CN102276029A - Inverted cavity of by-pass fluid treatment device - Google Patents
Inverted cavity of by-pass fluid treatment device Download PDFInfo
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- CN102276029A CN102276029A CN2010101973096A CN201010197309A CN102276029A CN 102276029 A CN102276029 A CN 102276029A CN 2010101973096 A CN2010101973096 A CN 2010101973096A CN 201010197309 A CN201010197309 A CN 201010197309A CN 102276029 A CN102276029 A CN 102276029A
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- fluid
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Abstract
The invention relates to an inverted cavity of a by-pass fluid treatment device. The inverted cavity comprises: a fluid inlet pipe, a fluid outlet pipe, a fluid treatment device chamber requiring treatment, a fluid treatment device treated chamber, a fluid treatment material, a separation plate and an air release valve. The inverted cavity is characterized in that: the fluid treatment device chamber requiring treatment is arranged below the fluid treatment device treated chamber. According to the present invention, the fluid treatment device chamber requiring treatment is arranged below the fluid treatment device treated chamber, such that natural characteristics of the fluid are utilized sufficiently, in the chamber requiring treatment, with the passage of working time, contents of various slime, bacteria and algae are ceaselessly increased, the formation probability of macromolecule clusters due to collision generating between the molecules is increased, various macromolecule clusters naturally precipitate due to gravitational effect. With the present invention, the natural characteristic of the gravity is adopted, a natural precipitation chamber is provided for the macromolecule clusters, such that various slime, bacteria, algae and other impurities are prevented from sedimentation on various fluid treatment materials so as to improve purification effect of the fluid treatment device.
Description
Technical field
The present invention relates to a kind of fluid treating plant cavity, refer in particular to a kind of side stream treatment facility and be inverted cavity, can be widely used in industrial circulating water, on the fluid treating plant in fields such as civilian recirculated water, pharmacy, chemical industry, food-processing, environmental engineering, metallurgy, central air-conditioning, electric power.
Background technology
In the industrial circulating water system of modernization, all fluid treating plants all are conveniently to consider from materials for fluid management is installed, thereby do not utilize the effect of various characteristics of fluidic and gravity fully, artificial method is too many, and seldom design fluid treating plant from natural science applied angle, adopt the cavity of inversion type, though install than prior art complexity from material, but angle and purification effects from fluid handling, prior art is just less than the cavity of inversion type, from the modern materials for fluid management of development, there is not a technical difficult problem in the installation of being inverted material for water treatment in the cavity yet especially.
Summary of the invention
The purpose of invention
The purpose of this invention is to provide a kind of side stream treatment facility and be inverted cavity, this cavity mainly is because of adopting the installation method of inversion type, with the pending chamber of fluid treating plant cavity partly design and installation below fluid treating plant cavity treatment chamber, thereby at fluid treating plant in when operation, along with the various glutinous mud of the prolongation of time, bacterium, the degree of algae molecular grouping rises, increase because of various foreign matter contents in the unit volume, assemble bigger molecular grouping and natural sedimentation, the materials for fluid management of inversion type cavity all is installed in the top of pending chamber, therefore, below pending chamber, form one and given the sedimentary natural sediment chamber of various molecular groupings, made full use of the effect of gravity, after having avoided prior art that materials for fluid management is installed, the precipitation of various molecular groupings drops on the materials for fluid management, the phenomenon that causes fluid purification effect and efficient all to descend has fast reduced the number of times of equipment blowdown simultaneously, has saved water resources.
Technical scheme
Structure iron 1 is made a by-pass flow double pump recoil negative pressure inversion type water treating equipment cavity according to the present invention, produce structure iron 2, as shown in Figure 2: in fluid treating plant W cavity, dividing plate G is arranged, it below dividing plate G pending chamber, the top is treatment chamber, fluid intake pipeline A is installed on the pending chamber of fluid treating plant cavity W, and fluid outlet pipeline B is installed in fluid treating plant cavity W on the treatment chamber; Above in the pending chamber of fluid treating plant cavity W materials for fluid management S is installed; In the pending chamber upper shed of fluid treating plant cavity W recoil outlet conduit D is installed, recoil inlet duct C is installed at fluid treating plant cavity W treatment chamber upper shed.The assembling of a by-pass flow double pump recoil negative pressure inversion type water treating equipment cavity finishes.
(in structure iron 2, fluid intake pipeline A and recoil outlet conduit D are installed on the pending chamber of fluid treating plant cavity W, according to the fluidic characteristics, fluid intake pipeline A and recoil outlet conduit D can own an opening together on the pending chamber of fluid treating plant cavity W; In like manner fluid outlet pipeline B and recoil inlet duct C are also on fluid treating plant cavity W treatment chamber, pipeline B and pipeline C also can own an opening together on fluid treating plant cavity W treatment chamber, the variation structure iron and the structure iron 2 of its generation are in full accord on principle of work, below describe and only press structure iron 2, other changes no longer describes).
Structure iron 2 is assembled into a by-pass flow formula double pump recoil negative pressure inversion type fluid treating plant produces structure iron 3, its structure is made of five major parts, as shown in Figure 3:
1, on the pending chamber of fluid treating plant cavity W, install:
Fluid operation inlet part=fluid intake pipeline A+ fluid intake control valve A
1+ fluid intake pipeline A
2+ process pump A
3+ fluid intake pipeline A
4
2, install on the treatment chamber at fluid treating plant cavity W:
Fluid operation outlet part=fluid outlet pipeline B+ fluid outlet control valve B
1+ fluid outlet pipeline B
2
3, install on the treatment chamber at fluid treating plant cavity W:
Recoil fluid intake part=recoil inlet duct C+ recoil inlet control valve C
1+ recoil inlet duct C
2
4, on the pending chamber of fluid treating plant cavity W, install:
Recoil fluid outlet part=recoil outlet conduit D+ recoil discharge control valve D
1+ recoil outlet conduit D
2+ recoil pump D
3+ blow-off line D
4
5, on fluid treating plant cavity W body, install:
Fluid treating plant cavity=pending the chamber of fluid treating plant W (and be installed in top pending chamber in materials for fluid management S)+fluid treating plant is treatment chamber+dividing plate+vent valve X (treatment chamber should be installed in pending chamber top when mounted).
A by-pass flow formula double pump is inverted the assembling of cavity recoil negative pressure water treating equipment and is finished, shown in Figure 3 as structure, now structure iron 3 is parallel on the industrial cycle water-system pipeline H, produce structure iron 4, a kind of side stream treatment facility of the present invention inversion type cavity can be in food-processing, widespread use on the fluid purifying apparatus such as environmental engineering, metallurgy, chemical industry, central air-conditioning, industrial circulating water, civilian recirculated water, electric power, light industry, and manufacture various single pumps, double pump; Operation under positive pressure, negative pressure operation; The fluid treating plant of various ways such as by-pass flow, direct current.
The present invention has an innovation greatly on the fluid treating plant cavity:
1, the pending chamber of fluid treating plant is below fluid treating plant treatment chamber, thereby various impurity are trapped in the pending chamber of fluid treating plant cavity by materials for fluid management, passing along with the working hour, the opacity of various impurity in the pending chamber of fluid treating plant cavity increases, concentration rises, intermolecular mutual collision frequency increases, forming more, the macromolecular mass probability increases, under the effect of gravity, bigger, some heavier molecular groupings precipitate downwards, because of materials for fluid management at this moment in pending chamber above, so form the sediment chamber of a nature below in pending chamber, it is littler with the top that the pending chamber of fluid treating plant is placed on treatment chamber than prior art that these impurity deposit influence that the back convection cell handles material naturally, from fluid handling purification effects angle, though materials for fluid management is installed complexity a bit, but the present invention pays attention to the fluidic natural characteristic more, effectively raise the fluidic decontamination effect improving, prolonged the working hour of materials for fluid management, and reduced the number of times of blowdown, saved water resources.
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 that Fig. 1 makes a kind of structure iron that by-pass flow formula double pump recoil negative pressure water treating equipment are inverted cavity according to the present invention.
Fig. 3 makes the general assembly structure iron that a by-pass flow formula double pump recoil negative pressure is inverted the cavity water treating equipment according to Fig. 2.
Fig. 4 is assembled into by-pass flow formula double pump recoil negative pressure according to Fig. 3 to be inverted the cavity water treating equipment and to be parallel in the industrial cycle water system mounting structure figure as the side stream treatment facility.
Fig. 5 is that Fig. 1 makes behind Fig. 3 a double pump recoil negative pressure inversion type fluid treating plant and is connected on structure iron when handling gas (air) in the environmental engineering according to the present invention.
Embodiment:
Among Fig. 1, fluid intake pipeline A, fluid outlet pipeline B, fluid treating plant cavity W, materials for fluid management S, dividing plate G, vent valve X.
In Fig. 1, fluid intake pipeline A connects the pending chamber of fluid treating plant cavity W, and fluid handling pipeline B connects fluid treating plant cavity W treatment chamber; At the pending chamber of fluid treating plant cavity W and dividing plate G has been arranged between the treatment chamber; Materials for fluid management S is installed above in pending chamber; At treatment chamber highest point vent valve X is installed, a kind of side stream treatment facility inversion type cavity assembling finishes, and produces structure iron 1.
Recoil fluid outlet pipeline D is installed in the pending chamber upper shed of fluid treating plant cavity W in structure iron 1 of the present invention; At fluid treating plant cavity W treatment chamber upper shed recoil inlet duct C is installed, produces structure iron 2.
Structure iron 2 is assembled into double pump inversion type cavity recoil negative pressure water treating equipment, produces structure iron 3, this equipment is by five most of compositions, as shown in Figure 3:
1, on the pending chamber of fluid treating plant cavity W, install:
Fluid operation inlet part=fluid intake pipeline A+ fluid intake control valve A
1+ fluid intake pipeline A
2+ process pump A
3+ fluid intake pipeline A
4
2, install on the treatment chamber at fluid treating plant cavity W:
Fluid operation outlet part=fluid outlet pipeline B+ fluid outlet control valve B
1+ fluid outlet pipeline B
2
3, install on the treatment chamber at fluid treating plant cavity W:
Recoil fluid outlet part=recoil inlet duct C+ recoil inlet control valve C
1+ recoil inlet duct C
2
4, on the pending chamber of fluid treating plant cavity W, install:
Recoil fluid outlet part=recoil outlet conduit D+ recoil discharge control valve D
1+ recoil outlet conduit D
2+ recoil pump D
3+ blow-off line D
4
5, on fluid treating plant cavity W body, assemble:
The pending chamber of fluid treating plant cavity W=fluid treating plant W (and be installed in top pending chamber in materials for fluid management S)+fluid treating plant is treatment chamber+dividing plate G+ vent valve X (treatment chamber should be installed in pending chamber top when mounted).
A by-pass flow formula double pump is inverted the assembling of cavity recoil negative pressure water treating equipment and is finished, and is shown in Figure 3 as structure, now structure iron 3 is parallel in the industrial cycle water system, with fluid intake pipeline A
4With fluid outlet pipeline B
2Be connected on respectively on the recycle system pipeline H, produce structure iron 4.
1 one kinds of side stream treatment facilities of structure iron of the present invention inversion type cavity is made into enforcement and the operation of a side stream treatment facility (a by-pass flow formula double pump recoil negative pressure is inverted the cavity water treating equipment) in the industrial cycle water system:
1, as shown in Figure 4, when will be, close recoil pump D earlier to the water treatment among the circulating line H
3, recoil inlet control valve C
1, recoil discharge control valve D
1, open fluid intake control valve A
1, fluid outlet control valve B restarts process pump A
3, the water inflow pipe A among the recycle system pipeline H at this moment
4→ process pump A
3→ pipeline A
2→ valve A
1The pending chamber of → pipeline A → fluid treating plant cavity W → materials for fluid management S → fluid treating plant cavity W is treatment chamber → pipeline B → valve B
1→ pipeline B
2→ return circulating line H, through constantly circulation, water among the circulating line H constantly is cleaned, its various impurity constantly by materials for fluid management S retaining cut below pending chamber in, the fluid opacity, impurity, rise along with the prolongation of working hour, the molecular impact increased frequency, and form under the effect of gravity and slowly precipitation of macromolecular mass, if prior art, throw out then drops on the materials for fluid management S, so after improving, the negative impact that its natural sedimentation thing convection cell is handled the decontamination effect improving of material S diminishes, decontamination effect improving more is better than prior art, and prolongs backwashing time, conserve water resource.
2, structure iron 1 of the present invention is inverted cavity as a kind of side stream treatment facility and is made the implementation process that is parallel to back flushing in the industrial cycle water system behind the water treating equipment:
As Fig. 4, when pending chamber with treatment chamber pressure reduction is increasing, the opacity of water in pending chamber, the concentration of various impurity rises, the flow by materials for fluid management S reduces, equipment just need carry out back flushing, at this moment first pump A out of service
3, shut-off valve A
1, valve B
1, open valve C then
1, valve D
1, start recoil pump D
3, the fluid that at this moment recoils enters pipeline C
2→ valve C
1→ pipeline C → fluid treating plant cavity W is the treatment chamber → pending chamber of materials for fluid management S → fluid treating plant cavity W → pipeline D → valve D
1→ pipeline D
2→ recoil pump D
3→ blow-off line D
4, when from blow-off line D
4In clear water appears and after, recoil pump D
3Quit work, whole fluid treating plant enters next circulation.
Enforcement and the operation of the present invention in environmental engineering:
Structure iron 1 of the present invention becomes single flow fluid treating plant inversion cavity in the environmental engineering system in this embodiment, a fluid treating plant (as structure iron 3) that is assembled into by structure iron 1 of the present invention, change vent valve into below that water discharge valve is installed in fluid treating plant chamber W, with fluid intake pipeline A
4With room air supply duct T
1Join, with fluid outlet pipeline B
2With room return air duct T
2Join, it is constant that all the other structures are pressed structure iron 3, produces structure iron 5, and inversion cavity work effect and structure iron of the present invention 1 in structure iron 5 are in full accord.
The process of its operation is as follows:
1, as shown in Figure 5, in the time will purifying, close recoil pump D earlier to the air in the room M
3, valve D
1, valve C
1Open valve A again
1, valve B
1, start process pump A
3At this moment air enters pipeline T from room M
1→ pipeline A
4→ process pump A
3→ pipeline A
2→ valve A
1The pending chamber of → pipeline A → fluid treating plant cavity W → materials for fluid management S → fluid treating plant cavity W is treatment chamber → pipeline B → valve B
1→ pipeline B
2→ return air duct T
2Through constantly circulation, air constantly is cleaned in the room M, various impurity, dust is trapped within the pending chamber of fluid treating plant cavity W, along with the working hour passes, dust is more and more in pending chamber, and air flow quantity descends, and various impurity and dust form more macromolecular mass because of the rising of concentration, and precipitate downwards because of action of gravity, but because of the present invention is installed in pending chamber top with materials for fluid management, diminish, pending chamber is installed in treatment chamber top so the natural sedimentation process is better than prior art so various throw out convection cell is handled the influence of material, prolong the pitch time of back flushing, improved purification effects.
2, the present invention makes the implementation process that is connected on back flushing when handling gas (air) in the environmental engineering system behind the fluid treating plant:
As Fig. 5, when pending chamber with treatment chamber pressure reduction is increasing, various impurity, dust content rise in pending chamber, after flow reduced, equipment needed back flushing, pump A at this moment out of service
3, shut-off valve A
1, valve B
1Open valve C then
1, valve D
1, restart recoil pump D
3, the fluid that at this moment recoils enters pipeline C
2→ valve C
1→ pipeline C → fluid treating plant cavity W is the treatment chamber → pending chamber of materials for fluid management S → fluid treating plant cavity W → pipeline D → valve D
1→ pipeline D
2→ recoil pump D
3→ blow-off line D
4, when from blow-off line D
4Gas opacity of coming out and concentration diminish the back to certain value, and recoil pump quits work, and whole fluid treating plant enters next circulation.
Claims (4)
1. a side stream treatment facility is inverted cavity, include: the fluid intake pipeline, the fluid outlet pipeline, the pending chamber of fluid treating plant cavity, the fluid treating plant cavity is treatment chamber, dividing plate, materials for fluid management, vent valve is characterized in that: the fluid treating plant cavity treatment chamber above the pending chamber of fluid treating plant cavity.
2. a kind of side stream treatment facility according to claim 1 is inverted cavity, and it is characterized in that: vent valve is installed in the extreme higher position of treatment chamber.
3. a kind of side stream treatment facility according to claim 1 is inverted cavity, it is characterized in that: this cavity can be used on the fluid of handling other form on other fluid treating plant.
4. a kind of side stream treatment facility according to claim 1 is inverted cavity, it is characterized in that: when the fluid that this inversion cavity is handled was gas, its vent valve changed water discharge valve into and is installed in the bottom of pending chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010101973096A CN102276029A (en) | 2010-06-11 | 2010-06-11 | Inverted cavity of by-pass fluid treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010101973096A CN102276029A (en) | 2010-06-11 | 2010-06-11 | Inverted cavity of by-pass fluid treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102276029A true CN102276029A (en) | 2011-12-14 |
Family
ID=45101831
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010101973096A Pending CN102276029A (en) | 2010-06-11 | 2010-06-11 | Inverted cavity of by-pass fluid treatment device |
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Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2131593Y (en) * | 1992-06-20 | 1993-05-05 | 湖南岳阳市巴陵现代技术研究所 | Vortex sedimentation floating filter |
| CN2234809Y (en) * | 1995-11-01 | 1996-09-11 | 沈祖良 | Siphon sewage filter |
| CN1470310A (en) * | 2003-06-18 | 2004-01-28 | 宁波大学 | A granular bed filter dust removal device and method thereof |
| CN2754799Y (en) * | 2004-07-08 | 2006-02-01 | 许进男 | Laser cutting special dust collection device |
| CN1896017A (en) * | 2006-06-20 | 2007-01-17 | 刘端华 | Efficient integrated treater for living sewage |
| CN101152609A (en) * | 2006-09-25 | 2008-04-02 | 葛敬 | Float bed filter |
| CN201299995Y (en) * | 2008-10-28 | 2009-09-02 | 石家庄常山恒新纺织有限公司 | Back washing water refiltration device for refrigerated water filter |
-
2010
- 2010-06-11 CN CN2010101973096A patent/CN102276029A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2131593Y (en) * | 1992-06-20 | 1993-05-05 | 湖南岳阳市巴陵现代技术研究所 | Vortex sedimentation floating filter |
| CN2234809Y (en) * | 1995-11-01 | 1996-09-11 | 沈祖良 | Siphon sewage filter |
| CN1470310A (en) * | 2003-06-18 | 2004-01-28 | 宁波大学 | A granular bed filter dust removal device and method thereof |
| CN2754799Y (en) * | 2004-07-08 | 2006-02-01 | 许进男 | Laser cutting special dust collection device |
| CN1896017A (en) * | 2006-06-20 | 2007-01-17 | 刘端华 | Efficient integrated treater for living sewage |
| CN101152609A (en) * | 2006-09-25 | 2008-04-02 | 葛敬 | Float bed filter |
| CN201299995Y (en) * | 2008-10-28 | 2009-09-02 | 石家庄常山恒新纺织有限公司 | Back washing water refiltration device for refrigerated water filter |
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Application publication date: 20111214 |