CN102145951A - Single-pump fluid treating equipment - Google Patents
Single-pump fluid treating equipment Download PDFInfo
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- CN102145951A CN102145951A CN 201010108051 CN201010108051A CN102145951A CN 102145951 A CN102145951 A CN 102145951A CN 201010108051 CN201010108051 CN 201010108051 CN 201010108051 A CN201010108051 A CN 201010108051A CN 102145951 A CN102145951 A CN 102145951A
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Abstract
The invention discloses single-pump fluid treating equipment, which mainly comprises a running pump, a running inlet control valve, fluid treating equipment, a running outlet control valve, a back flushing outlet control valve, a sewage pipeline and various types of detection equipment. The single-pump fluid treating equipment is characterized in that: a back flushing pipeline is arranged on a pipeline between the running pump and the running inlet control valve; the other end of the back flushing pipeline is connected with the back flushing inlet control valve; and the other end of the back flushing inlet control valve is connected to a treated chamber of the fluid treating equipment after passing through the back flushing inlet pipeline. A back flushing system is arranged on the treated chamber of the fluid treating equipment, so that the back flushing effect of the equipment is enhanced, the surface area regeneration effect is higher after various filtering, absorbing and ion exchange materials in the fluid treatment equipment are blocked, and various types of slime, suspended substances and the like are easier to discharge from the fluid treating equipment.
Description
Technical field
The present invention relates to a kind of fluid purifying apparatus, refer 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 invention is to provide 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 filtration, absorption, ion-exchange 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 present invention 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 is installed on the treatment chamber of fluid treating plant (6).Various suspended substances in the fluid treating plant and impurity are gone out in the fluid treating plant, are made 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 invention.
Fig. 2 is the structure iron that the present invention uses among industrial circulating water.
Fig. 3 is the structure iron that the present invention uses in the environmental engineering purification system.
Fig. 4 is the structure iron that the present invention uses in food, medicine, oils industry.
Fig. 5 is the structure iron that the present invention uses 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 present invention implements like this:
1, as Fig. 2, present device 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 present invention in industrial circulating water:
Shown in figure (2): present device is moved 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 present invention implements like this:
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 flows into check valve Z → pipeline (1) and flows through from the pond → process pump (2) → pipeline (3) → valve (4) → pipeline (5) → fluid treating plant (6) → pipeline (13) → valve (14) → pipeline (15) → return pond.
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 present invention in environmental engineering:
As shown in Figure 3, when the present invention was in running order, along with the continuity of working hour, the impurity in the fluid treating plant (6) can get more and more, the pressure of pressure transmitter A1 increases, flow sensor B1 flow diminishes, and it is big that the turbidity of water quality testing meter C1 becomes, 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 present invention in the purification system of food, pharmacy, oils industry:
1, as shown in Figure 4, the Detection ﹠ Controling of the present invention 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, wine that reception is on one side handled or medicament, oils, another edge joint recoil fluid valve of control valve X Y, 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), process pump (2) started.
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 present invention is at the backwash process of medicine, food-processing.
As Fig. 4, the present invention 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 (Q).
The present invention implements like this:
1, the aerial Detection ﹠ Controling of the present invention:
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).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 K, shut-off valve (11), valve (8), open valve (4), valve (14) start process pump (2).
Room K 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 K.
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 present invention:
As shown in Figure 5, when the present invention 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 K → 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 |
|---|---|---|---|
| CN 201010108051 CN102145951A (en) | 2010-02-10 | 2010-02-10 | Single-pump fluid treating equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201010108051 CN102145951A (en) | 2010-02-10 | 2010-02-10 | Single-pump fluid treating equipment |
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| Publication Number | Publication Date |
|---|---|
| CN102145951A true CN102145951A (en) | 2011-08-10 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201010108051 Pending CN102145951A (en) | 2010-02-10 | 2010-02-10 | Single-pump fluid treating equipment |
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Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201267732Y (en) * | 2008-09-25 | 2009-07-08 | 罗兴富 | Backwashing high-efficient defluorination and ferro manganese purifier |
| CN201620087U (en) * | 2010-02-10 | 2010-11-03 | 冯军 | Single-pump fluid process equipment |
-
2010
- 2010-02-10 CN CN 201010108051 patent/CN102145951A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201267732Y (en) * | 2008-09-25 | 2009-07-08 | 罗兴富 | Backwashing high-efficient defluorination and ferro manganese purifier |
| CN201620087U (en) * | 2010-02-10 | 2010-11-03 | 冯军 | Single-pump fluid process equipment |
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Application publication date: 20110810 |