CN1174814A - Water purifier with pressure-bearing type stepless speed changing vortex reactor - Google Patents
Water purifier with pressure-bearing type stepless speed changing vortex reactor Download PDFInfo
- Publication number
- CN1174814A CN1174814A CN 96117681 CN96117681A CN1174814A CN 1174814 A CN1174814 A CN 1174814A CN 96117681 CN96117681 CN 96117681 CN 96117681 A CN96117681 A CN 96117681A CN 1174814 A CN1174814 A CN 1174814A
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- pressure
- reactor
- water
- housing
- back taper
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Abstract
The present invention relates to a water-purifying equipment with coiled reactor, and is characterized by that it includes outer shell, coiled reactor, filter, water inlet and outlet ,and the coiled reactor and filter are placed in the outer shell, the water inlet is connected to the side of bottom end of said coiled reactor, and the water discharged from the coiled reactor is flowed into the space in the shell, and the inlet of the filter is communicated with the space of the shell, and its discharge hole is connected with water outlet. Said invention possesses the advantages of simple structure ,small valume, low cost and good purification effect.
Description
The invention belongs to the device for purifying potable water technical field.
Drink water purification, often must be through the flocculation treatment program, promptly in former water, add coagulating agent, as Tai-Ace S 150, ferrous sulfate, iron trichloride, aluminium chlorohydroxide, alum, polyacrylamide etc., mixing the back reacts in reactor, make the impurity in the former water combine flocculation with composition in the coagulating agent, precipitation then is to remove the middle impurity that anhydrates.Good in order to ensure reaction effect, generally should satisfy two major requirements: the firstth, the flow velocity Ying Youda in reactor diminishes gradually, under bigger flow velocity, collision fully and absorption could take place in the colloidal solid in the water, little at less flow velocity, colloidal solid just can be formed bigger wadding grain, precipitates; The secondth, the enough reaction times be arranged, to guarantee the abundant and perfect of reaction process, generally take 10-30 minute.The reactor of prior art has iris type reactor, whirlwind-type reactor, gravity type boat davit Vortex reactor, folded plate type reactor, multistage pore chamber whirlwind-type reactor, mechanical stir-reactor.Yet the effect of these several reactors is all undesirable, and for example their floor spaces are big, is unsuitable for using and family expenses in the transportation means; In the whirlwind-type reactor, current are entered by upper side wall by the lower wall of reactor and flow out, water forms eddy flow from the bottom to top in reactor, each reactor can only produce a kind of flow velocity, need 2 above reactors in series that its existing big flow velocity is had again than minimum velocity, and mixed effect is insufficient, and the reaction times is longer; In the gravity type boat davit Vortex reactor, current are directly entered by the upper end by the reactor lower end of back taper and flow out, current by the time on conical wall, produce eddy current to strengthen mixing effect, yet also need 2 above reactors in series to use, could have again than minimum velocity by existing big flow velocity, and this reactor just produces reaction under the action of gravity of water, reaction effect is not good, and the reaction times is longer; Mechanism's stirring reactor complex structure.
The object of the present invention is to provide a kind of can produce eddy current can produce again eddy flow, flow velocity can by diminish gradually greatly, volume simple in structure is little, sufficient reacting and only need the purifier of A reactor.
The object of the present invention is achieved like this; A kind of purifier that pressure-bearing type stepless speed changing vortex reactor is arranged comprises housing, pressure-bearing type vortex reactor, strainer, water-in, water outlet, slag notch.Pressure-bearing type vortex reactor and strainer are contained in the housing, and vortex reactor is contained in the housing bottom, and the pressure-bearing type vortex reactor comprises back taper pipe, loam cake, and loam cake is contained in back taper pipe upper end, and the logical intravital space of shell of outlet is arranged therebetween.Space in the logical housing of the import of strainer, outlet connects water outlet.Water-in is connected on side, back taper pipe bottom, current are gone into from back taper pipe bottom end side surface current, in the back taper pipe, form eddy flow from bottom to up, and between eddy flow and tube wall, produce eddy current, enter the intravital space of shell by the outlet outflow between back taper pipe upper end and the loam cake, enter strainer then after filtering, flow out, become and purify waste water by water outlet.Enter the water of vortex reactor by side direction, the vortex water flow that in the back taper pipe, is produced, flow velocity can be realized stepless change by diminishing greatly gradually, in the current than big flow velocity of back taper pipe hypomere, collision based on colloidal solid, and in the current than minimum velocity of back taper pipe epimere, based on flocculation, because vortex reactor is in the pressure field of whole refining plant, under big hydraulic pressure effect, its reaction is abundant than the gravity type boat davit Vortex reactor.The wadding grain that throwing out in vortex reactor forms enters the space between vortex reactor and the housing, is deposited in the slag notch place of purifier bottom gradually, and button is left cinder notch and discharged precipitation in case of necessity.
Advantage of the present invention is: adopt the pressure-bearing type vortex reactor, current can be realized stepless change in reactor, and flow velocity is reflected at the artesian condition operation from large to small, and is abundant than the gravity type boat davit Vortex reactor.The reactor of prior art needs more than 2, and the present invention only needs 1 reactor, and simple in structure, volume is little, and cost is low, and good purification is applicable to large, medium and small type clean water treatment.
Fig. 1 is a structure iron of the present invention.Fig. 1 is described as follows: 1 is housing, and 2 is the pressure-bearing type vortex reactor, and 3 is strainer, and 4 is water-in, and 5 is water outlet, and 6 is slag notch, and 7 is the back taper pipe, and 8 is loam cake.
Be described as follows below in conjunction with Fig. 1: water-in 4 is contained in the lower end side of back taper pipe 7, loam cake 8 is contained in back taper pipe 7 upper ends, space in the logical housing 1 of outlet is arranged between loam cake 8 and the back taper pipe 7, current are entered by the side of back taper pipe 7 bottoms, form from the bottom to top eddy flow and eddy current in the pipe, and flow velocity is by reducing greatly gradually, can realize stepless deceleration, enter space in the housing 1 by vortex reactor 2 outlet outflows, enter strainer 3 then, flow out by water outlet 5 after filtering.
Claims (1)
1, a kind of purifier that pressure-bearing type stepless speed changing vortex reactor is arranged, comprise housing (1), strainer (3), slag notch (6), water-in (4), water outlet (5), it is characterized in that also comprising pressure-bearing type vortex reactor (2), pressure-bearing type vortex reactor (2) comprises back taper pipe (7) and loam cake (8); Pressure-bearing type vortex reactor (2) and strainer (3) are contained in the housing (1), and pressure-bearing type vortex reactor (2) is contained in housing (1) bottom; Loam cake (8) is contained in back taper pipe (7) upper end, and the logical interior space of housing (1) of outlet is arranged therebetween; The interior space of housing (1) is led in strainer (3) import, and outlet picks out the mouth of a river (5); Water-in (4) is connected on the side of back taper pipe (7) lower end, current enter from the side, bottom of back taper pipe (7), in back taper pipe (7), form eddy flow from bottom to up and between eddy flow and tube wall, produce eddy current, flow rate of water flow reduces from bottom to up gradually, flow out by the outlet between back taper pipe (7) and loam cake (8), enter the space in the housing (1), enter strainer (3) then, flow out by water outlet (5) after filtering; Slag notch (6) is contained in the bottom of housing (1), can open in case of necessity, discharges throw out wherein.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 96117681 CN1072188C (en) | 1996-08-24 | 1996-08-24 | Water purifier with pressure-bearing type stepless speed changing vortex reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 96117681 CN1072188C (en) | 1996-08-24 | 1996-08-24 | Water purifier with pressure-bearing type stepless speed changing vortex reactor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1174814A true CN1174814A (en) | 1998-03-04 |
| CN1072188C CN1072188C (en) | 2001-10-03 |
Family
ID=5124511
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 96117681 Expired - Lifetime CN1072188C (en) | 1996-08-24 | 1996-08-24 | Water purifier with pressure-bearing type stepless speed changing vortex reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1072188C (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101596374B (en) * | 2009-06-23 | 2011-05-18 | 中国海洋石油总公司 | Swirling flow reaction inclined tube sedimentation tank |
| CN101734771B (en) * | 2008-11-06 | 2011-07-27 | 北京中天油石油天然气科技有限公司 | Settling separation device and method |
| US9653199B2 (en) | 2012-11-29 | 2017-05-16 | Honeywell International Inc. | Electromagnetic coil assemblies having braided lead wires and/or braided sleeves |
| CN109179765A (en) * | 2018-10-08 | 2019-01-11 | 毛燕婷 | A kind of water process efficient combined-type dirt separator |
-
1996
- 1996-08-24 CN CN 96117681 patent/CN1072188C/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101734771B (en) * | 2008-11-06 | 2011-07-27 | 北京中天油石油天然气科技有限公司 | Settling separation device and method |
| CN101596374B (en) * | 2009-06-23 | 2011-05-18 | 中国海洋石油总公司 | Swirling flow reaction inclined tube sedimentation tank |
| US9653199B2 (en) | 2012-11-29 | 2017-05-16 | Honeywell International Inc. | Electromagnetic coil assemblies having braided lead wires and/or braided sleeves |
| CN109179765A (en) * | 2018-10-08 | 2019-01-11 | 毛燕婷 | A kind of water process efficient combined-type dirt separator |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1072188C (en) | 2001-10-03 |
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| C14 | Grant of patent or utility model | ||
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| ASS | Succession or assignment of patent right |
Owner name: YATAI WATER INDUSTRY SCIENCE + TECH CO LTD, CHONGQ Free format text: FORMER OWNER: CHONGQING YATAI ENVIRONMENTAL PROTECTION ENGINEERING TECHNOLOGY DESIGN RESEARCH INSTITUTE CO., LTD. Effective date: 20110725 |
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| C41 | Transfer of patent application or patent right or utility model | ||
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Owner name: CHONGQING YA TAI ENVIRONMENTAL PROTECTION ENGINEER Free format text: FORMER NAME: YATAI ENVIRONMENT PROTECTION TECH. INST. Owner name: CHONGQING YATAI ENVIRONMENTAL PROTECTION ENGINEERI Free format text: FORMER NAME: CHONGQING YA TAI ENVIRONMENTAL PROTECTION ENGINEERING TECHNOLOGY DESIGN + RESEAR |
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| CP03 | Change of name, title or address |
Address after: 470 No. 401147 Chongqing Yubei District City Longxi Turquoise Avenue Patentee after: CHONGQING YATAI ENVIRONMENTAL PROTECTION ENGINEERING TECHNOLOGY DESIGN RESEARCH INSTITUTE Co.,Ltd. Address before: 401147, No. 40 Pine Bridge Road, Longxi Town, Chongqing, Yubei District Patentee before: Chongqing Asia Pacific Environmental Protection Engineering Technology Design Institute Address after: 401147, No. 40 Pine Bridge Road, Longxi Town, Chongqing, Yubei District Patentee after: Chongqing Asia Pacific Environmental Protection Engineering Technology Design Institute Address before: 631147 No. 40 Pine Bridge Road, Jiangbei District, Sichuan, Chongqing, China Patentee before: YATAI ENVIRONMENTAL PROTECTION |
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| TR01 | Transfer of patent right |
Effective date of registration: 20110725 Address after: 470 No. 401147 Chongqing Yubei District City Longxi Turquoise Avenue Patentee after: CHONGQING YATAI WATER INDUSTRIAL TECHNOLOGY CO.,LTD. Address before: 470 No. 401147 Chongqing Yubei District City Longxi Turquoise Avenue Patentee before: CHONGQING YATAI ENVIRONMENTAL PROTECTION ENGINEERING TECHNOLOGY DESIGN RESEARCH INSTITUTE Co.,Ltd. |
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| CX01 | Expiry of patent term |
Granted publication date: 20011003 |
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