CN205367917U - Integration is filtered and is adsorbed water purification system - Google Patents
Integration is filtered and is adsorbed water purification system Download PDFInfo
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- CN205367917U CN205367917U CN201520969716.2U CN201520969716U CN205367917U CN 205367917 U CN205367917 U CN 205367917U CN 201520969716 U CN201520969716 U CN 201520969716U CN 205367917 U CN205367917 U CN 205367917U
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- Prior art keywords
- tower
- chamber
- layer
- mud discharging
- water
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 80
- 238000000746 purification Methods 0.000 title abstract description 3
- 238000007599 discharging Methods 0.000 claims description 36
- 238000004140 cleaning Methods 0.000 claims description 16
- 238000010521 absorption reaction Methods 0.000 claims description 14
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 14
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 9
- 229910052748 manganese Inorganic materials 0.000 claims description 7
- 239000011572 manganese Substances 0.000 claims description 7
- 229920000742 Cotton Polymers 0.000 claims description 6
- 229910052799 carbon Inorganic materials 0.000 claims description 6
- 239000004576 sand Substances 0.000 claims description 6
- 239000000741 silica gel Substances 0.000 claims description 6
- 229910002027 silica gel Inorganic materials 0.000 claims description 6
- 150000002696 manganese Chemical class 0.000 claims description 4
- PWHULOQIROXLJO-UHFFFAOYSA-N manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 claims description 4
- 210000003141 Lower Extremity Anatomy 0.000 claims description 3
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 claims description 3
- 239000003830 anthracite Substances 0.000 claims description 3
- 239000003245 coal Substances 0.000 claims description 3
- 239000011148 porous material Substances 0.000 claims description 3
- 238000010926 purge Methods 0.000 claims description 3
- 239000012535 impurity Substances 0.000 abstract description 11
- 238000005429 turbidity Methods 0.000 abstract description 8
- 238000001556 precipitation Methods 0.000 abstract description 3
- 230000000694 effects Effects 0.000 description 7
- 238000004062 sedimentation Methods 0.000 description 6
- 238000001914 filtration Methods 0.000 description 4
- 238000010276 construction Methods 0.000 description 3
- 239000002384 drinking water standard Substances 0.000 description 3
- 231100000614 Poison Toxicity 0.000 description 2
- 230000002159 abnormal effect Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000000796 flavoring agent Substances 0.000 description 2
- 235000019634 flavors Nutrition 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- JLUFWMXJHAVVNN-UHFFFAOYSA-N Methyltrichlorosilane Chemical compound C[Si](Cl)(Cl)Cl JLUFWMXJHAVVNN-UHFFFAOYSA-N 0.000 description 1
- 230000001413 cellular Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000005202 decontamination Methods 0.000 description 1
- 230000003588 decontaminative Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 230000035622 drinking Effects 0.000 description 1
- 235000021271 drinking Nutrition 0.000 description 1
- 230000004634 feeding behavior Effects 0.000 description 1
- 230000002147 killing Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000000644 propagated Effects 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
Abstract
The utility model discloses an integration is filtered and is adsorbed water purification system, including the primary settling tower that connects gradually, inclined tube setting chamber, filter chamber and adsorption chamber, the primary settling tower includes inside and outside tower and the mud discharge -channel between the two, the relative cross arrangement of nei tanei has tilt up's baffling board, be equipped with inclined pipe precipitation device in the inclined tube setting chamber, inclined tube setting chamber passes through the lower part pipeline and the switch -on of interior top of the tower portion, the filter chamber top is equipped with the water distributor and the middle part is equipped with the filter layer, the water distributor is intake the end and is connected with the inclined tube setting chamber top, the filter chamber bottom is equipped with the delivery port, be equipped with multilayer adsorption layer and vertical water distributor in the adsorption chamber, the upper end of vertical water distributor is worn out the adsorbed layer and is connected the water -locator, the lower extreme stretches out the adsorption chamber and is connected with the delivery port of filter chamber, the utility model discloses utilize the primary settling tower to reduce the turbidity of raw water, aquatic residual impurity has further been detached through inclined tube setting chamber, filter chamber, adsorption chamber again to the raw water, and the entire system overall arrangement is compact, and area is little.
Description
Technical field
This utility model relates to water-suppling treatment equipment field, is specifically related to a kind of integration filter absorption water cleaning systems.
Background technology
nullThe activity of the mankind can make substantial amounts of industry、Agricultural and domestic refuse enter in water，Water body is made to be contaminated，The current whole world there are about the sewage of billion cubic meter more than 4200 every year and enters rivers,lakes and seas，Pollute the fresh water of 5.5 tcms，This is equivalent to more than the 14% of whole world runoff volume，Increasingly the water aggravated pollutes，The living safety of the mankind is constituted significant threat，Become human health、The major obstacles of economy and social sustainable development，Investigate according to authoritative institution of the world，In developing country，Various diseases has 80% to be because having drunk antihygienic water and having propagated，Annual at least cause global 200d 00,000 people death because drinking unhygienic water，Therefore water pollutes and is referred to as " world's number one killer "，At present，In river and the dirty water decontamination handles，Various informative water treatment facilities just play an important role，But general purifier requires that influent turbidity is not high，The water that some turbidity are higher is also tended to be difficult to reach drinking water standard after general process，Complexity additionally, due to water treatment technology，It is various to there is cellular construction in traditional water supply water purification integration apparatus、The defect that land occupation resource is big.
Utility model content
For solving above technical problem, this utility model provides a kind of integration filter absorption water cleaning systems being applicable to the higher former water of turbidity.
Technical scheme is as follows:
A kind of integration filter absorption water cleaning systems, including the primary settling tower being sequentially connected with, tube settling room, filter chamber and adsorption chamber, it it is critical only that:
Described primary settling tower includes Wai Ta and Nei Ta, therebetween mud discharging passage is formed, the bottom of described interior tower is connected to inlet channel, intersect from top to bottom at described Nei Tanei and be provided with at least two deflection plate, this deflection plate is inclined upwardly 5-10 °, described deflection plate lower side is fixing with the tower wall of described interior tower to be connected, described deflection plate upper side edge is respectively equipped with baffle plate, each described deflection plate and described Nei Ta junction are respectively equipped with mud discharging mouth, and the lower limb of this mud discharging mouth is concordant with this deflection plate lower side；
Described tube settling indoor are provided with inclined-pipe settler, and the described tube settling room below this inclined-pipe settler is connected with described interior top of tower by pipeline；
Described filter chamber top is provided with water distributor, and described water distributor water inlet end is connected with described tube settling ceiling portion, is provided with outlet, is provided with filter course in the middle part of described filter chamber bottom described filter chamber；
Adsorption layer and vertical water distributor it is provided with in described adsorption chamber, the two ends of this vertical water distributor pass described adsorption layer respectively, the upper end of this vertical water distributor is connected to water-locator, described adsorption chamber is stretched out in the lower end of this vertical water distributor and the outlet with described filter chamber is connected, adsorption chamber below described adsorption layer is connected to outlet conduit, the diatomite layer that described adsorption layer includes setting gradually from the bottom up, fluffy cotton layer, layer of silica gel and active carbon layer, the thickness of described diatomite layer, fluffy cotton layer, layer of silica gel and active carbon layer ratio is for 3:2:1.5:1.
The technical program is adopted to provide the benefit that former water that turbidity the is higher deflection plate through primary settling tower, wherein bigger impurity and can enter Wai Tazhong on deflection plate by preliminary sedimentation, now the turbidity of former water is substantially reduced, former water impurity in water after the secondary precipitation of tube settling room is substantially removed, former water after filtering then through filter chamber can reach drinking water standard substantially, and now former water will be removed further then through the abnormal flavour remained in water after adsorption chamber adsorption filtration and poisonous and harmful substance.
As preferably: above-mentioned water-locator includes star-like arm, this star-like arm external part is connected to same outer endless tube, it is provided with interior endless tube, described outer endless tube and interior endless tube in this outer endless tube to connect with described star-like arm respectively, described interior endless tube, outer endless tube and star-like arm are respectively equipped with water distributing pore.Adopting the beneficial effects of the utility model is the top that water source can be distributed to adsorption layer by disc type narrow meshed water-locator uniformly, and will not produce bigger turbulent water.
Above-mentioned star-like arm is Samsung arm, and the angle between adjacent arm is 120 °.This scheme is adopted to provide the benefit that the fixing more firm of outer endless tube and interior endless tube.
Above-mentioned adsorption layer is connected with back purge system.This scheme is adopted to provide the benefit that the service life that can effectively extend adsorption layer.
Above-mentioned deflection plate is 20-30, is evenly distributed at the bottom of the tower of described interior tower and between tower top.Deflection plate density is arranged rationally to adopt this scheme to provide the benefit that, shortens the distance of impurity sedimentation, is conducive to accelerating the sedimentation of impurity.
Being provided with the first mud discharging pipe at the bottom of the tower of above-mentioned outer tower, described first mud discharging pipe is provided with the first mud discharging and regulates valve.The beneficial effect adopting this scheme is deposited on the mud at the bottom of outer tower tower and regularly can be discharged by mud discharging pipe.
Being provided with mud collection bucket bottom above-mentioned tube settling room, the bottom of this mud collection bucket is provided with the second mud discharging pipe, and described second mud discharging pipe is provided with the second mud discharging and regulates valve.Adopting this scheme to provide the benefit that can periodically blowdown, it is to avoid mud is piled up and too much affected tube settling effect.
Above-mentioned first mud discharging regulates valve and the second described mud discharging regulates valve opening time and is spaced apart 20-24 hour.Adopt this scheme to provide the benefit that regularly to be got rid of by the mud of deposition, it is to avoid mud is piled up too much, affects sedimentation effect.
Above-mentioned primary settling tower and described tube settling room are connected with sludge-tank, and the top of above-mentioned primary settling tower, tube settling room, filter chamber and described adsorption chamber is equipped with observation window, and described tube settling ceiling portion is provided with automatic exhaust steam valve.Adopting this scheme to provide the benefit that, the mud of deposition can be concentrated is emitted in sludge-tank, facilitates workman to concentrate cleaning, and workman can pass through observation window fast check purifier inner case.
Above-mentioned filter course includes manganese layer of sand and the anthracite coal measure being laid on this manganese layer of sand.Adopt this scheme to provide the benefit that the residual impurity that can remove in water further, particularly ferrum, manganese class impurity.
Beneficial effect:
Adopting the beneficial effects of the utility model is that former water that turbidity is higher is through primary settling tower, wherein bigger impurity can settle layer by layer on deflection plate, deflection plate density arranges rationally, shorten the distance of impurity sedimentation, be conducive to accelerating the sedimentation of impurity, reduce the turbidity of former water, former water filters then through filter chamber after the secondary precipitation of tube settling room can reach drinking water standard substantially, now former water will be removed further then through the abnormal flavour remained in water after adsorption chamber adsorption filtration and poisonous and harmful substance, additionally this device is to the ferrum in water, the impurity such as manganese have good filtration result, whole system reasonable in design, compact in design, it is greatly saved the floor space of structures, it is applicable not only to the construction of water supply plant on a small scale, the construction for larger water supply plant of the multiple stage mode in parallel can also be passed through.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model；
Fig. 2 is the enlarged drawing of Fig. 1；
Fig. 3 is water distributor structure schematic diagram.
Detailed description of the invention
Below in conjunction with embodiment and accompanying drawing, the utility model is described in further detail.
As Figure 1-3, a kind of integration filter absorption water cleaning systems, including the primary settling tower 1 being sequentially connected with, tube settling room 2, filter chamber 3 and adsorption chamber 4, described primary settling tower 1 and tube settling room 2 are connected with sludge-tank 8, the top of described primary settling tower 1, tube settling room 2, filter chamber 3 and described adsorption chamber 4 is equipped with observation window 12, and top, described tube settling room 2 is provided with automatic exhaust steam valve 14.
nullDescribed primary settling tower 1 includes outer tower 104 and Nei Ta 103，Therebetween mud discharging passage 106 is formed，The bottom of described interior tower 103 is connected to inlet channel 5，Intersect from top to bottom in described interior tower 103 and be provided with at least two deflection plate 102，Described deflection plate 102 is 20-30，It is evenly distributed at the bottom of the tower of described interior tower 103 and between tower top，This deflection plate 102 is inclined upwardly 5-10 °，Described deflection plate 102 lower side is fixing with the tower wall of described interior tower 103 to be connected，Described deflection plate 102 upper side edge is respectively equipped with baffle plate 101，Each described deflection plate 102 is respectively equipped with mud discharging mouth 105 with described interior tower 103 junction，The lower limb of this mud discharging mouth 105 is concordant with this deflection plate 102 lower side，Thus it is deposited on the mud on deflection plate 102 to be entered in mud discharging passage 106 by described mud discharging mouth 105，And be gradually deposited at the bottom of the tower of outer tower 104，The first mud discharging pipe 6 it is provided with at the bottom of the tower of described outer tower 104，Described first mud discharging pipe 6 is provided with the first mud discharging and regulates valve 7.
It is provided with inclined-pipe settler 202 in described tube settling room 2, described tube settling room 2 below this inclined-pipe settler 202 is connected with described interior tower 103 top by pipeline 11, it is provided with mud collection bucket 201 bottom described tube settling room 2, the bottom of this mud collection bucket 201 is provided with the second mud discharging pipe 9, described second mud discharging pipe 9 is provided with the second mud discharging and regulates valve 10, and described first mud discharging regulates valve 7 and the second described mud discharging adjustment valve 10 opening time is spaced apart 20-24 hour.
Top, described filter chamber 3 is provided with water distributor 13, described water distributor 13 water inlet end and top, described tube settling room 2 are connected by pipeline, it is provided with outlet bottom described filter chamber 3, being provided with filter course in the middle part of described filter chamber 3, described filter course includes manganese layer of sand and the anthracite coal measure being laid on this manganese layer of sand.
Adsorption layer 17 and vertical water distributor 18 it is provided with in described adsorption chamber 4, the two ends of this vertical water distributor 18 pass described adsorption layer 17 respectively, the upper end of this vertical water distributor 18 is connected to water-locator 16, described adsorption chamber 4 is stretched out in the lower end of this vertical water distributor 18 and the outlet with described filter chamber 3 is connected, adsorption chamber 4 below described adsorption layer 17 is connected to outlet conduit 15, described adsorption layer 17 includes the diatomite layer 171 set gradually from the bottom up, fluffy cotton layer 172, layer of silica gel 173 and active carbon layer 174, described diatomite layer 171, fluffy cotton layer 172, the thickness of layer of silica gel 173 and active carbon layer 174 is than for 3:2:1.5:1, described adsorption layer 17 is connected with back purge system 19.
Described water-locator 16 includes star-like arm 164, described star-like arm 164 is Samsung arm, angle between adjacent arm is 120 °, this star-like arm 164 external part is connected to same outer endless tube 162, it is provided with interior endless tube 163 in this outer endless tube 162, described outer endless tube 162 is connected with described star-like arm 164 respectively with interior endless tube 163, is respectively equipped with water distributing pore 161 on described interior endless tube 163, outer endless tube 162 and star-like arm 164.
Finally it should be noted that; foregoing description is only preferred embodiment of the present utility model; those of ordinary skill in the art is under enlightenment of the present utility model; under the premise without prejudice to this utility model objective and claim; can making and representing like multiple types, such conversion each falls within protection domain of the present utility model.
Claims (10)
1. an integration filter absorption water cleaning systems, including the primary settling tower (1) being sequentially connected with, tube settling room (2), filter chamber (3) and adsorption chamber (4), it is characterised in that:
Described primary settling tower (1) includes outer tower (104) and interior tower (103), therebetween mud discharging passage (106) is formed, the bottom of described interior tower (103) is connected to inlet channel (5), intersect from top to bottom in described interior tower (103) and be provided with at least two deflection plate (102), this deflection plate (102) is inclined upwardly 5-10 °, described deflection plate (102) lower side is fixing with the tower wall of described interior tower (103) to be connected, described deflection plate (102) upper side edge is respectively equipped with baffle plate (101), each described deflection plate (102) and described interior tower (103) junction are respectively equipped with mud discharging mouth (105), the lower limb of this mud discharging mouth (105) is concordant with this deflection plate (102) lower side；
Being provided with inclined-pipe settler (202) in described tube settling room (2), the described tube settling room (2) of this inclined-pipe settler (202) lower section is connected with described interior tower (103) top by pipeline (11)；
Described filter chamber (3) top is provided with water distributor (13), described water distributor (13) water inlet end is connected with described tube settling room (2) top, bottom, described filter chamber (3) is provided with outlet, and described filter chamber (3) middle part is provided with filter course；
nullAdsorption layer (17) and vertical water distributor (18) it is provided with in described adsorption chamber (4)，The two ends of this vertical water distributor (18) pass described adsorption layer (17) respectively，The upper end of this vertical water distributor (18) is connected to water-locator (16)，Described adsorption chamber (4) is stretched out in the lower end of this vertical water distributor (18) and the outlet with described filter chamber (3) is connected，The adsorption chamber (4) of described adsorption layer (17) lower section is connected to outlet conduit (15)，Described adsorption layer (17) includes the diatomite layer (171) set gradually from the bottom up、Fluffy cotton layer (172)、Layer of silica gel (173) and active carbon layer (174)，Described diatomite layer (171)、Fluffy cotton layer (172)、The thickness of layer of silica gel (173) and active carbon layer (174) is than for 3:2:1.5:1.
2. integration filter according to claim 1 absorption water cleaning systems, it is characterized in that: described water-locator (16) includes star-like arm (164), this star-like arm (164) external part is connected to same outer endless tube (162), it is provided with interior endless tube (163) in this outer endless tube (162), described outer endless tube (162) is connected with described star-like arm (164) respectively with interior endless tube (163), is respectively equipped with water distributing pore (161) on described interior endless tube (163), outer endless tube (162) and star-like arm (164).
3. integration filter according to claim 2 absorption water cleaning systems, it is characterised in that: described star-like arm (164) is Samsung arm, and the angle between adjacent arm is 120 °.
4. integration filter according to claim 1 and 2 absorption water cleaning systems, it is characterised in that: described adsorption layer (17) is connected with back purge system (19).
5. integration filter according to claim 4 absorption water cleaning systems, it is characterised in that: described deflection plate (102) is 20-30, is evenly distributed at the bottom of the tower of described interior tower (103) and between tower top.
6. integration filter adsorbs water cleaning systems according to claim 1 or 5, it is characterized in that: be provided with the first mud discharging pipe (6) at the bottom of the tower of described outer tower (104), described first mud discharging pipe (6) is provided with the first mud discharging and regulates valve (7).
7. integration filter according to claim 6 absorption water cleaning systems, it is characterized in that: described tube settling room (2) bottom is provided with mud collection bucket (201), the bottom of this mud collection bucket (201) is provided with the second mud discharging pipe (9), and described second mud discharging pipe (9) is provided with the second mud discharging and regulates valve (10).
8. integration filter according to claim 7 absorption water cleaning systems, it is characterised in that: described first mud discharging regulates valve (7) and the second described mud discharging adjustment valve (10) opening time is spaced apart 20-24 hour.
9. integration filter according to claim 4 absorption water cleaning systems, it is characterized in that: described primary settling tower (1) and tube settling room (2) are connected with sludge-tank (8), the top of described primary settling tower (1), tube settling room (2), filter chamber (3) and described adsorption chamber (4) is equipped with observation window (12), and described tube settling room (2) top is provided with automatic exhaust steam valve (14).
10. the integration filter absorption water cleaning systems according to claim 1,2 or 3, it is characterised in that: described filter course includes manganese layer of sand and the anthracite coal measure being laid on this manganese layer of sand.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520969716.2U CN205367917U (en) | 2015-11-30 | 2015-11-30 | Integration is filtered and is adsorbed water purification system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520969716.2U CN205367917U (en) | 2015-11-30 | 2015-11-30 | Integration is filtered and is adsorbed water purification system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205367917U true CN205367917U (en) | 2016-07-06 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520969716.2U Expired - Fee Related CN205367917U (en) | 2015-11-30 | 2015-11-30 | Integration is filtered and is adsorbed water purification system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205367917U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105502713A (en) * | 2015-11-30 | 2016-04-20 | 綦江县狮子桥供水有限公司 | Waterwork water purification treatment equipment |
-
2015
- 2015-11-30 CN CN201520969716.2U patent/CN205367917U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105502713A (en) * | 2015-11-30 | 2016-04-20 | 綦江县狮子桥供水有限公司 | Waterwork water purification treatment equipment |
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Legal Events
| 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: 20160706 Termination date: 20161130 |
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| CF01 | Termination of patent right due to non-payment of annual fee |