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CN202080908U - Single pump negative pressure operation and self pressure back-flushing fluid treatment device - Google Patents

Single pump negative pressure operation and self pressure back-flushing fluid treatment device Download PDF

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Publication number
CN202080908U
CN202080908U CN2010205095306U CN201020509530U CN202080908U CN 202080908 U CN202080908 U CN 202080908U CN 2010205095306 U CN2010205095306 U CN 2010205095306U CN 201020509530 U CN201020509530 U CN 201020509530U CN 202080908 U CN202080908 U CN 202080908U
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CN
China
Prior art keywords
fluid
treatment device
pipeline
control valve
treating plant
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Expired - Fee Related
Application number
CN2010205095306U
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Chinese (zh)
Inventor
冯军
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Individual
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Individual
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Priority to CN2010205095306U priority Critical patent/CN202080908U/en
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Publication of CN202080908U publication Critical patent/CN202080908U/en
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Expired - Fee Related legal-status Critical Current

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Abstract

A single pump negative pressure operation and self pressure back-flushing fluid treatment device mainly comprises a fluid inlet control valve, a fluid outlet control valve, a process pump, a cavity of the fluid treatment device, a back-flushing control valve, a blow down valve, a blow-off line and an exhaust valve, and is mainly characterized in that the cavity of the fluid treatment device is in a negative pressure operation state in the running process of the fluid treatment device; and the cavity of the fluid treatment device is in a positive pressure state in the back-washing process of the device, back-flushing fluid is the fluid in the system to be treated, and the pressure of the back-flushing fluid is determined by the self pressure of the fluid in a system to be treated, so that other pumps are not needed for pressurization. Through the adoption of a new structure, when the single pump fluid treatment device with a back-flushing system is in running, the cavity of the fluid treatment device is in a negative-pressure working state, when the device is in the back washing process, the cavity of the fluid treatment device is in a positive-pressure state, and the pressure of the back-flushing fluid is decided by the self pressure of the fluid in the system to be treated, so that other pumps are not needed for pressurization. As back washing pipelines are not required to be laid, the structure has the characteristics of safe operation, low construction cost and convenience in operation.

Description

A kind of single pump negative pressure operation is from pressing the recoil fluid treating plant
Technical field
The utility model relates to a kind of fluid purifying apparatus, refer in particular to a kind of single pump negative pressure operation from pressing the recoil fluid treating plant, can be widely used in industrial circulating water, civilian recirculated water, pharmacy, environmental engineering, electric power, central air-conditioning, the circulating water system in fields such as chemical industry, light industry, oil, food-processing, metallurgy, medical treatment.
Background technology
In modern industry recirculated water fluid treatment facility, the by-pass flow formula fluid treating plant of all single pump band back-purge systems does not all have single pump negative pressure operation from the design of pressing recoil, present side stream treatment facility negative pressure operation all is through water pump pressurization recoil, complex structure, particularly in the scrap build engineering, do not consider the side stream processing scheme because of original design, the laying of recoil fluid line just becomes a difficult problem, if in the industrial cycle water system, adopt intrasystem water again without water pump pressurization recoil, move saferly, structure is simpler, the manufacturing of slave unit, expense is cheaper on the installation cost, and staff's operation is easier.
Summary of the invention
Goal of the invention:
The utility model provides a kind of single pump negative pressure operation from pressing the recoil fluid treating plant, the purpose of this invention for apparatus is to save the expense and the trouble of laying a back flushing pipeline, allow the equipment can safe operation under the working order of negative pressure simultaneously, this structure be particularly suitable for improvement project.
Technical scheme
Process pump with after the fluid outlet control valve is connected again with the series-parallel connection body of recoil control valve generation in parallel together be installed in fluid treating plant treatment chamber to the pipeline of the recycle system.
The fluid intake control valve is installed on the fluid intake pipeline of the pending chamber of fluid treating plant.
As Fig. 1, make a single pump negative pressure operation from pressing the recoil fluid treating plant to form by five major parts:
1. the fluid treating plant cavity W=fluid treating plant cavity W pending chamber of treatment chamber+fluid treating plant cavity W+vent valve X.
2. fluid moves inlet part=fluid intake pipeline A+ fluid intake control valve A 1+ fluid intake pipeline A 2, a wherein end of fluid intake pipeline A is installed on the pending chamber of fluid treating plant cavity W.
3. blowdown exports part=blow-off line B+ blowdown control valve B 1+ blow-off line B 2, the blow-off line B the other end is installed on the pending chamber of fluid treating plant cavity W.
4. the fluid operation exports part=fluid outlet pipeline C+ fluid outlet control valve C 1+ fluid outlet pipeline C 2+ process pump C 3+ fluid outlet pipeline C 4, the fluid outlet pipeline C the other end is installed on fluid treating plant cavity W treatment chamber.
5. fluid intake part=recoil pipeline D recoils 1+ recoil control valve D 2+ recoil pipeline D 3, recoil pipeline D is installed on fluid outlet pipeline C 3The other end is at fluid outlet pipeline C 4Last installation recoil pipeline D 1The other end.(recoil pipeline D 1The other end also can be installed on the pipeline of the recycle system; Recoil pipeline D 3The other end also can be installed in fluid treating plant on the treatment chamber.)
Whole equipment installs.
The utility model has an innovation greatly in single pump band backwashed fluid treatment facility:
1. the utility model is handled fully as a kind of side stream of circulating water system in single pump fluid treating plant, and this fluid treating plant is the negative pressure operation in the fluid treating plant cavity when operation; Be malleation in the fluid treating plant cavity when the equipment back flushing, the recoil fluid is processed intrasystem fluid, and recoil fluidic pressure size is determined by processed system fluid self pressure.
Description of drawings
The utility model is described in further detail below in conjunction with drawings and Examples.
Fig. 1 is that a kind of single pump negative pressure operation of structure iron of the present utility model is from pressing the recoil fluid treating plant
Fig. 2 is the structure iron that a kind of single pump negative pressure operation of the utility model is used as a kind of by-pass flow formula fluid treating plant when pressing the recoil fluid treating plant to be installed in parallel in industrial circulating water
Embodiment:
Among Fig. 1, fluid intake pipeline A, fluid intake control valve A 1, fluid intake pipeline A 2, fluid outlet pipeline C, fluid outlet control valve C 1, fluid outlet pipeline C 2, process pump C 3, fluid outlet pipeline C 4, blow-off line B, blowdown control valve B 1, blow-off line B 2, fluid treating plant cavity W, recoil pipeline D 1, recoil control valve D 2, recoil pipeline D 3, vent valve X, recoil pipeline D 1, recoil control valve D 2, recoil pipeline D 3
As Fig. 1, make a single pump negative pressure operation from pressing the recoil fluid treating plant to form by five major parts:
1. the fluid treating plant cavity W=fluid treating plant cavity W pending chamber of treatment chamber+fluid treating plant cavity W+vent valve X.
2. fluid moves inlet part=fluid intake pipeline A+ fluid intake control valve A 1+ fluid intake pipeline A 2, a wherein end of fluid intake pipeline A is installed on the pending chamber of fluid treating plant cavity W.
3. blowdown exports part=blow-off line B+ blowdown control valve B 1+ blow-off line B 2, the blow-off line B the other end is installed on the pending chamber of fluid treating plant cavity W.
4. the fluid operation exports part=fluid outlet pipeline C+ fluid outlet control valve C 1+ fluid outlet pipeline C 2+ process pump C 3+ fluid outlet pipeline C 4, the fluid outlet pipeline C the other end is installed on fluid treating plant cavity W treatment chamber.
5. fluid intake part=recoil pipeline D recoils 1+ recoil control valve D 2+ recoil pipeline D 3, recoil pipeline D is installed on fluid outlet pipeline C 3The other end is at fluid outlet pipeline C 4Last installation recoil pipeline D 1The other end.(recoil pipeline D 1The other end also can be installed on the pipeline of the recycle system; Recoil pipeline D 3The other end also can be installed in fluid treating plant on the treatment chamber.)
Whole equipment installs.
The utility model is to implement operation like this in the industrial cycle water system:
1, operation and the control of the utility model in the industrial cycle water system:
As shown in Figure 2, with pipeline C 4, pipeline A 2Be connected on respectively on the circulating line H, in the time will carrying out purifying treatment to the water in the recycle system, shut-off valve B 1, valve D 2, open valve A 1, valve C 1, process pump C 3Water inflow pipe A among the circulating water system pipeline H 2, via valve A 1The pending chamber of → pipeline A → fluid treating plant cavity W → fluid treating plant cavity W is treatment chamber → pipeline C → valve C 1→ pipeline C 2→ process pump C 3→ pipeline C 4→ return circulating water system pipeline H.
At this moment treated water imports pipeline H, materials such as glutinous mud, impurity, suspended substance, microorganism, mushroom constantly are trapped the pending chamber of fluid treating plant W cavity in the circulating line, make it be difficult for being deposited on the heat exchange system surface, guarantee the heat exchanger effectiveness of circulating water system, thereby reach object of energy saving.
2, the sewage backwash process of the utility model in the industrial cycle water system:
As shown in Figure 2, after the utility model equipment moves for some time, impurity increases in the pending chamber of fluid treating plant cavity W, the pending chamber of fluid treating plant cavity W constantly rises with the pressure reduction of treatment chamber, the equipment clean decrease in efficiency, need back flushing,, at this moment close process pump C with the treatment effect of restorer 3, valve A 1, valve C 1, open valve D again 2, valve B 1, at this moment system's inner fluid because of self pressure through pipeline C 4→ pipeline D 1→ valve D 2→ pipeline D 3→ enter the fluid treating plant cavity W pending chamber of treatment chamber → fluid treating plant W → pipeline B → wash water valve B 1→ pipeline B 2Shut-off valve B after recoil blowdown for some time 1, valve D 2, whole backwash process is finished, and the impurity in fluid treating plant cavity W, glutinous mud etc. is exhausted from system, and the fluid treating plant purification efficiency is restored.

Claims (2)

1. a single pump negative pressure operation is from pressing the recoil fluid treating plant, consist predominantly of: the fluid intake control valve, the fluid outlet control valve, process pump, fluid treating plant cavity, recoil control valve, wash water valve, blow-off line, vent valve is characterized in that: process pump with after the fluid outlet control valve is connected again with the series-parallel connection body of recoil control valve generation in parallel together be installed in fluid treating plant treatment chamber to the pipeline of the recycle system.
2. the recoil fluid treating plant is pressed in 1 described a kind of single pump negative pressure operation certainly according to claim, it is characterized in that: the fluid intake control valve is installed on the fluid intake pipeline of the pending chamber of fluid treating plant.
CN2010205095306U 2010-08-30 2010-08-30 Single pump negative pressure operation and self pressure back-flushing fluid treatment device Expired - Fee Related CN202080908U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010205095306U CN202080908U (en) 2010-08-30 2010-08-30 Single pump negative pressure operation and self pressure back-flushing fluid treatment device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2010205095306U CN202080908U (en) 2010-08-30 2010-08-30 Single pump negative pressure operation and self pressure back-flushing fluid treatment device

Publications (1)

Publication Number Publication Date
CN202080908U true CN202080908U (en) 2011-12-21

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN2010205095306U Expired - Fee Related CN202080908U (en) 2010-08-30 2010-08-30 Single pump negative pressure operation and self pressure back-flushing fluid treatment device

Country Status (1)

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CN (1) CN202080908U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111823359A (en) * 2020-08-13 2020-10-27 广东金马领科智能科技有限公司 High pressure grouting system and high pressure grouting process

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111823359A (en) * 2020-08-13 2020-10-27 广东金马领科智能科技有限公司 High pressure grouting system and high pressure grouting process

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Date Code Title Description
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: 20111221

Termination date: 20140830

EXPY Termination of patent right or utility model