CN2494828Y - Comprehensive water purifier - Google Patents

Comprehensive water purifier Download PDF

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Publication number
CN2494828Y
CN2494828Y CN 01255715 CN01255715U CN2494828Y CN 2494828 Y CN2494828 Y CN 2494828Y CN 01255715 CN01255715 CN 01255715 CN 01255715 U CN01255715 U CN 01255715U CN 2494828 Y CN2494828 Y CN 2494828Y
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China
Prior art keywords
water
pipe
sediment
purifier
district
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Expired - Lifetime
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CN 01255715
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Chinese (zh)
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梁克诚
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梁克诚
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Abstract

The utility models provides a comprehensive water purifier integrating the physical, chemical and biological features; before the purification, the jetting flow negative-pressure oxygen increase, the jetting flow negative-pressure ozone increase and the water backwashing are done. The utility model comprises a medicine pool, a pump, a jetting element, a mixing air-floating groove, a reaction sand-deposition pipe, and various areas. The device integrates the chemical cohesion, the ozone increase, the aerobic and other biological things, the physical filtration, the air floatation into one body to purify the water. Therefore, the utility model can effectively and economically deal with a plurality of water sources: the sewage (industrial and life), the general water and the seriously polluted fresh water (rivers, lakes and other water bodies), the underground water with the iron (manganese), the underground water of the high hardness, the underground water with the high fluoride and so on, so as to reach the health standards of the drinking water and the required standards of the users. The utility model is a novel water purifier which can effectively solve the ''difficult water problem''.

Description

The Comprehensive water purifier device
Technical field
The utility model relates to a kind of quality purifying device for water, and particularly a kind of follow-on negative pressure that integrates physics, chemistry, biotechnology adds ozone Comprehensive water purifier device.
Background technology
Existing integral water purifying device generally all is to adopt chemical physics object space method in all one's life that water is handled, and receives certain effect.But, then can not clear the pollution off economically for the processing of high pollution water, special water (as contain high ferrimanganic, high rigidity, contain high fluorine etc.), its effect is not good enough yet.
Summary of the invention
The purpose of this utility model is that a kind of physics, chemistry, biotechnology of integrating will be provided, and adopt that negative pressure adds that comparatively economic incorporate of ozone can be disposed of sewage, the Comprehensive water purifier device of underground water, the surface water (fresh water).
This device as shown in Figure 1-Figure 3, it by water source 1, water absorption tube 2, dispensing pond 4, water pump 5, penstock 7, ejector 8, shell 32, send ozonizer 9 and one to send before oxygen (air) pipe 10, gas mixture floating trough 13, central reaction sand sediment pipe 36, sediment district 26, porous net 22, stable region, filtrate district 28, the filter water subfill 31 etc. to form, its purification of water quality and backwash process are as follows:
Purification of water quality process: as shown in Figure 1, open water pump 5 and suction valve 34, when opening pressure valve 6, the water at water source 1 is sucked by water absorption tube 2, open dispensing valve 3 this moment, so the medicament of explosive barrel 4 just is inhaled in the water absorption tube of dispensing valve 3, such water is through water pump 5 time, after having obtained to mix for the first time, again along the pressure valve 6 of opening, deliver to ejector 8 behind the penstock 7, current are under the effect of the high speed spout 38 (Fig. 3) of ejector 8, form enough negative pressure at negative pressuren zone, so by sending ozonizer 9 and sending oxygen (air) pipe 10 needed ozone, oxygen (air) sucks, medicament in the water like this, ozone, oxygen (air) dissolves in the water effectively, increased the dissolved oxygen in the water, thereby accelerate oxidation and other chemical reaction of materials such as oxygen-consumption, a large amount of ozone have been carried like this, the processing valve 11 of the water of oxygen (air) and medicament by opening, handle water pipe 12, enter gas mixture floating trough 13, here, various materials in the water obtain further to mix--reaction and aeration, make the impurity in the water, obtain sufficient oxidation, coagulation, lighter impurity, emerge and overflow in the air, its scum silica frost is then collected by scum silica frost receiving tank 16, is discharged by scum silica frost vent pipe 17.Removed the water behind this part impurity, continued to flow into from top to bottom the downcomer 50 of central reaction sand sediment pipe 36,, entered upper hose 51 tops, entered inhalent siphon 15 more again by downcomer 50 bottoms through water-in 52 (Fig. 2).Water is in the time of central reaction sand sediment pipe 36 stops, impurity wherein is owing to obtained sufficient oxidizing reaction chance, so be condensed into the floss of alumen ustum shape substantially and dissolve in enough oxygen, taking the water of these materials, by inhalent siphon 15, and porous water distribution (row's mud) pipe 14, from lower to upper, evenly enter sediment district 26 at leisure, from bottom to top flow, so precipitated by cohesion impurity major part in the water; Simultaneously, sufficient dissolved oxygen in the water (ozone) can with water in be difficult to the material oxidation further of oxidation, after working after a while, the increase of the mud slag of being held back along with sediment district 26, oxygen consumption and double oxygen animalcule constantly breeding increase, under action of microorganisms, organic in the water (or other) impurity, can be because of constantly being adsorbed, digest, degrade by it, and further minimizing.This water, after passing the mud slag in sediment district 26, its large granular impurity is trapped, it is carrying tiny impurity particle and is continuing to rise to porous net 22, when it passes mesh, form the membranoid substance of one deck with many microorganisms because of impurity is adsorbed around the hole, this membranoid substance has extremely strong absorption and Degradation for organic (or inorganic) impurity, and the impurity in the water is further reduced; In addition,, therefore, after water enters the stable region, make the stable streamflow regime of this district formation because porous net 22 is distributed in the top in sediment district 26 and the bottom of stable region 27 equably, be convenient in the water that impurity precipitates further and and water sepn.Because in sediment district 26, stable region 27, the impurity that porous net 22 is held back constantly increases, microorganism wherein needs to update owing to metabolism is constantly aging, cause their cisco unity malfunctions, therefore, must regularly open wash water valve 49, above-mentioned redundant impurities is got rid of, made it to resume work.Be trapped the water of most impurity, by 27 tops, stable region, by communicating pipe 33, from bottom to top, enter the preceding water subfill 31 of filter, again by water subfill 31 before the filter, flow into filtrate district 28 from top to bottom, under its effect such as absorption of granule filter material 46, on the surface of granule filter material 46, the biology filter that can form one deck attached microbial at leisure is unconcerned, because filter membrane has absorption to impurity (comprising bacterium), digestion, the ability of degraded, therefore, water is after passing through it, and impurity promptly is trapped, the water of cleaning just passes granule filter material 46, collect by clear water collection tube 48 again, by purge valve 24, clear water pipe 23 flows into clean water basin 25 (user).
Process is washed in reaction: when the production water yield of device constantly increases, the filter membrane on granule filter material 46 surfaces can constantly increase, cause its water production rate constantly to reduce, when the water yield reduces to can not meet design requirement the time, then must carry out back flushing to it, unnecessary filter membrane is removed, made it to recover normal operating conditions.Concrete operations are: close medicine valve 3, close purge valve 24, open recoil wash water valve 18, close and send ozonizer 9, open recoil valve 29, open water pump 5, so after current just carry a large amount of oxygen (air) by ejector 8, by the porous clear water collection tube 48 of 28 bottoms, filtrate district, from bottom to top, equably granule filter material 46 is carried out air-water backwashing, sewage is promptly collected by recoil sewage collecting pipe 53, again through recoil wash water valve 18, recoil blow-off pipe 19, enter pollution discharge pond 20, each backwashing time was generally 10-30 minute, but will depend on the circumstances, Here it is backwash process.Back flushing finishes, and can recover the purification of water quality process, continues to produce.
Characteristics of the present utility model are: under negative pressure condition, add ozone, increased the oxidative function to organism (or other impurity) greatly, help to purify water; In addition, between sediment district and stable region, established the porous net, be convenient to the impurity in their trap water and form the satisfactory stability stream mode, be convenient to water and separate, be beneficial to effects of purification quality with impurity in the stable region.
Description of drawings
Fig. 1 is that Fig. 2 is along 1-1 line top view;
Fig. 2 is that Fig. 1 is along 2-2 line sectional view;
Fig. 3 is the ejector structure iron.
In Fig. 1-3: 1) water source 2) suction hose 3) dispensing valve 4) explosive barrel 5) water pump 6) pressure valve 7) force pipe 8) ejector 9) send ozonizer 10) send oxygen (air) pipe 11) process valve 12) process water pipe 13) gaseous mixture floating trough 14) row's mud pipe 15) oral siphon 16) scum silica frost feeder 17) scum silica frost discharge pipe 18) recoil blowoff valve 19) recoil blow-off pipe 20) cesspool 21) porous pipes 22) porous web 23) clear water pipe 24) purge valve 25) clear water reserviors (user) 26) sediment district 27) stable region 28) filtrate district 29) recoil valve 30) recoil tube 31) water subfill 32 before the filter) shell 33) communicating pipe 34) suction valve 35) median septum 36) central reaction sand sediment pipe 37) sediment outflow pipe 38) spout D139) receiving port D 240) come water pipe D 341) rising pipe D 442) negative pressuren zone 43) inlet zone 44) mixing zone 45) closed bottom 46) granule filter material 47) sediment outflow pipe 48) porous clear water collection tube 49) row's mud valve 50) downcomer 51) upper hose 52) water-in 53) recoil sewage collecting pipe
Embodiment
Comprehensive water purifier device as Figure 1-3, comprise water source 1, dispensing pond 4, water absorption tube 2, water pump 5, penstock 7, ejector 8, shell 32, send ozonizer 9, water subfill 31 before (air) pipe 10 that send oxygen, gas mixture floating trough 13, center sand sediment pipe 36, filter, it is characterized in that processed water is before entering gas mixture floating trough 13, on penstock 7, installed one and be equipped with one and send ozonizer 9 and one to send oxygen (air) pipe 10, water has been added the ejector 8 of ozone and oxygen (air); This ejector 8 is by inlet zone 43, negative pressuren zone 42, mixing zone 44, spout D 138, come water pipe D 340, receive D 439 compositions such as grade.Wherein come water pipe D 340, rising pipe D 441 caliber with come water pipe D 3The caliber of 40 penstocks that connect 7 is identical, spout D 138 diameter is for coming water pipe D 340 diameter is 0.2-0.4 times, receiving port D 239 diameter is spout D 138 1.2-1.4 times, spout D 138 with receiving port D 2Distance between 39 is the 50-150 millimeter, and negative pressuren zone 42 is sealed in spray D 138 receiving port D 2Between 39; Being provided with the aperture between the stable region 27 on sediment district 26 and its top is 15-35 purpose porous net 22, is convenient to improve purifying water effect.Place the sediment district 26 under the porous net 22, one side of the porous water distribution that the bottom is provided with (row's mud) pipe 14 is connected with central reaction sand sediment pipe 36, and the other side then joins with row's mud valve 49.Filtrate district 28 is made up of closed bottom 45, granule filter material 46, communicating pipe 33, recoil valve 29, porous clear water collection tube 48.Gas mixture floating trough 13 by the scum silica frost receiving tank 16 that its top is provided with, is formed by the water-in 50 that central reaction sand sediment pipe 36 1 upper lateral parts are provided with.Central reaction sand sediment pipe 36, form by downcomer 50, upper hose 51, median septum 35, water inlet pipe 15, sand dump valve 47, sediment outflow pipe 37, and the median septum 35 that downcomer 50, upper hose 51 separate, its bottom left aquaporin so that the water of downcomer 50 by under enter upper hose 51; And the upper orifice of water inlet pipe 15 is located at the top of upper hose 51, and its underpart is connected with porous water distribution (row's mud) pipe 14.Water subfill 31 before the filter is provided with recoil sewage collecting pipe 53, recoil wash water valve 18 and recoil blow-off pipe 19, so that the usefulness of the sewage when getting rid of granule filter material 46 recoils.

Claims (8)

1, a kind of Comprehensive water purifier device, its structure comprises water source (1), water absorption tube (2), dispensing pond (4), water pump (5), penstock (7), ejector (8), shell (32), it is characterized in that having on the negative pressuren zone of ejector (8) one to send ozonizer (9) and one to send oxygen (air) pipe (10), a gas mixture floating trough (13) is arranged at the top of purifier, there is a central reaction sand sediment pipe (36) at the middle part, the preceding water subfill (31) of a filter is arranged in the purifier, filtrate district (28), sediment district (26), and have one deck porous net (22) to be arranged between filtrate district and the sediment district.
2, Comprehensive water purifier device according to claim 1 is characterized in that coming water pipe D in the ejector (8) 3(40), the D of rising pipe 4(41) caliber comes water pipe D with it 3(40) caliber of the penstock that is connect (7) is identical, spout D 1(38) diameter is for coming water pipe D 3The 0.2-0.4 of diameter (40) times, receiving port D 2(39) diameter is spout D 1(38) 1.2-1.4 of diameter times, spout D 1(38) with receiving port D 2(39) apart from being the 50-150 millimeter, negative pressuren zone (42) is sealed in spout D between 1(38), receiving port D 2(39) between.
3, Comprehensive water purifier device according to claim 1 is characterized in that a scum silica frost receiving tank (16) is arranged on the gas mixture floating trough (13), and by central reaction sand sediment pipe (36) top a drain gully (50) is being arranged.
4, Comprehensive water purifier device according to claim 1, it is characterized in that central reaction sand sediment pipe (36) is made up of downcomer (50), upper hose (51), median septum (35), water inlet pipe (15), sand dump valve (47), sediment outflow pipe (37), aquaporin was left in median septum (35) bottom that downcomer (50), upper hose (51) separate, so that the water of downcomer (50) by under enter upper hose (51), water inlet pipe (15) upper orifice is located at the top of upper hose (51), and its underpart is connected with porous water distribution (row's mud) pipe (14).
5, Comprehensive water purifier device according to claim 1, it is characterized in that filtering have in the preceding water subfill (31) one the recoil sewage collecting pipe (53), the recoil wash water valve (18) and the recoil blow-off pipe (19).
6, Comprehensive water purifier device according to claim 1 is characterized in that one deck closed bottom (45), granule filter material (46) and communicating pipe (33), recoil valve (29) and porous clear water collection tube (48) are arranged in the filtrate district (28).
7, Comprehensive water purifier device according to claim 1, it is characterized in that placing its aperture of porous net (22) between sediment district (26) and filtrate district (28) is the 15-35 order.
8, Comprehensive water purifier device according to claim 1, one side that the bottom that it is characterized in that sediment district (26) is provided with porous water distribution (row's mud) pipe (14) is connected with central reaction sand sediment pipe (36), and the other side then is connected with row's mud valve (49).
CN 01255715 2001-09-14 2001-09-14 Comprehensive water purifier Expired - Lifetime CN2494828Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 01255715 CN2494828Y (en) 2001-09-14 2001-09-14 Comprehensive water purifier

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Application Number Priority Date Filing Date Title
CN 01255715 CN2494828Y (en) 2001-09-14 2001-09-14 Comprehensive water purifier

Publications (1)

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CN2494828Y true CN2494828Y (en) 2002-06-12

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1297492C (en) * 2004-12-27 2007-01-31 西安建筑科技大学 Air floated water treating separators
CN103601339A (en) * 2013-11-06 2014-02-26 西安建筑科技大学 Process system for synergically removing Fe, Mn and ammonia nitrogen in composite micropolluted source water
CN104787822A (en) * 2015-05-06 2015-07-22 湖州天濮环保科技有限公司 Sewage separating device
CN109912077A (en) * 2019-03-29 2019-06-21 武汉理工大学 It is a kind of using ferric manganese ore as the pollution of chromium underground water in-situ immobilization simulator of reaction medium

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1297492C (en) * 2004-12-27 2007-01-31 西安建筑科技大学 Air floated water treating separators
CN103601339A (en) * 2013-11-06 2014-02-26 西安建筑科技大学 Process system for synergically removing Fe, Mn and ammonia nitrogen in composite micropolluted source water
CN104787822A (en) * 2015-05-06 2015-07-22 湖州天濮环保科技有限公司 Sewage separating device
CN104787822B (en) * 2015-05-06 2016-12-07 浙江天濮环保科技有限公司 A kind of sewage separating device
CN109912077A (en) * 2019-03-29 2019-06-21 武汉理工大学 It is a kind of using ferric manganese ore as the pollution of chromium underground water in-situ immobilization simulator of reaction medium

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GR01 Patent grant
C14 Grant of patent or utility model
CX01 Expiry of patent term

Expiration termination date: 20110914

Granted publication date: 20020612

C17 Cessation of patent right