CN104261580A - Pressure decontaminating water purifying device - Google Patents
Pressure decontaminating water purifying device Download PDFInfo
- Publication number
- CN104261580A CN104261580A CN201410491917.6A CN201410491917A CN104261580A CN 104261580 A CN104261580 A CN 104261580A CN 201410491917 A CN201410491917 A CN 201410491917A CN 104261580 A CN104261580 A CN 104261580A
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- Prior art keywords
- cylinder
- pressure
- quartz sand
- water inlet
- gac
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Classifications
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
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- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Water Treatment By Sorption (AREA)
Abstract
The invention discloses a pressure decontaminating water purifying device which sequentially comprises an active carbon cylinder filled with active carbon, a quartz sand cylinder filled with quartz sand, a water inlet cylinder and a pressure cylinder from top to bottom, wherein the active carbon cylinder, the quartz sand cylinder and the water inlet cylinder are all cylindrical and the pressure cylinder is shaped like a cone; the water inlet cylinder is provided with a raw water inlet, the active carbon cylinder is provided with a purified water outlet and the pressure cylinder is provided with a drain outlet; separation nets are respectively arranged between the active carbon cylinder and the quartz sand cylinder as well as between the quartz sand cylinder and the water inlet cylinder. By adopting a pressure backwashing separating manner, silt, sludge, dirt, particles, colloids and organic matter in water can be efficiently removed by virtue of the principle of pressure separation in a physical mode, emission of chemical medical liquor, acid and alkali can be avoided and an acid-base neutralization treatment process is omitted; in addition, the pressure decontaminating water purifying device is low in using cost and free from secondary pollution, and moreover, pollutants are immediately discharged, the operating service life of machinery equipment is ensured, and the energy sources are saved. The pressure decontaminating water purifying device has the advantages of high safety, high efficiency, high stability, good economical performance, environment-friendliness and the like.
Description
Technical field
The present invention relates to technical field of water purification, particularly a kind of pressure sewage purifier.
Background technology
At present, pre-process of purifying waste water generally has input pharmaceutical chemicals, electrolysis and employing quartz sand and gac cylinder to filter three kinds of methods.Wherein, throw in pharmaceutical chemicals and remove the method for impurities in water and refer to drop into pharmaceutical chemicals in preposition purification water pool, pharmaceutical chemicals plays precipitating action with particulate matter, salt and colloid etc. in water, thus separable with the partial impurities in discharge water.But this method dispensing is expensive, and increases pharmaceutical chemicals in water, produces toxic action, causes the secondary pollution of water quality.Electrolysis process is removed the method for impurities in water and is referred to put into negative and positive the two poles of the earth electrolyzer in preposition purification water pool, and decompose impurities in water with ion-exchange method, electrolysis goes out impurities in water.But the loss of this method electrolyzer is large, work-ing life is short, need change in time; And electrolyzer material used is noble metal, use cost is very expensive.Filter impurities in water with quartz sand and gac cylinder to refer to adopt and filter and suction type, filter with quartz sand and gac cylinder in preposition water treatment, can macrobead thing, scale, floating matter and mud in filtered water.But this method can not filter the water quality that mud is many or impurity is many, otherwise results in blockage.And can not filtered water small particles thing.In this external filtration procedure, impurities in water and pollutent are adsorbed in quartz sand cylinder and activated carbon cylinder and cannot discharge, and frequently need change filter material, and replacing filter material cost is high, replacing complex procedures, produces secondary pollution simultaneously.
Summary of the invention
Main purpose of the present invention is to provide the pressure sewage purifier of a kind of safe, efficient, stable, economy, environmental protection.
For achieving the above object, the present invention proposes a kind of pressure sewage purifier, described pressure sewage purifier comprises the gac cylinder being filled with gac, the quartz sand cylinder being filled with quartz sand, water inlet cylinder and pressure cylinder from top to bottom successively, wherein, described gac cylinder, quartz sand cylinder and water inlet cylinder are all arranged in tubular, and described pressure cylinder is that taper is arranged; Upper end closed, the lower end of described gac cylinder are open; Two ends all openings of described quartz sand cylinder and water inlet cylinder; The bottom surface opened of described pressure cylinder; The lower end of described gac cylinder is connected with the upper end of quartz sand cylinder, and the lower end of quartz sand cylinder is connected with the upper end of water inlet cylinder, and the water inlet lower end of cylinder is connected with the bottom surface of pressure cylinder; The sidewall of described water inlet cylinder offers raw water inlet, and the top of described gac cylinder offers water purification water outlet, and the cone tip part of described pressure cylinder offers sewage draining exit; Between described gac cylinder and quartz sand cylinder, and be equipped with separation net between quartz sand cylinder and water inlet cylinder.
Preferably, described gac cylinder, quartz sand cylinder, water inlet cylinder and pressure cylinder are coaxial, and the diameter of described gac cylinder, quartz sand cylinder and water inlet cylinder is 800mm, and the maximum diameter of described pressure cylinder is 800mm, and minimum diameter is 35mm.
Preferably, the height of described gac cylinder is 600mm; The height of described quartz sand cylinder is 500mm; The height of described water inlet cylinder is 250mm; The height of described pressure cylinder is 300mm.
Preferably, the diameter of described raw water inlet is 50mm; The diameter of described water purification water outlet is 50mm, and the diameter of described sewage draining exit is 25mm.
Preferably, the thickness of described separation net is 1.5mm; The mesh diameter of described separation net is not more than 5mm; It is the stiffening web of 10mm that separation net described in each is provided with at least 5 diameters.
Preferably, described gac cylinder upper end is provided with tensimeter.
Preferably, the shell activated carbon granule of the gac of filling in described gac cylinder to be diameter be 5mm.
Preferably, the quality of the gac of filling in described gac cylinder is 100kg.
Preferably, the quartz sand particle of the quartz sand of filling in described quartz sand cylinder to be diameter be 5mm.
Preferably, the quality of the quartz sand of filling in described quartz sand cylinder is 400kg.
Technical solution of the present invention adopts " pressure bounce-back separation " mode; utilize the principle that physics mode, pressure are separated; silt, mud, spot, particulate matter, colloid and organism during energy high-efficient cleaning dewaters, without chemical liquid, acid, alkali discharge, without soda acid neutralizing treatment process; use cost is low; do not produce secondary pollution, and timely out contaminants, guarantee machinery equipment operation life; save energy, has the advantages such as safety, efficient, stable, economy, environmental protection.
Accompanying drawing explanation
Fig. 1 is the structural representation of pressure sewage purifier of the present invention.
The realization of the object of the invention, functional characteristics and advantage will in conjunction with the embodiments, are described further with reference to accompanying drawing.
Embodiment
Be described further with regard to technical scheme of the present invention below in conjunction with drawings and the specific embodiments.Should be appreciated that specific embodiment described herein only in order to explain the present invention, be not intended to limit the present invention.
The present invention proposes a kind of pressure sewage purifier, for purifying waste water.
With reference to the structural representation that Fig. 1, Fig. 1 are pressure sewage purifier of the present invention.
In embodiments of the present invention, this pressure sewage purifier comprises gac cylinder 10, quartz sand cylinder 20, water inlet cylinder 30 and pressure cylinder 40 from top to bottom successively, wherein, in this gac cylinder 10, be filled with activated carbon granule, in this quartz sand cylinder 20, be filled with quartz sand particle.This gac cylinder 10, quartz sand cylinder 20 and water inlet cylinder 30 are all arranged in tubular, and pressure cylinder 40 is arranged in taper.Upper end closed, the lower end of this gac cylinder 10 are open; Two ends all openings of quartz sand cylinder 20 and water inlet cylinder 30; The bottom surface opened of pressure cylinder 10.The lower end of this gac cylinder 10 is connected with the upper end of quartz sand cylinder 20, and the lower end of quartz sand cylinder 20 is connected with the upper end of water inlet cylinder 30, and the lower end of water inlet cylinder 30 is connected with the bottom surface of pressure cylinder 40.The sidewall of this water inlet cylinder 30 offers raw water inlet 31, and the top of gac cylinder 10 offers water purification water outlet 11, and the cone tip part of pressure cylinder 40 offers sewage draining exit 41.Between this gac cylinder 10 and quartz sand cylinder 20, and being equipped with separation net 50 between quartz sand cylinder 20 and water inlet cylinder 30, this separation net 50 is for isolating activated carbon granule and quartz sand particle and preventing isolation activated carbon granule and quartz sand particle from entering into water cylinder 30 and pressure cylinder 40.
When clean water treatment, former water enters into water cylinder 30 by raw water inlet 31, under the effect of hydraulic pressure, former water upwards flows, first larger in the former water of quartz sand cylinder 20 coarse filtration particulate matter, and then in the former water of gac cylinder 10 filtering less particulate matter, adsorb the impurity such as the chlorine residue in former water, heavy metal and pesticide remnant, finally obtain water purification and sent by water purification water outlet 11.And be separated by recoil under the dual function of impurity liquid, solids pressure in water pressure with cylinder such as silt, mud, spot, particulate matter, colloid, organism in former water, finally discharged by sewage draining exit 41.
Technical solution of the present invention adopts " pressure bounce-back separation " mode; utilize the principle that physics mode, pressure are separated; silt, mud, spot, particulate matter, colloid and organism during energy high-efficient cleaning dewaters, without chemical liquid, acid, alkali discharge, without soda acid neutralizing treatment process; use cost is low; do not produce secondary pollution, and timely out contaminants, guarantee machinery equipment operation life; save energy, has the advantages such as safety, efficient, stable, economy, environmental protection.
In the present invention in a certain or whole embodiment, in order to ensure the cleaning water of this pressure sewage purifier, reduce flow resistance, this gac cylinder 10, quartz sand cylinder 20, water inlet cylinder 30 and pressure cylinder 40 are coaxial, and the diameter of gac cylinder 10, quartz sand cylinder 20 and water inlet cylinder 30 is preferably 800mm, the maximum diameter of pressure cylinder is 800mm, and minimum diameter is preferably 35mm.
In the present invention in a certain or whole embodiment, in order to ensure the cleaning water of sewage purifier further, and the pressure to recoil, the height of this gac cylinder is preferably 600mm; The height of quartz sand cylinder is preferably 500mm; The height of water inlet cylinder is preferably 250mm; The height of pressure cylinder is preferably 300mm.
In the present invention in a certain or whole embodiment, in order to ensure that sewage purifier inputs former water and exports the flow of water purification, the diameter of this raw water inlet is preferably 50mm; The diameter of water purification water outlet is preferably 50mm, and the diameter of sewage draining exit is preferably 25mm.
In the present invention in a certain or whole embodiment, the thickness of this separation net 50 is preferably 1.5mm; The mesh diameter of separation net 50 is not more than 5mm.In addition, in order to make separation net 50 have enough supporting capacity, each separation net 50 is provided with the stiffening web (not shown) that at least 5 diameters are preferably 10mm.
In the present invention in a certain or whole embodiment, be also provided with tensimeter 60 in the upper end of this gac cylinder 10, user can according to the size of the hydraulic pressure of the pressure adjusting raw water inlet 31 in gac cylinder 10, with the demand of satisfied different occasion.
In the present invention in a certain or whole embodiment, in order to the pressure of the effect and recoil that ensure water purification, the gac of filling in this gac cylinder 10 is preferably the shell activated carbon granule that diameter is 5mm, and the quality optimization of the shell activated carbon granule of filling is 100kg.The quartz sand of filling in this quartz sand cylinder 20 is the quartz sand particle that diameter is preferably 5mm, and the quality optimization of the quartz sand particle of filling is 400kg.
Pressure sewage purifier of the present invention all reach good purifying water effect through repeatedly surveying, just 3 actual measurements wherein illustrate below.
1, Shenzhen.From the stormwater tank after heavy rain, water pump (pump motor is 20 lifts) is installed, with the original water inlet 31 of water pipe Bonding pressure sewage purifier, close sewage draining exit 41, water pump energising is drawn water, muddy Chi Shui is by after the purification of pressure sewage purifier, and from the pure water inlet 11 limpid inclusion-free of water out, then switch off the pump power supply one point of kind, open sewage draining exit 41, excrete silt, mud, spot, particulate matter and suspended substance.Test flow of purifying waste water, the maximum net water yield is 10 tons/hour.
2, Zhengzhou.From the Yellow River, Huayuankou section, water pump (pump motor is 30 lifts) is installed and takes out Huanghe water, with the original water inlet 31 of water pipe Bonding pressure sewage purifier, close sewage draining exit 41, water pump energising is drawn water, and muddy Huanghe water, by after the purification of pressure sewage purifier, out flows out from pure water inlet 11, the limpid inclusion-free of water, then switch off the pump power supply one point of kind, opens sewage draining exit 41, excrete silt, mud, spot, particulate matter and suspended substance.Test flow of purifying waste water, the maximum net water yield is 15 tons/hour.
3, Quzhou, Zhejiang.Water pump (pump motor is 30 lifts) is installed from feeder pig manure pond, Quzhou and takes out ight soil water, with the original water inlet 31 of water pipe Bonding pressure sewage purifier, close sewage draining exit 41, water pump energising is drawn water, and the ight soil water of black muddiness, by after the purification of pressure sewage purifier, out flows out from pure water inlet 11, the limpid inclusion-free of water, then switch off the pump power supply one point of kind, opens sewage draining exit 41, excrete ight soil residue, swill, silt, mud, particulate matter and suspended substance.Test flow of purifying waste water, the maximum net water yield is 10 tons/hour.
From the purify waste water censorship of above three places after the process of excess pressure sewage purifier, Shenzhen stormwater tank water, Huayuankou, Zhengzhou Huanghe water, Quzhou feeder pig manure Chi Shui, three kinds of water all reach national category-B water quality standard after purifying treatment.
The foregoing is only the preferred embodiments of the present invention; not thereby the scope of the claims of the present invention is limited; every equivalent structure transformation utilizing specification sheets of the present invention and accompanying drawing content to do; or be directly or indirectly used in other relevant technical fields, be all in like manner included in scope of patent protection of the present invention.
Claims (10)
1. a pressure sewage purifier, it is characterized in that, described pressure sewage purifier comprises the gac cylinder being filled with gac, the quartz sand cylinder being filled with quartz sand, water inlet cylinder and pressure cylinder from top to bottom successively, wherein, described gac cylinder, quartz sand cylinder and water inlet cylinder are all arranged in tubular, and described pressure cylinder is that taper is arranged; Upper end closed, the lower end of described gac cylinder are open; Two ends all openings of described quartz sand cylinder and water inlet cylinder; The bottom surface opened of described pressure cylinder; The lower end of described gac cylinder is connected with the upper end of quartz sand cylinder, and the lower end of quartz sand cylinder is connected with the upper end of water inlet cylinder, and the water inlet lower end of cylinder is connected with the bottom surface of pressure cylinder; The sidewall of described water inlet cylinder offers raw water inlet, and the top of described gac cylinder offers water purification water outlet, and the cone tip part of described pressure cylinder offers sewage draining exit; Between described gac cylinder and quartz sand cylinder, and be equipped with separation net between quartz sand cylinder and water inlet cylinder.
2. pressure sewage purifier as claimed in claim 1, it is characterized in that, described gac cylinder, quartz sand cylinder, water inlet cylinder and pressure cylinder are coaxial, and the diameter of described gac cylinder, quartz sand cylinder and water inlet cylinder is 800mm, the maximum diameter of described pressure cylinder is 800mm, and minimum diameter is 35mm.
3. pressure sewage purifier as claimed in claim 2, it is characterized in that, the height of described gac cylinder is 600mm; The height of described quartz sand cylinder is 500mm; The height of described water inlet cylinder is 250mm; The height of described pressure cylinder is 300mm.
4. pressure sewage purifier as claimed in claim 3, it is characterized in that, the diameter of described raw water inlet is 50mm; The diameter of described water purification water outlet is 50mm, and the diameter of described sewage draining exit is 25mm.
5. pressure sewage purifier as claimed in claim 4, it is characterized in that, the thickness of described separation net is 1.5mm; The mesh diameter of described separation net is not more than 5mm; It is the stiffening web of 10mm that separation net described in each is provided with at least 5 diameters.
6. the pressure sewage purifier as described in claim 1 to 5, is characterized in that, described gac cylinder upper end is provided with tensimeter.
7. pressure sewage purifier as claimed in claim 6, is characterized in that, the shell activated carbon granule of the gac of filling in described gac cylinder to be diameter be 5mm.
8. pressure sewage purifier as claimed in claim 7, is characterized in that, the quality of the gac of filling in described gac cylinder is 100kg.
9. pressure sewage purifier as claimed in claim 6, is characterized in that, the quartz sand particle of the quartz sand of filling in described quartz sand cylinder to be diameter be 5mm.
10. pressure sewage purifier as claimed in claim 9, is characterized in that, the quality of the quartz sand of filling in described quartz sand cylinder is 400kg.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410491917.6A CN104261580A (en) | 2014-09-23 | 2014-09-23 | Pressure decontaminating water purifying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410491917.6A CN104261580A (en) | 2014-09-23 | 2014-09-23 | Pressure decontaminating water purifying device |
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| Publication Number | Publication Date |
|---|---|
| CN104261580A true CN104261580A (en) | 2015-01-07 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410491917.6A Pending CN104261580A (en) | 2014-09-23 | 2014-09-23 | Pressure decontaminating water purifying device |
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| Country | Link |
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| CN (1) | CN104261580A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109322372A (en) * | 2017-10-30 | 2019-02-12 | 湖南雨创环保工程有限公司 | The non-buried rainwater treatment device of one kind and method |
Citations (10)
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|---|---|---|---|---|
| CN2426877Y (en) * | 2000-06-09 | 2001-04-18 | 任孚保 | Integrated pressure type automatic water purifier |
| CN2440063Y (en) * | 2000-09-04 | 2001-07-25 | 北京科大环保技术研究所 | Farm water-purifying tank |
| CN2727148Y (en) * | 2004-09-15 | 2005-09-21 | 张学勤 | Outdoor and domestic integrated water purifier |
| CN201538726U (en) * | 2009-04-28 | 2010-08-04 | 徐宏志 | Novel rural domestic sewage purification device |
| CN201545751U (en) * | 2009-08-28 | 2010-08-11 | 徐彬 | Waste water purifying and processing device |
| CN202038934U (en) * | 2011-05-17 | 2011-11-16 | 靳宇斯 | Multi-stage serially-connected fluidized bed reclaimed water purification tower |
| CN203715418U (en) * | 2014-03-13 | 2014-07-16 | 山西中力信达环保科技有限公司 | Quick mine water treatment device |
| CN103979749A (en) * | 2014-06-06 | 2014-08-13 | 福州大学 | Treatment device and method for removing heavy metals out of sewage |
| CN203833732U (en) * | 2014-03-06 | 2014-09-17 | 北京联众华禹环保科技有限公司 | Fracturing flowback liquid treatment device |
| CN204097220U (en) * | 2014-09-23 | 2015-01-14 | 深圳市博儒环境技术有限公司 | Pressure sewage purifier |
-
2014
- 2014-09-23 CN CN201410491917.6A patent/CN104261580A/en active Pending
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2426877Y (en) * | 2000-06-09 | 2001-04-18 | 任孚保 | Integrated pressure type automatic water purifier |
| CN2440063Y (en) * | 2000-09-04 | 2001-07-25 | 北京科大环保技术研究所 | Farm water-purifying tank |
| CN2727148Y (en) * | 2004-09-15 | 2005-09-21 | 张学勤 | Outdoor and domestic integrated water purifier |
| CN201538726U (en) * | 2009-04-28 | 2010-08-04 | 徐宏志 | Novel rural domestic sewage purification device |
| CN201545751U (en) * | 2009-08-28 | 2010-08-11 | 徐彬 | Waste water purifying and processing device |
| CN202038934U (en) * | 2011-05-17 | 2011-11-16 | 靳宇斯 | Multi-stage serially-connected fluidized bed reclaimed water purification tower |
| CN203833732U (en) * | 2014-03-06 | 2014-09-17 | 北京联众华禹环保科技有限公司 | Fracturing flowback liquid treatment device |
| CN203715418U (en) * | 2014-03-13 | 2014-07-16 | 山西中力信达环保科技有限公司 | Quick mine water treatment device |
| CN103979749A (en) * | 2014-06-06 | 2014-08-13 | 福州大学 | Treatment device and method for removing heavy metals out of sewage |
| CN204097220U (en) * | 2014-09-23 | 2015-01-14 | 深圳市博儒环境技术有限公司 | Pressure sewage purifier |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109322372A (en) * | 2017-10-30 | 2019-02-12 | 湖南雨创环保工程有限公司 | The non-buried rainwater treatment device of one kind and method |
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Application publication date: 20150107 |
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