CN201620087U - Single-pump fluid process equipment - Google Patents
Single-pump fluid process equipment Download PDFInfo
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- CN201620087U CN201620087U CN2010201113095U CN201020111309U CN201620087U CN 201620087 U CN201620087 U CN 201620087U CN 2010201113095 U CN2010201113095 U CN 2010201113095U CN 201020111309 U CN201020111309 U CN 201020111309U CN 201620087 U CN201620087 U CN 201620087U
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- pipeline
- recoil
- control valve
- treating plant
- fluid treating
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Abstract
Single-pump fluid process equipment mainly comprises an operation pump, an operation inlet control valve, fluid process equipment, an operation outlet control valve, a reflush outlet control valve, a blow-off line and a great range of detection equipment. The equipment is characterized in that a reflush pipeline is mounted on a pipeline between the operation pump and the operation inlet control valve, the other end of the reflush pipeline is connected with the reflush inlet control valve, and the other end of the reflush inlet control valve is connected with a chamber of the fluid process equipment dedicated for processed fluid through a reflush inlet pipeline. Due to the adoption of the reflush pipeline, the fluid process equipment ensures enhanced reflush performance, improved surface area resilience from material blockage due to filtration, absorption and ion exchange, and facilitated discharge of sticky mud, suspended matter and the like.
Description
Technical field
The utility model relates to a kind of fluid purifying apparatus, refers in particular to a kind of single pump fluid treating plant, can be widely used in fields such as industrial circulating water, pharmacy, chemical industry, civilian recirculated water, environmental engineering, food-processing, central air-conditioning.
Background technology
In the modern industry circulating water system, the drainage of all water treating equipment all is in line from pending chamber, filth-discharging effect is poor, various glutinous mud, mushroom are difficult to break away from water treating equipment treat surface absorption back, equipment is after operation for some time, effect just descends greatly, on fluid treating plant treatment chamber, install the recoil inlet duct now, change the fluid flushing path, improve filth-discharging effect, reduce blindly blowdown, reach the water saving purpose, prolong the duration of service of interior various sorbing materials of fluid treating plant and filtering material.
Summary of the invention
Goal of the invention:
The purpose of this utility model provides a kind of single pump fluid treating plant, this complete equipment mainly is by the recoil pipeline, with various glutinous mud in the pending chamber of fluid treating plant and suspended substance device for transferring, improve the device processes precision, prolong the work-ing life of filtering adsorbing material, reduce the number of times of changing filtering material and sorbing material, reduce the maintenance time of equipment.
Technical scheme
On the circulation main pipe line of industrial cycle water system, and receipts or other documents in duplicate pump fluid treating plant.Fluid intake pipeline (1) connects process pump (2), another termination process pump of process pump (2) connects pipeline (3), process pump connects another termination operation inlet control valve (4) of pipeline (3), another termination operation inlet duct (5) of operation inlet control valve (4), the pending chamber of operation another termination fluid treating plant (6) of inlet duct (5), the pending chamber opening of fluid treating plant (6) is installed recoil outlet conduit (7), another termination of recoil outlet conduit (7) recoil discharge control valve (8), recoil discharge control valve (8) the other end dirty pipeline (9) that runs in; And connect at process pump and to connect recoil pipeline (10) on the pipeline (3), another termination recoil inlet control valve (11) of recoil pipeline (10), another termination recoil inlet duct (12) of recoil inlet control valve (11), another termination fluid treating plant (6) of recoil inlet duct (12) is treatment chamber, fluid treating plant (6) on the treatment chamber perforate connect operation outlet conduit (13), operation outlet conduit (13) connects operation discharge control valve (14), operation discharge control valve (14) connects fluid outlet pipeline (15), at fluid treating plant (6) extreme higher position dress vent valve (16), upward want the setting pressure sensors A at pipeline (3), go up installation flow sensor B at pipeline (5), go up at pipeline (15) water quality testing meter C is installed.
In food service industry such as wine, edible oil or pharmaceutical industries, in the purification system of environmental engineering, single pump fluid handling that various detection systems are installed can directly be connected on the main pipe line of system.
The utility model has an innovation greatly in the industrial cycle water system:
1, the recoil entrance system of Chuan Xin recoil pipeline and recoil inlet control valve and recoil inlet duct composition, various suspended substances in the fluid treating plant and impurity are gone out in the fluid treating plant, make the working efficiency of fluid device can very fast recovery, reduced change filter, absorption, and the number of times of ion-exchange material.
Description of drawings
The invention will be further described below in conjunction with drawings and Examples.
Fig. 1 is a structure iron of the present utility model.
Fig. 2 is the structure iron that the utility model is used among industrial circulating water.
Fig. 3 is the structure iron that the utility model is used in the environmental engineering purification system.
Fig. 4 is the structure iron that the utility model is used in food, medicine, oils industry.
Fig. 5 is the structure iron that the utility model is used in air-purification system.
Embodiment:
Among Fig. 1, fluid intake pipeline (1), process pump (2), process pump connects pipeline (3), operation inlet control valve (4), operation inlet duct (5), fluid processor (6), recoil outlet conduit (7), recoil discharge control valve (8), blow-off line (9), recoil pipeline (10), recoil inlet control valve (11), recoil inlet duct (12), operation outlet conduit (13), operation discharge control valve (14), fluid outlet pipeline (15), vent valve (16), pressure transmitter A, flow sensor B, water quality testing meter C.
In Fig. 1, fluid intake pipeline (1) connects process pump (2), another termination process pump of process pump (2) connects pipeline (3), process pump connects another termination operation inlet control valve (4) of pipeline (3), another termination operation inlet duct (5) of operation inlet control valve (4), the pending chamber of operation another termination fluid treating plant (6) of inlet duct (5), the pending chamber of fluid treating plant (6) connects recoil outlet conduit (7), another termination recoil discharge control valve (8) of recoil outlet conduit (7), recoil discharge control valve (8) the other end dirty pipeline (9) that runs in, connect pipeline (3) upper shed at process pump simultaneously and connect recoil pipeline (10), another termination recoil inlet control valve (11) of recoil pipeline (10), another termination recoil inlet duct (12) of recoil inlet control valve (11), another termination fluid treating plant (6) of recoil inlet duct (12) is treatment chamber, connect operation outlet conduit (13) at fluid treating plant (6) treatment chamber upper shed, another termination operation discharge control valve (14) of operation outlet conduit (13), another termination fluid outlet pipe road (15) of operation discharge control valve (14), and at fluid treating plant (6) highest point installation vent valve (16).
In Fig. 2, on the circulation main pipe line H of industrial circulating water, and receipts or other documents in duplicate pump fluid treating plant.
Open a bypass on the recirculated water main pipe line H and connect fluid intake pipeline (1), another termination process pump (2) of fluid intake pipeline (1), another termination process pump of process pump (2) connects pipeline (3), process pump connects another termination operation inlet control valve (4) of pipeline (3), another termination operation inlet duct (5) of operation inlet control valve (4), the pending chamber of operation another termination fluid treating plant (6) of inlet duct (5), the pending chamber of fluid treating plant (6) connects recoil outlet conduit (7), another termination recoil discharge control valve (8) of recoil outlet conduit (7), recoil discharge control valve (8) the other end dirty pipeline (9) that runs in, connect pipeline (3) upper shed at process pump simultaneously and connect recoil pipeline (10), another termination recoil inlet control valve (11) of recoil pipeline (10), another termination recoil inlet duct (12) of recoil inlet control valve (11), another termination fluid treating plant (6) of recoil inlet duct (12) is treatment chamber, connect operation outlet conduit (13) at fluid treating plant (6) treatment chamber upper shed, another termination operation discharge control valve (14) of operation outlet conduit (13), another termination fluid outlet pipe road (15) of operation discharge control valve (14), and at fluid treating plant highest point installation vent valve (16).
In Fig. 3, in purifying air and food, the pharmaceutical industries purification system, single pump fluid handling backflush device can directly be connected on the circulation main pipe line of the recycle system in the environmental engineering circulating water system.
The utility model is to implement like this in the industrial cycle water system:
1, as Fig. 2, the utility model equipment is connected in parallel on the main pipe line of industrial cycle water system, and when starting the water of this device processes industrial cycle water system, valve (4), valve (14) are opened, and valve (11), valve (8) are closed, and process pump (2) is opened.
Industrial circulating water is flowed through → process pump (2) → pipeline (3) → valve (4) → pipeline (5) → fluid treating plant (6) → pipeline (13) → valve (14) → pipeline (15) → return main pipe line H from pipeline (1).
At this moment the water turbidity in the main pipe line H can As time goes on and constantly reduce, thereby various impurity, suspended substance, microorganism, mushroom etc. are difficult for being deposited in the industrial cycle water system and influence the heat-exchange capacity of total system, reach object of energy saving.
2, the backwash process of the utility model in industrial circulating water:
Shown in figure (2): the utility model equipment moves for some time in the industrial cycle water system after, various detecting instruments, as tensimeter, pressure transmitter pressure rise, the flow sensor flow diminishes, the increase of water quality testing meter turbidity can show that each impurity is too much in the fluid treating plant (6), the equipment claimed back flushing, at this moment close process pump (2), shut-off valve (4), valve (14); Open valve (11), valve (8) are restarted process pump (2) again.The fluid of back flushing is from pipeline (1) → process pump (2) → pipeline (3) → pipeline (10) → valve (11) → pipeline (12) → fluid treating plant (6) → pipeline (7) → valve (8) → blow-off line (9), stop after clear water occurring, whole backwash process is finished.Impurity in fluid treating plant (6) is discharged from fluid treating plant (6), and various absorption, filter core, ion-exchange material obtain regeneration, and the turbidity in the fluid treating plant (6) obviously descends, and has improved the working efficiency of fluid treating plant (6).
The utility model is to implement like this in the environmental engineering system:
1, as shown in Figure 3, when water will be handled among the G of pond, open valve (4), valve (14), shut-off valve (8), valve (11) start process pump (2), and the fluid handling backflush device is started working.
Water is flowed through → process pump (2) → pipeline (3) → valve (4) → pipeline (5) → fluid treating plant (6) → pipeline (13) → valve (14) → pipeline (15) → return pond from pipeline (1).
At this moment various suspended substances, algae, the mushroom in the pond is filtered or is adsorbed onto in the fluid treating plant (6), and as time passes, turbidity descends in the pond, and it is clear that water quality becomes.
2, the backwash process of the utility model in environmental engineering:
As shown in Figure 3, when the utility model was in running order, along with the continuity of working hour, the impurity in the fluid treating plant (6) can get more and more pressure transmitter A
1Pressure increase flow sensor B
1Flow diminishes, water quality testing meter C
1Turbidity become big, the equipment claimed back flushing, at this moment process pump (2) stops, valve (4), valve (14) are closed, and open valve (8), valve (11) then, start process pump (2).
The recoil fluid is flowed through → process pump (2) → pipeline (3) → pipeline (10) → valve (11) → pipeline (12) → fluid treating plant (6) → pipeline (7) → valve (8) → blow-off line from pipeline (1).
The enforcement of the utility model in the purification system of food, pharmacy, oils industry:
1, as shown in Figure 4, the Detection ﹠ Controling of the utility model in the purification system of food (wine), pharmacy, oils industry:
As shown in Figure 4, because of pipeline (12) and pipeline (13) all are installed in same isobaric chamber, according to the fluid characteristics, pipeline (12) can be owned an opening together with pipeline (13), pipeline (12) can be installed on the pipeline (13), pipeline (13) also can be installed on the pipeline (12), now pipeline (13) is installed on the pipeline (12).On pipeline (1), connect a threeway, another edge joint recoil fluid valve of the wine that reception is on one side handled or medicament, oils and control valve X Y, pending control valve for fluids X, pending fluid container W, when the fluid in the W container is carried out purifying treatment, close recoil fluid valve Y, open pending fluid valve X, and simultaneously shut-off valve (8), valve (11), open valve (4), valve (16), start process pump (2).
Fluid is from pending container W pending control valve X → pipeline (1) → process pump (2) → pipeline (3) → valve (4) → pipeline (5) → fluid treating plant (6) → pipeline (13) → valve (14) → pipeline (15) → fluid treatment reservoirs M that flows through.
At this moment treated fluid imports container M, and the fluid turbidity reduces, and various impurity, suspended substance, microorganism, mushroom etc. are deposited in the pending chamber of fluid treating plant (6), thereby fluid obtains purifying.
2, the utility model is at the backwash process of medicine, food-processing.
As Fig. 4, the utility model is in working order the time, along with the prolongation of working hour, impurity can get more and more various detecting instruments in the pending chamber of fluid treating plant (6), show as the data as shown in pressure transmitter, flow sensor, the turbidity detector etc., fluid treating plant need carry out back flushing, at this moment answers pump out of service (2), closes pending fluid valve X, valve (4), valve (14), open recoil fluid valve Y, valve (8), valve (11), restart process pump (2).
The recoil fluid is from valve Y → pipeline (1) → process pump (2) → pipeline (3) → pipeline (10) → valve (11) → fluid treating plant (6) → pipeline (7) → valve (8) → blow-off line (9) → pond for recovering.
The utility model is to implement like this in air:
1, the aerial Detection ﹠ Controling of the utility model:
As shown in Figure 5, because of pipeline (5) and pipeline (7) all are installed in same isobaric chamber, according to the fluid characteristics, pipeline (5) can be owned an opening together with pipeline (7), and pipeline (5) can be installed on the pipeline (7), pipeline (7) also can be installed on the pipeline (5), in like manner, also on same isobaric chamber, pipeline (12) also can be owned same opening together with pipeline (13) for pipeline (12) and pipeline (13), pipeline (12) can be opened on pipeline (13), and pipeline (13) can be opened on pipeline (12).The logical order of its each valve and pump and the logical order of structure iron of the present invention 1 are consistent.Now pipeline (7) is installed on the pipeline (5), pipeline (13) is installed on the pipeline (12), produces figure (5) structure.When air will be handled in the room M, shut-off valve (11), valve (8), open valve (4), valve (14) start process pump (2).
Room M air is from pipeline (T) → pipeline (1) → process pump (2) → pipeline (3) → valve (4) → pipeline (5) → fluid treating plant (6) → pipeline (12) → pipeline (13) → valve (14) → pipeline (15) → pipeline (T) → room.
At this moment air is purified in the room, and each suspended substance in the air obtains removing.
2, the aerial backwash process of the utility model:
As shown in Figure 5, when the utility model is in running order, because the prolongation of working hour, the impurity in fluid treating plant (6) can get more and more, and pending chamber pressure can be increasing, the gaseous mass of having handled can descend, at this moment equipment claimed back flushing, pump at this moment out of service (2), shut-off valve (4), valve (14), open valve (11), valve (8) are restarted process pump (2).
Air is from room M → pipeline (T) → pipeline (1) → process pump (2) → pipeline (3) → pipeline (10) → valve (11) → pipeline (12) → fluid treating plant (6) → pipeline (7) → valve (8) → blow-off line (9) → returnable N.
Claims (4)
1. single pump fluid treating plant, mainly comprise: process pump, operation inlet control valve, fluid treating plant, fluid outlet control valve, blow-off line and various detecting instrument, it is characterized in that: between process pump and operation inlet control valve, the recoil pipeline is installed, after the recoil pipeline the other end connects recoil inlet control valve, be connected on fluid treating plant on the treatment chamber.
2. according to the described a kind of single pump fluid treating plant of claim (1), it is characterized in that: fluid intake pipeline (1) connects process pump (2), another termination process pump connecting tube (3) of process pump (2), another termination operation inlet control valve (4) of process pump connecting tube (3), another termination operation inlet duct (5) of operation inlet control valve (4), the pending chamber of operation another termination fluid treating plant (6) of inlet duct (5), the pending chamber opening of fluid treating plant (6) connects recoil outlet conduit (7), another termination of recoil outlet conduit (7) recoil discharge control valve (8), recoil discharge control valve (8) the other end dirty pipeline (9) that runs in; Go up at process pump connecting tube (3) simultaneously recoil pipeline (10) is installed, another termination recoil inlet control valve (11) of recoil pipeline (10), another termination recoil inlet duct (12) of recoil inlet control valve (11), another termination fluid treating plant (6) of recoil inlet duct (12) is treatment chamber, and perforate on fluid treating plant (6) treatment chamber, installation and operation outlet conduit (13), operation outlet conduit (13) connects operation discharge control valve (14), vent valve (16) is installed at the fluid treating plant highest point in another termination fluid outlet pipe road (15) of operation discharge control valve (14).
3. according to the described a kind of single pump fluid treating plant of claim (1), it is characterized in that: in-service pipeline (5) and recoil outlet conduit (7) are on the pending chamber of same fluid treating plant (6), recoil inlet duct (12) and operation outlet conduit (13) are on the treatment chamber of same fluid treating plant (6), according to the fluidic characteristics, pipeline (5) can be owned an opening together with pipeline (7), and pipeline (5) can be in pipeline (7) upper shed, and pipeline (7) can be in pipeline (5) upper shed; In like manner pipeline (12) also can have same opening with pipeline (13), and pipeline (12) can be in pipeline (13) upper shed, and pipeline (13) also can be in pipeline (12) upper shed.
4. a kind of single pump fluid treating plant according to claim 1, it is characterized in that: each detection system can be contained on each pipeline of fluid treating plant (6).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201113095U CN201620087U (en) | 2010-02-10 | 2010-02-10 | Single-pump fluid process equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201113095U CN201620087U (en) | 2010-02-10 | 2010-02-10 | Single-pump fluid process equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201620087U true CN201620087U (en) | 2010-11-03 |
Family
ID=43023544
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010201113095U Expired - Fee Related CN201620087U (en) | 2010-02-10 | 2010-02-10 | Single-pump fluid process equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201620087U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102145951A (en) * | 2010-02-10 | 2011-08-10 | 冯军 | Single-pump fluid treating equipment |
| CN102789248A (en) * | 2011-05-20 | 2012-11-21 | 长沙旁流水处理设备有限公司 | Temperature control system for negative pressure recoil pump |
| CN102799198A (en) * | 2011-05-21 | 2012-11-28 | 冯军 | Blowdown valve temperature control system |
| CN102799199A (en) * | 2011-05-21 | 2012-11-28 | 冯军 | Inlet valve temperature control system |
-
2010
- 2010-02-10 CN CN2010201113095U patent/CN201620087U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102145951A (en) * | 2010-02-10 | 2011-08-10 | 冯军 | Single-pump fluid treating equipment |
| CN102789248A (en) * | 2011-05-20 | 2012-11-21 | 长沙旁流水处理设备有限公司 | Temperature control system for negative pressure recoil pump |
| CN102799198A (en) * | 2011-05-21 | 2012-11-28 | 冯军 | Blowdown valve temperature control system |
| CN102799199A (en) * | 2011-05-21 | 2012-11-28 | 冯军 | Inlet valve temperature control system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| DD01 | Delivery of document by public notice |
Addressee: Feng Jun Document name: Notification of Termination of Patent Right |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20101103 Termination date: 20150210 |
|
| EXPY | Termination of patent right or utility model |