. The investment of the currently and commonly used sewage treatment equipment for treating ten thousand tons per day is more than million yuan, while the investment of a filtration system with the same treatment capacity is only about four hundred yuan.
Seven, the running cost is low
Taking direct drinking water as an example, a 10000 ton full-automatic external pressure internal suction type membrane filtration system is processed every day, the installed power is 82KW, and the cost for processing each ton of water is about 0.078 yuan through tests; and traditional equipment needs a water supply equipment at least, a back flush, chemical cleaning equipment, and total cost is about 624 ten thousand yuan, consequently the utility model discloses become the economical and practical type equipment that sewage treatment upgrades and reforms transform and the running water upgrades and reforms transform.
The utility model discloses a pressurization water installations carries pending water to the treatment tank in, and make the water tank internal water pressure keep a quantitative malleation, water carries out filtration treatment through the systematic formula membrane module in the treatment tank, systematic formula membrane module will filter the water of accomplishing and outwards discharge through water outlet means, air water washing unit and back flush mounting can carry out the recoil washing clearance to the internal absorption formula membrane module, but this system is automatic water treatment and clearance maintenance in water treatment process, make water treatment system's processing technology use more nimble effective, can extensively be used for the purification treatment and the straight water treatment of sewage, the bid of specially adapted municipal sewage treatment plant, upgrade, reform transform and the big water purification treatment of river course black and odorous water body use.
The description of the present invention has been presented for purposes of illustration and description, and is not intended to be exhaustive or limited to the invention in the form disclosed. Many modifications and variations will be apparent to practitioners skilled in this art. The embodiment was chosen and described in order to best explain the principles of the invention and the practical application, and to enable others of ordinary skill in the art to understand the invention for various embodiments with various modifications as are suited to the particular use contemplated.
Claims (8)
1. Full-automatic external pressure internal suction type membrane filtration system comprises a case and is characterized in that: the quick-witted incasement interval at least is provided with processing water tank and clean water tank, and at least processing water tank is the closed structure, runs through processing water tank installs inward water supply and increases the hydraulic pressurization water installations in the case, install the systematic formula membrane module in the processing water tank, clean water tank with be connected with water outlet device and back flush mounting between the systematic formula membrane module, still include air water washing unit, install in water pressure monitoring device and discharge valve on the processing water tank, air water washing unit's exhaust port corresponds systematic formula membrane module sets up, pressurization water inlet device water outlet device back flush mounting with air water washing unit is connected to the PLC controller respectively.
2. The full automatic internal pressure external system type membrane filtration system as claimed in claim 1, wherein: an equipment box is arranged between the treatment water tank and the clear water tank, the water outlet device, the backwashing device, the PLC controller and part of the air-water flushing device are respectively arranged in the equipment box, and a distribution box is also arranged in the equipment box.
3. The full automatic internal pressure external system type membrane filtration system as claimed in claim 1, wherein: the internal suction type membrane assemblies are arranged in groups and at least two groups are arranged in parallel, each internal suction type membrane assembly in the same group is arranged in series, and each group of internal suction type membrane assemblies is respectively and correspondingly connected with the water outlet device and the backwashing device.
4. The full automatic internal pressure external system type membrane filtration system as claimed in claim 3, wherein: the internal suction type membrane assembly comprises at least one module pipe frame, curtain type hollow fiber membranes are arranged in the module pipe frame in a parallel communication mode, and the module pipe frame is communicated to the water outlet device and the backwashing device respectively.
5. The full automatic internal pressure external system type membrane filtration system as claimed in claim 1, wherein: the pressurizing water inlet device comprises a pressurizing water inlet pump, water tank water inlet pipes are arranged at the water outlet end of the pressurizing water inlet pump in parallel, water outlet ports are correspondingly arranged on the water tank water inlet pipes, and the water outlet ports penetrate through the top wall of the treatment water tank in a sealing mode.
6. The full automatic internal pressure external system type membrane filtration system as claimed in claim 1, wherein: the water outlet device comprises a water outlet pipe communicated with the treatment water tank and the clear water tank, a universal water pump is connected in series on the water outlet pipe, a first water outlet electromagnetic valve is installed on the water outlet pipe on the water inlet side of the universal water pump, and a second water outlet electromagnetic valve is installed on the water outlet pipe on the water outlet side of the universal water pump.
7. The full automatic internal pressure external system type membrane filtration system as claimed in claim 6, wherein: the back washing device comprises two back washing pipelines, back washing electromagnetic valves are respectively arranged on the two back washing pipelines, one back washing pipeline is communicated with the water outlet side of the first water outlet electromagnetic valve and the water outlet side of the second water outlet electromagnetic valve, and the other back washing pipeline is communicated with the water inlet side of the first water outlet electromagnetic valve and the water inlet side of the second water outlet electromagnetic valve.
8. The full automatic internal pressure external system type membrane filtration system as claimed in claim 1, wherein: the air-water flushing device comprises an air compressor, the air compressor is connected to the PLC, an air outlet end of the air compressor is connected with an air distribution pipe, and air holes are formed in the air distribution pipe;
the side walls of the treatment water tank and the clear water tank are respectively provided with an emptying pipe, the emptying pipe is provided with an emptying electromagnetic valve, and the emptying electromagnetic valve is connected to the PLC.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022215267.6U CN213493001U (en) | 2020-09-30 | 2020-09-30 | Full-automatic external-pressure internal-suction type membrane filtration system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022215267.6U CN213493001U (en) | 2020-09-30 | 2020-09-30 | Full-automatic external-pressure internal-suction type membrane filtration system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN213493001U true CN213493001U (en) | 2021-06-22 |
Family
ID=76394476
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202022215267.6U Expired - Fee Related CN213493001U (en) | 2020-09-30 | 2020-09-30 | Full-automatic external-pressure internal-suction type membrane filtration system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN213493001U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113230895A (en) * | 2021-07-12 | 2021-08-10 | 南京依柯卡特排放技术股份有限公司 | Ceramic membrane filtration remote real-time control system and method based on Internet of things |
-
2020
- 2020-09-30 CN CN202022215267.6U patent/CN213493001U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113230895A (en) * | 2021-07-12 | 2021-08-10 | 南京依柯卡特排放技术股份有限公司 | Ceramic membrane filtration remote real-time control system and method based on Internet of things |
| CN113230895B (en) * | 2021-07-12 | 2021-09-28 | 南京依柯卡特排放技术股份有限公司 | Ceramic membrane filtration remote real-time control system and method based on Internet of things |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105152399A (en) | Reverse osmosis container-type sea water desalination plant and water producing process thereof | |
| CN102616954B (en) | Integrated water purification and supply method and system | |
| CN104129887A (en) | Reclaimed water recycling system based on membrane bioreactor | |
| KR100751233B1 (en) | Ultra filtration type heavy water treatment system | |
| CN205222857U (en) | Reverse osmosis container formula sea water desalination device | |
| CN213493001U (en) | Full-automatic external-pressure internal-suction type membrane filtration system | |
| CN112090281A (en) | Full-automatic external-pressure internal-suction type membrane filtration system and filtration process thereof | |
| CN220149324U (en) | Device for recycling citric acid, reducing consumption and saving water by reclaimed water membrane method | |
| CN202246314U (en) | Water treatment system for polycrystalline silicon production | |
| CN112426886A (en) | Low-consumption high-efficiency flat ceramic membrane microfiltration system based on gas-liquid two-phase flow | |
| CN101830607B (en) | Alternate two-stage aerobic membrane bioreactor | |
| CN104140172A (en) | Seawater desalination pretreatment method | |
| CN208648833U (en) | A kind of double film combination sewage-treatment plants | |
| CN105668952A (en) | Smart two-membrane integrated sewage treatment system | |
| CN213493000U (en) | Full-automatic external-pressure internal-suction type membrane filter | |
| CN216808509U (en) | Movable advanced sewage treatment system based on microorganism embedding construction method | |
| CN214571013U (en) | Leachate and kitchen wastewater MBR system | |
| CN202465450U (en) | Treatment device of electroplating pretreatment waste water | |
| CN202543003U (en) | Landfill leachate treatment device | |
| CN213506113U (en) | Membrane treatment device containing aeration | |
| CN212222745U (en) | Domestic sewage treatment device with integrated membrane bioreactor | |
| CN110776091B (en) | Immersed MBR (membrane bioreactor) in-situ chemical cleaning method without impact influence on sludge activity | |
| CN201809253U (en) | Internal-external membrane filtration and separation sewage treatment device | |
| CN220413095U (en) | Harmless back spraying treatment device for percolate concentrate | |
| CN220664999U (en) | Water purification system based on off-grid solar photovoltaic power generation |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20210622 |