CN105668841A - Manufacturing method of integrated full-automatic backwash ultra-filter machine - Google Patents
Manufacturing method of integrated full-automatic backwash ultra-filter machine Download PDFInfo
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- CN105668841A CN105668841A CN201510798537.1A CN201510798537A CN105668841A CN 105668841 A CN105668841 A CN 105668841A CN 201510798537 A CN201510798537 A CN 201510798537A CN 105668841 A CN105668841 A CN 105668841A
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- China
- Prior art keywords
- filter
- water
- container
- core shell
- ultra
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- 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.)
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Classifications
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/42—Treatment of water, waste water, or sewage by ion-exchange
- C02F2001/425—Treatment of water, waste water, or sewage by ion-exchange using cation exchangers
Abstract
A manufacturing method of an integrated full-automatic backwash ultra-filter machine. The ultra-filter machine includes a micro-computer control system device and an ultra-filter membrane filtering apparatus. A left annular filter plate and a right annular filter plate are arranged in a sealed container. A plurality of circular holes are formed in the left filter plate, a filter head having a short handle is arranged in each hole. A KDF55 filter layer and an activated carbon filter layer are arranged on the surface of each filter head. A filter core, which is composed of a filter core shell, an ultra-filter film and a resin filter bag, is fixed to the center of the right annular filter plate. A plurality of water inlet seams are formed all over in an arc-shaped top of the filter core shell. The ultra-filter core is disposed in the middle-upper part of the filter core shell and the resin filter bag is arranged in the middle-lower part of the filter core shell. Two annular fixing hoops are arranged at the two ends of the cylinder body. A water inlet and a backwash sewage draining outlet are disposed on the left side of the container. A filler inlet and outlet is disposed on the upper part of the container. A backwash sewage draining outlet is disposed on the lower part of the cylinder body. A water outlet is arranged on the right side of the container. The water outlet of the filter apparatus is connected to a water inlet of an external pipeline. The ultra-filter machine is economic and practical.
Description
Technical field
This is bright relate to water correction plant, the manufacture field of the ultrafilter of the drinking water used especially for urban households and enterprises and institutions.
Background technology
World Health Organization's investigation is pointed out, human diseases 80% is relevant with water. the main sterilization method of tap water is chlorination sterilization, although a large amount of antibacterial can be removed, but there is also harmful substance, especially the heavy metal in water, the compositions such as chlorine molecule and nitrite, course of conveying simultaneously, water tower storage etc. all causes a degree of secondary pollution, although by water boil, but the harmful substances such as heavy metal in water cannot be removed, the Excess free enthalpy of these materials, human body can be caused great harm, threaten the healthy of the mankind, the part of town and country tap water exceeds standard, do not reach People's Republic of China's new " drinking water sanitary standard ", and the present situation of above-mentioned pollution constitutes the great threat to town and country personnel health.
Now known water purifier product design simple structure on the market, with low content of technology, there is certain defect in design and manufacture, especially the multistage back flush discharge of sewage has been become a technical bottleneck of this series products, existing product is mainly based upon the general purification to city tap-water, reach the purpose of Drinking Water and design, can not solve after rural and urban population directly adopts tap water water source purified, to be better than People's Republic of China's new " drinking water sanitary standard ", become the purpose directly drunk. As: Chinese patent literature discloses one " General water purification " (sy188242019) and " water-purifying filter " (Sy168246427), and both, with tap water for water source, adopts PP filtration core, and active carbon purifying sterilization processing becomes Drinking Water.
Summary of the invention
It is an object of the invention to provide the manufacture method of a kind of integrated full-automatic back flush ultrafiltration machine, with solve town and country exceed standard tap water purified after be better than the problem of the People's Republic of China's new " drinking water sanitary standard ". the purpose of the present invention is realized by techniques below scheme: the manufacture method of a kind of integrated full-automatic back flush ultrafiltration machine, system and device is controlled including microcomputer program, cocoanut active charcoal filter course, KDF55 filter course, it is characterized in that, also there is ultrafiltration membrane filter element and cation exchange resin defecator: it is closed and is provided with left annular filter plate and right toroidal membrane in container, left annular filter plate has several circular port, its hole is equipped with short-handled filter head, filter surface configuration has KDF55 filter course, active carbon filtration layer, right toroidal membrane centre bore is fixed with a filter element being made up of filter-core shell and ultrafilter membrane and cation exchange resin filter bag, the arc top of filter-core shell spreads all over and has inlet opening, apopore is had bottom filter-core shell, described ultrafiltration membrane filter element and cation exchange resin filter bag are arranged on the middle part of filter-core shell, water inlet it is provided with on the left of container, back flush discharge mouth, filler intake-outlet it is provided with on the left of upper vessel portion, back flush discharge mouth it is provided with on the right side of lower vessel portion, outlet it is provided with on the right side of container,The described outlet of former water connects with the water inlet of defecator, and the outlet of defecator connects with the water inlet of external pipeline.
Also there is microcomputer program and control system and device: its device is provided with unitary one-piece computer circuitry plate, select chip microprocessor, and it is provided with the parts compositions such as special Voltage stabilizing module, duty nixie display, output control relay, it is additionally provided with ancillary circuit elements quartz crystal, drives audion, drives audion, drives audion, buzzer; Control circuit is provided with three tunnel inputs: state-detection input, state-detection input, operational mode switch; Three tunnels control output: blowdown controls output, blowdown controls output, water inlet complex controll output; Input, output control signal and power supply are connected by five-pointed star socket with external control component, and+24V power supply inputs, common ground; Micro processor leg: output port, output port, output port, LCD display port, input port, input port, input port, power port, crystal ports, crystal ports; Described 24V positive source is connected with external 24V supply socket positive pole; Power cathode is connected with the public negative pole of electromagnetic valve, and is connected with external 24V supply socket negative pole; Complex controll exports, and connects normally open solenoid valve T3 positive pole; Blowdown controls output, connects normally closed solenoid valve T2 positive pole; Blowdown controls output, connects normally closed solenoid valve T1 positive pole.
In above-mentioned design, the present invention adopts multistage multilayer integrated filtering device and microcomputer program to control system and device with the needs for urban households and enterprises and institutions' drinking water treatment. Such as tap water that the part in town and country is exceeded standard, after it is carried out cocoanut active charcoal filtration by the present invention, carry out KDF55 filtration again, hollow fiber ultrafiltration membrane filters, cation exchange resin filters and antibacterial process.
Compared with prior art (on the basis that existing PP cotton is filtered and active carbon purifying processes), the present invention is directed to tap water water source, town and country, adding twin-stage sewage backwash system, cocos active carbon filtration, KDF55 filtration, hollow fiber ultrafiltration membrane filtration, cation exchange resin filtration etc. process step. In the present invention, twin-stage sewage backwash system can effectively discharge the various harmful substances being suspended in filter cylinder water body, utilizes pressure bounce-back filter element and filtering layer, emission index is up to more than 97%, effectively preventing out aqueous metamorphism, monolithic computer chip controls, and has automatic detection function; Health is threatened the granulometric impurity in maximum chlorine residue, abnormal flavour, heterochromatic, foreign odor thing, pesticide, chloroform and water by cocos active carbon energy active adsorption water, stops the harmful substances such as antibacterial, chemical substance and heavy metal element, remove the Organic substance in water, retain the mineral that human body is useful and trace element; KDF55 can remove the chlorine residue in water, remove soluble heavy metal, control growth of microorganism, stop the accumulation of hard scale, deironing, reduce fluoride, nitrate, sulfate, well water can be purified, remove the chlorine in tap water, antibacterial and algae, the filter membrane of protection ultrafiltration and reduce mineral scale and suppress microbial reproduction; Ultrafilter membrane can effectively remove the silt in water, rust, float, colloid, antibacterial, virus, reduction hardness of water, separates 0.001 micron of aperture, and filter efficiency is up to more than 99.8%; Cation exchange resin filter bag can effectively remove the calcium in water, magnesium ion, can demineralized water, the harmful substance such as larger molecular organics, retain the mineral that human body is useful and trace element, improve mouthfeel, make water quality glycol more sweet.
The present invention has a characteristic that 1, can effectively discharge the various harmful substances being suspended in filter cylinder water body, utilizes pressure bounce-back filter element and filtering layer, and emission index, up to more than 97%, effectively prevents out aqueous metamorphism, and monolithic computer chip controls, and has automatic detection function. 2, the granulometric impurity in water, health threatened in maximum chlorine residue, abnormal flavour, heterochromatic, foreign odor thing, pesticide, chloroform and water can be adsorbed, stop the harmful substances such as antibacterial, chemical substance and heavy metal element, remove the Organic substance in water, retain the mineral that human body is useful and trace element. 3, the chlorine residue in water can be removed; remove soluble heavy metal; control growth of microorganism; stop the accumulation of hard scale; deironing, reduce fluoride, nitrate, sulfate, well water can be purified, remove the chlorine in tap water, antibacterial and algae, the filter membrane of protection ultrafiltration and reduce mineral scale and suppress microbial reproduction. 4, effectively removing the silt in water, rust, float, colloid, antibacterial, virus, reduction hardness of water, separate 0.001 micron of aperture, filter efficiency is up to more than 99.8%. 5, can effectively remove the calcium in water, magnesium ion, can demineralized water, the harmful substance such as larger molecular organics, retain the mineral that human body is useful and trace element, improve mouthfeel, so that water quality glycol more is sweet. 6, after filtering, water quality is better than People's Republic of China's new " drinking water sanitary standard ".
The present invention is economic and practical, and floor space is little, is particularly suitable for urban households and enterprises and institutions use, and can install one by each household.
Accompanying drawing explanation
Below in conjunction with drawings and Examples, the invention will be further described
Fig. 1 is the device connection diagram of one embodiment of the invention;
Fig. 2 is the structure chart of ultrafiltration membrane filter device shown in Fig. 1;
Fig. 3 is the circuit theory diagrams of the device of Full-automatic microcomputer program control system shown in Fig. 1.
Detailed description of the invention
Fig. 1 illustrates that the water treatment facilities of the present invention is equipped with automatic pollution discharge and controls the situation of system and device, for town-dweller-rural-family and enterprises and institutions are used, then directly tap water is introduced, and sends into by the road in apparatus of the present invention and be filtered processing, the water after process through valve 9 outwards export for. Such as former water pressure deficiency, booster pump can be added.
In Fig. 2, the closing container that ultrafiltration membrane filter device 4 is made up of cylinder 4b and right end socket 4a, cylinder 4b and right end socket 4a spiral connect, this container is provided with left annular filter plate 29, right toroidal membrane 31, left filter plate has several circular port, being equipped with short-handled filter head 30 on circular port, filter surface configuration has KDF55 filter course 28(granularity to be about 0.6mm), cocoanut active charcoal filter course 27(granularity be about 0.9mm), the gross thickness > 0.39m of above-mentioned filtering layer; Right toroidal membrane centre bore is fixed with a filter element being made up of filter-core shell and ultrafilter membrane and cation exchange resin filter bag, the arc top 32 of filter-core shell spreads all over and has water gap, the bottom of filter-core shell 35 has apopore, described ultrafiltration core is arranged on the upper middle part 33 of filter-core shell, to be arranged on the lower middle part 34(granularity of filter-core shell be 0.5-0.8mm to cation exchange resin filter bag), the gross thickness > 0.16m of above-mentioned filter bag; Two of cylinder is each provided with an annular and installs clips 36, water inlet 4c, backwash one-level sewage draining exit 4e it is provided with on the left of container, be provided with on filler import and export its mouth of 37(on the left of upper vessel portion and be provided with sealing lid, spiral connects), it is provided with two grades of sewage draining exit 4f of backwash on the right side of lower vessel portion, container right flank is provided with outlet 4d;In this container, activated carbon filter layer 27 is provided above annular separated material sieve 26, and it spreads all over water hole, plays distribution and the filler buffer action of water. It is lined with filter cloth between above-mentioned filtering layer.
The filter-core shell of above-mentioned filter element is upper and lower two sections, is connected with right toroidal membrane 31 spiral respectively. Especially, filter-core shell can be divided into an arc top 32(to have gap) it is connected with hypomere filter-core shell 35, filter-core shell is provided with ultrafiltration core 33, cation exchange resin filter bag 34, housing bottom has apopore.
In Fig. 3, microcomputer program controls the control system that system and device 5 is made up of with external control component circuit board schematic diagram 5b, the core of this control circuit system is a piece of microprocessor 40, being additionally provided with Voltage stabilizing module 41, duty nixie display 51, output control relay 48, contact 59, output control relay 49, contact 60, other ancillary circuit elements has quartz crystal 56, drives audion 45, drives audion 46, drives audion 47, buzzer 58; Control circuit is provided with three tunnel inputs, state-detection input 35, state-detection input 36, operational mode switch 55; Three tunnels control output: blowdown controls output 37, blowdown controls output 38, water inlet complex controll output 39; Input, output control signal and power supply are connected by five-pointed star socket 65 with external control component ,+24V power supply input 63, common ground 64; Micro processor leg: output port 42, output port 43, output port 44, LCD display port 50, input port 52, input port 53, input port 54, power port 57, crystal ports 61, crystal ports 62.
Referring to Fig. 1, from the process that water processes, former water enters from the water inlet 4c the container of ultrafiltration membrane filter device through valve 6 and electromagnetic valve 7 and valve 8, (now, backwash manual drain valve 11 and 13 on external pipe is closed), after multilamellar ultrafiltration sterilizes, flow out from the outlet 4d the right flank of container, become pure water, through valve 9 outwards export for. the above-mentioned outlet of former water connects with the water inlet of ultrafiltration membrane filter device, and the outlet of ultrafiltration membrane filter device connects with the water inlet of external pipeline. above-mentioned it was cleaned the sewage filtered and all kinds of harmful substance is stored in filter cylinder and blowdown pipe network temporarily, await orders in the instruction of Full-automatic microcomputer program control system device, normally opened electromagnetic valve controls switching water body, water supply network water route pressure is saved in cylinder or pot type filter element filter cylinder, complete storage pressure, automatically cut off into water by normally open solenoid valve during blowdown, meanwhile, two-stage normally closed solenoid valve automatically opens up, release pressure, constitute trapway passage, filtering layer and filter element are rinsed in the outburst release reverse flow of rear class pressure store, so that sewage flows out from sewage draining exit automatically, complete sewage backwash overall process, drain valve 11 and 13 on manual blowdown mouth, is use when not using similar folk power supply condition or having folk power supply condition and have a power failure, and is a kind of interim emergent blowoff valve. above-mentioned normally open solenoid valve controls the outlet of device and connects with the water inlet of water purifier, the water inlet that the one-level sewage draining exit of water purifier controls device with preposition normally closed solenoid valve connects, preposition normally closed solenoid valve controls the outlet of device and connects with the water inlet of one-level blowdown pipe network, the water inlet that two grades of sewage draining exits of water purifier control device with rearmounted normally closed solenoid valve connects, and rearmounted normally closed solenoid valve controls the outlet of device and the water inlet connection of two grades of blowdown pipe networks.
Additionally, a control panel can be arranged, it arranges control knob and nixie display, above-mentioned control system and device is placed on panel, becomes as a whole, to facilitate use.
Claims (6)
1. the manufacture method of integrated full-automatic back flush ultrafiltration machine, system and device is controlled including microcomputer program, cocoanut active charcoal filter course, KDF55 filter course, it is characterized in that, also there is ultrafiltration membrane filter element and cation exchange resin defecator (4): it is closed and is provided with left annular filter plate (29) in container, right toroidal membrane (31), left filter plate has several circular port, circular port is equipped with short-handled filter head (30), filter surface configuration has KDF55 filter course (28), cocoanut active charcoal filter course (27), right toroidal membrane centre bore is fixed with a filter element being made up of filter-core shell and ultrafilter membrane and cation exchange resin filter bag, the arc top (32) of filter-core shell spreads all over and has water gap, the bottom of filter-core shell (35) has apopore, described ultrafiltration core is arranged on the upper middle part (33) of filter-core shell, cation exchange resin filter bag is arranged on the lower middle part (34) of filter-core shell, two of cylinder is each provided with an annular and installs clips (36), water inlet (4c) it is provided with on the left of container, it is provided with filler on the left of upper vessel portion and imports and exports (37), container right flank is provided with outlet (4d), the outlet of described former water connects with the water inlet (4c) of defecator (4), and the outlet of defecator (4) connects with the water inlet of external pipeline.
2. ultrafilter according to claim 1, it is characterized in that, also having microcomputer program and control system and device (5): be provided with unitary one-piece computer circuitry plate in its device, the core controlling circuit system is a piece of microprocessor (40), is additionally provided with Voltage stabilizing module (41), duty nixie display (51), output control relay (48), contact (59), output control relay (49), contact (60), other ancillary circuit elements has quartz crystal (56), drive audion (45), drive audion (46), drive audion (47), buzzer (58), control circuit is provided with three tunnel inputs, state-detection input (35), state-detection input (36), operational mode switch (55), three tunnels control output, blowdown controls output (37), blowdown controls output (38), water inlet complex controll output (39), five-pointed star socket (65) will input, output control signal and power supply are connected with external control component ,+24V power supply input (63), common ground (64), micro processor leg: output port (42), output port (43), output port (44), LCD display port (50), input port (52), input port (53), input port (54), power port (57), crystal ports (61), crystal ports (62), described 24V positive source is connected with external 24V supply socket positive pole, power cathode is connected with the public negative pole of electromagnetic valve, and be connected with external 24V supply socket negative pole, complex controll exports, and connects normally open solenoid valve T3 positive pole, blowdown controls output, connecing normally closed solenoid valve T2 positive pole, blowdown controls output, connects normally closed solenoid valve T1 positive pole.
3. ultrafilter according to claim 1, it is characterised in that in the container of described ultrafiltration membrane filter element and cation exchange resin defecator (4), activated carbon filter layer (27) is provided above annular separated material sieve (26).
4. ultrafilter according to claim 3, it is characterized in that, the granularity of the KDF55 filtering layer in the container of described ultrafiltration membrane filter element and cation exchange resin defecator (4) is about 0.6mm, the granularity of cocoanut active charcoal filtering layer is about 0.9mm, total thickness of filter bed > 0.39m, the granularity of cation exchange resin filter bag is 0.5-0.8mm, total thickness of filter bed > 0.16m.
5. ultrafilter according to claim 4, it is characterised in that the container of described ultrafiltration membrane filter element and cation exchange resin defecator (4) is spun formed by cylinder and right end socket; Described filter-core shell is upper and lower two sections, is connected with right toroidal membrane (31) spiral respectively.
6. ultrafilter according to claim 5, it is characterized in that, it is provided with backwash one-level sewage draining exit (4e) on the left of the cylinder of described ultrafiltration membrane filter element and cation exchange resin defecator (4), on the right side of cylinder bottom, is provided with two grades of sewage draining exits (4f) of backwash.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510798537.1A CN105668841A (en) | 2015-11-19 | 2015-11-19 | Manufacturing method of integrated full-automatic backwash ultra-filter machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510798537.1A CN105668841A (en) | 2015-11-19 | 2015-11-19 | Manufacturing method of integrated full-automatic backwash ultra-filter machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105668841A true CN105668841A (en) | 2016-06-15 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510798537.1A Withdrawn CN105668841A (en) | 2015-11-19 | 2015-11-19 | Manufacturing method of integrated full-automatic backwash ultra-filter machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105668841A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106336037A (en) * | 2016-08-30 | 2017-01-18 | 江苏万邦达环保科技有限公司 | Multi-stage filtering type sewage treatment equipment |
| CN108328792A (en) * | 2018-02-08 | 2018-07-27 | 宁波鑫隆净化设备有限公司 | Intelligent filtering purifies water dispenser and its application method |
-
2015
- 2015-11-19 CN CN201510798537.1A patent/CN105668841A/en not_active Withdrawn
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106336037A (en) * | 2016-08-30 | 2017-01-18 | 江苏万邦达环保科技有限公司 | Multi-stage filtering type sewage treatment equipment |
| CN108328792A (en) * | 2018-02-08 | 2018-07-27 | 宁波鑫隆净化设备有限公司 | Intelligent filtering purifies water dispenser and its application method |
| CN108328792B (en) * | 2018-02-08 | 2023-11-17 | 宁波鑫隆净化设备有限公司 | Intelligent filtering water purifier and use method thereof |
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Application publication date: 20160615 |
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| WW01 | Invention patent application withdrawn after publication |