CN205613150U - Intelligent membrane separation integrated equipment - Google Patents
Intelligent membrane separation integrated equipment Download PDFInfo
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- CN205613150U CN205613150U CN201620282268.3U CN201620282268U CN205613150U CN 205613150 U CN205613150 U CN 205613150U CN 201620282268 U CN201620282268 U CN 201620282268U CN 205613150 U CN205613150 U CN 205613150U
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- electromagnetic valve
- control cabinet
- electric control
- head tank
- pressure transducer
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model discloses an intelligent membrane separation integrated equipment, including electrical apparatus switch board, head tank, bag filter and the belt cleaning device who connects gradually, be equipped with the membrane module between head tank and the belt cleaning device, be equipped with in proper order between bag filter and the membrane module all with temperature sensor, booster pump, the preceding pressure sensor of first membrane and first solenoid valve that the electrical apparatus switch board is connected, be equipped with the head tank liquid level detection ware of being connected with the electrical apparatus switch board on the head tank. The protection of this equipment collection automatic operation, self - cleaning, malfunction alerting, trouble autodiagnosis and discharge and film element is as an organic whole, greatly reduced the human cost to the management equipment makes product quality to ensure in order.
Description
Technical field
This utility model belongs to membrane separator technical field, is specifically related to a kind of intelligent membrance separation integrated equipment.
Background technology
Membrane separation plant is based on membrane separation technique, carries out material separation, purifies and concentrate, has many advantages, as can at normal temperatures continuous print operation, without phase change without chemical change；Having energy-conserving and environment-protective and production process not to produce the advantage of pollution in the industrial production, therefore it is swift and violent in field development such as food, medicine, biochemistry.Membrane separation technique refers to that the mixture of different-grain diameter molecule on a molecular scale is when by semipermeable membrane, with semipermeable membrane as selecting barrier layer, then the selectivity (aperture) of film is utilized, the energy difference existed using the both sides of film is as power, other components allowing some component to pass through and to retain in mixture, thus reach the technology separating, purifying or concentrate.
Application of membrane separation technology mainly includes following several types in plant extract research: microfiltration (MF), ultrafiltration (UF), nanofiltration (NF), reverse osmosis (RO).The permeation mechanism of four kinds of films is essentially identical, mainly according to structure and the performance difference of the used film of size of the particle of separated object.Because film has this to be strict with (less than 5um) for the charging of material therefore needs to increase a bag filter before equipment is preposition pretreatment.
At present membrane separation plant produced problem mainly has the following aspects with defect: (1) bag filter separates with membrane separation plant cause space take up an area big, operation is complicated, be not easy to control；(2) using various butterfly valve, stop valve and ball valve to cause manual resource to waste, operation complexity, probability of makeing mistakes is high；(3) permeate end does not installs check valve, liquid backflow after equipment downtime, produces pressure, damages membrane component；(4) there is no automatic service data record, it is impossible to realize data and monitor in real time, fault pre-alarming, malfunction elimination and maintenance difficult, cannot follow the tracks of for service data；(5) there is no temperature, pressure, flow monitoring device, it is impossible to realize the intelligentized automatic operation of membrane separation plant, cleaning automatically, fault alarm, the eliminating of combination record data fault autognostic, cause manpower to waste, increase production cost.
Utility model content
For the above-mentioned problems in the prior art, this utility model provides a kind of intelligent membrance separation integrated equipment, efficiently solve membrane separation plant no pressure, temperature, flow monitoring device, intelligentized automatic operation, cleaning automatically, fault alarm, the eliminating of combination record data fault autognostic can not be realized, manpower is caused to waste, the problem increasing production cost.
For achieving the above object, this utility model solves its technical problem and be the technical scheme is that
A kind of intelligent membrance separation integrated equipment, including the electric control cabinet being sequentially connected with, head tank, bag filter and cleaning device；It is provided with membrane module between described head tank and cleaning device；Be sequentially provided with between described bag filter and membrane module be all connected with electric control cabinet temperature sensor, booster pump, pressure transducer and the first electromagnetic valve before the first film；Described head tank is provided with the head tank liquid level detector being connected with electric control cabinet.
Described equipment also includes pressure transducer and the 8th electromagnetic valve before the second film being all connected with electric control cabinet, and before described second film, pressure transducer and the 8th electromagnetic valve are successively set between cleaning device and membrane module.
Described cleaning device includes cleaning pump, cleaning dosing tank and clean the cleaning dosing tank liquid level detector of liquid level in dosing tank for detecting；Described cleaning pump and cleaning dosing tank liquid level detector are all connected with electric control cabinet.
Described equipment also includes that the 5th electromagnetic valve, the 6th electromagnetic valve and the 7th electromagnetic valve that the second turbine flowmeter, check valve are connected respectively with described check valve, described second turbine flowmeter and check valve are connected in turn clean between dosing tank and membrane module；Described second turbine flowmeter, the 5th electromagnetic valve, the 6th electromagnetic valve and the 7th electromagnetic valve are all connected with electric control cabinet.
Described equipment also includes pressure transducer after the first turbine flowmeter, motor valve and the film being connected with electric control cabinet, and after described first turbine flowmeter, motor valve and film, pressure transducer is successively set between described head tank and membrane module.
Described equipment also includes the second electromagnetic valve, the 3rd electromagnetic valve and the 4th electromagnetic valve being all connected with electric control cabinet, and described 3rd electromagnetic valve and the 4th electromagnetic valve are set in turn between head tank and the first turbine flowmeter.
The charging pump being connected with electric control cabinet it is provided with between described head tank and bag filter.
The pressure transducer being connected with electric control cabinet it is provided with on described bag filter.
This utility model provides a kind of intelligent membrance separation integrated equipment, has following several beneficial effect:
(1) this equipment is provided with temperature, pressure and flow monitoring device, it is connected with electric control cabinet respectively, membrane separating process is realized data monitor in real time, separation process is made to be smoothed out, fault pre-alarming signal can also be sent in advance simultaneously, avoid unnecessary fault or easily find out place of being out of order, and it is quickly repaired.
(2) this equipment integrate automatically run, cleaning, fault alarm, failure self-diagnosis and discharge automatically, greatly reduce human cost, and can orderly management equipment so that product quality is ensured.
(3) signal that the trouble-free operation between bag filter and membrane module can be sent to electric control cabinet by pressure transducer before temperature sensor, booster pump the 7, first film and the first electromagnetic valve 9 or receive controls, simple to operate.
(4) this equipment is provided with check valve, and after equipment downtime, liquid will not reflux, and will not damage membrane component because producing pressure.
(5) this equipment avoids the use of various Hand-operated butterfly valve, stop valve and ball valve, decreases the waste of human resources so that simple to operate, and reduces probability of makeing mistakes.
Accompanying drawing explanation
Fig. 1 is the structural representation of intelligent membrance separation integrated equipment.
Wherein, 1, electric control cabinet；2, head tank；3, charging pump；4, pressure transducer；5, bag filter；6, temperature sensor；7, booster pump；8, pressure transducer before the first film；9, the first electromagnetic valve；10, membrane module；11, pressure transducer after film；12, motor valve；13, the first turbine flowmeter；14, the second electromagnetic valve；15, the 3rd electromagnetic valve；16, the 4th electromagnetic valve；17, the second turbine flowmeter；18, check valve；19, the 5th electromagnetic valve；20, the 6th electromagnetic valve；21, the 7th electromagnetic valve；22, the 8th electromagnetic valve；23, pressure transducer before the second film；24, pump is cleaned；25, dosing tank is cleaned；26, dosing tank liquid level detector is cleaned；27, head tank liquid level detector.
Detailed description of the invention
For making the purpose of this utility model, technical scheme and advantage clearer, below in conjunction with this utility model specific embodiment and corresponding accompanying drawing, technical solutions of the utility model are clearly and completely described.
With reference to Fig. 1, the present embodiment provides a kind of intelligent membrance separation integrated equipment, including electric control cabinet 1, head tank 2, head tank liquid level detector 27, charging pump 3, first pressure transducer 4, bag filter 5, temperature sensor 6, booster pump 7, pressure transducer 8 before first film, first electromagnetic valve 9, membrane module 10, pressure transducer 11 after film, motor valve 12, first turbine flowmeter 13, second turbine flowmeter 17, check valve 18, 6th electromagnetic valve 20, clean pump 24, clean dosing tank 25, clean dosing tank liquid level detector 26, pressure transducer 23 before second film, 8th electromagnetic valve 22, second electromagnetic valve 14, 7th electromagnetic valve 21；
Wherein the head tank liquid level detector 27 on head tank 2 is connected with electric control cabinet 1, for detecting that whether the liquid level in head tank 2 is less than low liquid level, and transfer the signal to the electric control cabinet 1；Head tank 2 is connected by charging pump 3 with bag filter 5, and charging pump 3 one end is connected with electric control cabinet 1, and for receiving the signal sent by raw material, the other end is connected with head tank 2, for the raw material in head tank 2 is sent into bag filter 5；Bag filter 5 is for removing the particle diameter material more than 5um, and the first pressure transducer 4 on bag filter 5 is connected with electric control cabinet 1, whether is higher than 0.35Mpa, and transfer the signal to the electric control cabinet 1 for detecting the pressure in bag filter 5；Pressure transducer 8 and the first electromagnetic valve 9 before temperature sensor 6, booster pump the 7, first film it is sequentially connected with between bag filter 5 and membrane module 10, before temperature sensor simultaneously 6, booster pump the 7, first film, pressure transducer 8 and the first electromagnetic valve 9 are connected with electric control cabinet 1 respectively, whether the first temperature sensor 6 is higher than 45 DEG C, and transfer the signal to the electric control cabinet 1 for detecting the mass temperature after bag filter 5 filters；Pressure transducer 8 and first electromagnetic valve 9 mass temperature after receiving the filtration that electric control cabinet 1 the sends signal equal to or less than 45 DEG C before booster pump the 7, first film, and substance pump is sent into membrane module 10；Membrane module 10 is connected by the second turbine flowmeter 17 with check valve 18, the check valve 18 material after discharging filtration, second turbine flowmeter 17 is also connected with electric control cabinet 1, for the detection flow by membrane module 10, and transfers the signal to the electric control cabinet 1；6th electromagnetic valve 20 one end is connected with electric control cabinet 1, discharges for receiving the material after whether filtering, and the other end is connected with check valve 18, the material after discharging filtration；The cleaning dosing tank liquid level detector 26 cleaned on dosing tank 25 is connected with electric control cabinet 1, whether is less than low liquid level, and transfer the signal to the electric control cabinet 1 for detecting the liquid level cleaned in dosing tank 25；Clean and between dosing tank 25 and membrane module 10, be sequentially connected with pressure transducer 23 and the 8th electromagnetic valve 22 before cleaning pump the 24, second film, before cleaning pump the 24, second film, pressure transducer 23 and the 8th electromagnetic valve 22 are connected with electric control cabinet 1 respectively, for receiving the purge signal that electric control cabinet 1 sends, and cleanout fluid is sent to membrane module 10；Pressure transducer 11 after film, motor valve 12 and the first turbine flowmeter 13 it is sequentially connected with between membrane module 10 and the second electromagnetic valve 14, motor valve 12 is also connected with electric control cabinet 1, for receiving the purge signal that electric control cabinet 1 sends, and valve is opened releasing cleanout fluid；After film, pressure transducer 11 is also connected with electric control cabinet 1, for pressure value signal is sent to electric control cabinet 1；First turbine flowmeter 13 is also connected with electric control cabinet 1, for cleanout fluid flow signal is sent to electric control cabinet 1；Second electromagnetic valve 14 be also connected with electric control cabinet 1, discharge for receiving the signal discharged by cleanout fluid that electric control cabinet 1 sends cleanout fluid；7th electromagnetic valve 21 is connected with check valve 18, is also connected with electric control cabinet 1, for receiving the signal discharged by cleanout fluid that electric control cabinet 1 sends and will discharge from check valve 18 cleanout fluid out.
Being provided with the 5th electromagnetic valve 19 between check valve 18 and cleaning dosing tank 25, the 5th electromagnetic valve 19 is also connected with electric control cabinet 1.Cleaning dosing tank 25 and be also associated with the 4th electromagnetic valve 16, the 4th electromagnetic valve 16 is also connected with electric control cabinet 1.Being provided with the 3rd electromagnetic valve 15 between first turbine flowmeter 13 and head tank 2, the 3rd electromagnetic valve 15 is also connected with electric control cabinet 1.8th electromagnetic valve 22 and the first electromagnetic valve 9 start time different.
nullThe method of operation is: have the program finished in electric control cabinet 1，During normal operation mode, whether head tank liquid level detector 27 detects head tank 2 less than low liquid level，When being in low liquid level, background program does not runs and alarm indicator head tank 2 does not has material，Head tank liquid level detector 27 detects charging pump 3 when head tank 2 is not less than low liquid level and starts，Pressure transducer 4 runs and provides detection，When detecting numerical value higher than 0.35Mpa, system stops and triggering warning system，Prompting bag filter 5 blocks，When pressure is less than or equal to 0.35Mpa，System normal operating temperature sensor 6 is started working，When detecting temperature higher than 45 DEG C, system stops and triggering warning system，Prompt system feeding temperature is overheated，As during less than or equal to 45 DEG C, temperature sensor 6 normally detects，Booster pump 7 runs，Before first film, pressure transducer 8 is properly functioning，First electromagnetic valve 9 is opened，8th electromagnetic valve 22 cuts out，After film, pressure transducer 11 is properly functioning and provides pressure data to monitor，Motor valve 12 works and waits slowly closing after the time that program setting is good，After regulation pressure makes film, pressure transducer 11 reaches setup pressure value，First turbine flowmeter 13 is properly functioning and points out detection data，Second electromagnetic valve 14、4th electromagnetic valve 16 cuts out，3rd electromagnetic valve 15 is opened，Second turbine flowmeter 17 is properly functioning and points out detection data，Check valve 18 normally works，7th electromagnetic valve 21、5th electromagnetic valve 19 cuts out，6th electromagnetic valve 20 is opened；
When after pressure transducer 8 and film before Automatic Program detects the second turbine flowmeter 17 pressure transducer 11 constant pressure down-off drops to default value or the first film after film, pressure transducer 11 difference reaches default value, normal operation mode is by setting value program stopped and triggers cleaning model；
nullClean dosing tank liquid level detector 26 under cleaning model and whether run the liquid level of detection cleaning dosing tank 25 less than low liquid level，During low liquid level, background program does not runs and alarm indicator is cleaned dosing tank 25 and do not had cleanout fluid，Clean cleaning pump 24 when dosing tank 25 is not less than low liquid level to start，Before second film, pressure transducer 23 is properly functioning and provides pressure data to detect，8th electromagnetic valve 22 is opened，First electromagnetic valve 9 cuts out，Motor valve 12 works，Wait slowly closing after the time that program setting is good，After regulation pressure makes film, pressure transducer 11 reaches setup pressure value，First turbine flowmeter 13 is properly functioning and points out detection data，3rd electromagnetic valve 15、4th electromagnetic valve 16 cuts out，Second electromagnetic valve 14 is opened，Second turbine flowmeter 17 is properly functioning and points out detection data，Check valve 18 normally works，5th electromagnetic valve 19、6th electromagnetic valve 20 cuts out，7th electromagnetic valve 21 is opened，When reaching programmed values，Second electromagnetic valve 14 and the 3rd electromagnetic valve 15 are closed，4th electromagnetic valve 16 is opened，6th electromagnetic valve 20 and the 7th electromagnetic valve 21 are closed，5th electromagnetic valve 19 is opened；
When after pressure transducer 8 and film before Automatic Program detects the second turbine flowmeter 17 pressure transducer 11 constant pressure down-off rises to default value or the first film after film, pressure transducer 11 difference reaches default value, cleaning model pattern is by setting value program stopped and triggers normal operation mode.
Above-mentioned embodiment is used for illustrating this utility model; rather than this utility model is limited; in spirit of the present utility model and scope of the claims, any modifications and changes that this utility model is made, both fall within protection domain of the present utility model.
Claims (8)
1. an intelligent membrance separation integrated equipment, it is characterised in that include electric control cabinet, head tank, bag filter and the cleaning device being sequentially connected with；It is provided with membrane module between described head tank and cleaning device；Be sequentially provided with between described bag filter and membrane module be all connected with described electric control cabinet temperature sensor, booster pump, pressure transducer and the first electromagnetic valve before the first film；Described head tank is provided with the head tank liquid level detector being connected with electric control cabinet.
Intelligent membrance separation integrated equipment the most according to claim 1, it is characterized in that, also including pressure transducer and the 8th electromagnetic valve before the second film being all connected with electric control cabinet, before described second film, pressure transducer and the 8th electromagnetic valve are successively set between cleaning device and membrane module.
Intelligent membrance separation integrated equipment the most according to claim 1 and 2, it is characterised in that described cleaning device includes cleaning pump, cleaning dosing tank and clean the cleaning dosing tank liquid level detector of liquid level in dosing tank for detecting；Described cleaning pump and cleaning dosing tank liquid level detector are all connected with electric control cabinet.
Intelligent membrance separation integrated equipment the most according to claim 3, it is characterised in that also include the second turbine flowmeter, check valve and the 5th electromagnetic valve, the 6th electromagnetic valve and the 7th electromagnetic valve being connected respectively with described check valve；Described second turbine flowmeter and check valve are successively set between cleaning dosing tank and membrane module；Described second turbine flowmeter, the 5th electromagnetic valve, the 6th electromagnetic valve and the 7th electromagnetic valve are all connected with electric control cabinet.
Intelligent membrance separation integrated equipment the most according to claim 1, it is characterized in that, also including pressure transducer after the first turbine flowmeter, motor valve and the film being connected with electric control cabinet, after described first turbine flowmeter, motor valve and film, pressure transducer is successively set between described head tank and membrane module.
Intelligent membrance separation integrated equipment the most according to claim 5, it is characterized in that, also including the second electromagnetic valve, the 3rd electromagnetic valve and the 4th electromagnetic valve being all connected with electric control cabinet, described 3rd electromagnetic valve and the 4th electromagnetic valve are set in turn between head tank and the first turbine flowmeter.
Intelligent membrance separation integrated equipment the most according to claim 1, it is characterised in that be provided with the charging pump being connected with electric control cabinet between described head tank and bag filter.
Intelligent membrance separation integrated equipment the most according to claim 1, it is characterised in that be provided with the pressure transducer being connected with electric control cabinet on described bag filter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620282268.3U CN205613150U (en) | 2016-04-07 | 2016-04-07 | Intelligent membrane separation integrated equipment |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620282268.3U CN205613150U (en) | 2016-04-07 | 2016-04-07 | Intelligent membrane separation integrated equipment |
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| Publication Number | Publication Date |
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| CN205613150U true CN205613150U (en) | 2016-10-05 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201620282268.3U Expired - Fee Related CN205613150U (en) | 2016-04-07 | 2016-04-07 | Intelligent membrane separation integrated equipment |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115754193A (en) * | 2022-11-04 | 2023-03-07 | 哈尔滨乐普实业有限公司 | Digital membrane module and method thereof |
-
2016
- 2016-04-07 CN CN201620282268.3U patent/CN205613150U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115754193A (en) * | 2022-11-04 | 2023-03-07 | 哈尔滨乐普实业有限公司 | Digital membrane module and method thereof |
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Legal Events
| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20161005 Termination date: 20190407 |
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| CF01 | Termination of patent right due to non-payment of annual fee |