CN202427365U - Integrated fluoride and arsenic removing safe water dispensing equipment - Google Patents

Integrated fluoride and arsenic removing safe water dispensing equipment Download PDF

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Publication number
CN202427365U
CN202427365U CN2012200202090U CN201220020209U CN202427365U CN 202427365 U CN202427365 U CN 202427365U CN 2012200202090 U CN2012200202090 U CN 2012200202090U CN 201220020209 U CN201220020209 U CN 201220020209U CN 202427365 U CN202427365 U CN 202427365U
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CN
China
Prior art keywords
water
reverse osmosis
well pump
integrated
deep well
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN2012200202090U
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Chinese (zh)
Inventor
赵义峰
罗琴
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
WUHAN HUAKE TIANYUAN WATER ENGINEERING Co Ltd
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WUHAN HUAKE TIANYUAN WATER ENGINEERING Co Ltd
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Publication date
Application filed by WUHAN HUAKE TIANYUAN WATER ENGINEERING Co Ltd filed Critical WUHAN HUAKE TIANYUAN WATER ENGINEERING Co Ltd
Priority to CN2012200202090U priority Critical patent/CN202427365U/en
Application granted granted Critical
Publication of CN202427365U publication Critical patent/CN202427365U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model relates to integrated fluoride and arsenic removing safe water dispensing equipment, which comprises a deep-well pump (2), wherein a water inlet end of the deep-well pump (2) is connected with one end of a fiber cotton membrane pipe (3), while the other end of the fiber cotton membrane pipe (3) is connected with a water inlet (7); a water outlet end of the deep-well pump (2) is connected with a reverse osmosis chamber (6); a reverse osmosis membrane (1) is arranged between the water outlet end of the deep-well pump (2) in the reverse osmosis chamber (6) and a water outlet (8) of drinking water; and the reverse osmosis chamber (6) is provided with the water outlet (8) of the drinking water. With the adoption of the fiber cotton membrane pipe and the reverse osmosis membrane, filtration of drinking water is realized under the effect of the deep-well pump, so that harmful ions such as fluoride ions, arsenic ions and the like can be filtered. The water quality after filtration is stable. The integrated fluoride and arsenic removing safe water dispensing equipment is compact in structure, small in occupied area and convenient in operation and can be appropriate for demand of vast rural areas and is strong in adaptability to fluoride and arsenic contents in inflow; and secondary pollution cannot be generated.

Description

Integrated defluorination arsenic removal safty of drinking water equipment
Technical field
The utility model relates to a kind of drinking equipment, relates in particular to a kind of integrated defluorination arsenic removal safty of drinking water equipment, belongs to the purifier technical field.
Background technology
The fluorine ion that contains in the underground water, arsenic ion are harmful substance, be higher than the water of 1-1.5mg/L when the long-term drinking fluorinated volume after, suffer from the spot tooth disease easily, when fluorinated volume is higher than 4mg/L in the water, can cause fluorosis of bone.Existing defluorination filter adopts activated alumina to work as the purpose that under the situation of pH value 6-7, realizes the water body defluorination as Ion Exchange Medium through regulating water PH value more.The weak point that existing level exists is: water inlet fluorine content requirement is had restriction, and it is unstable water outlet situation effluent quality not up to standard when changing appears in water body fluorine content, will to occur.And equipment volume is bigger, and operation is very complicated, can not join with vast rural area reality level, and regenerated liquid has secondary pollution.
Like Chinese patent publication number: CN2046034U; Open day: the utility model patent on October 18th, 1989 disclosed a kind of family expenses and has removed the fluororesin filter water fountain, it is characterized in that having a nontoxic overall plastic or metal inside and outside, core structure housing up and down; Last annular space is the Al2O3 defluoridation filter material; The bottom cone is a complex micro-mineral water immersing lixiviation agent, and two parts separate through quill annular filter plate up and down, and quill annular filter plate central upper suspension low pressure superelevation polyethylene tubular type is filtered core; Top outer is equipped with water inlet pipe and feeds in the defluoridation filter material, and top center is equipped with outlet pipe through screw thread and communicates with the tubular type filter core.But this apparatus structure is complicated, and volume is bigger, and inconvenient operation can not adapt to the demand in vast rural area, and is relatively poor to the content adaptability of water inlet fluorine, arsenic simultaneously, and is easy to generate for the second time and pollutes.
Summary of the invention
The purpose of the utility model is that volume is bigger, inconvenient operation to existing defluorination drinking-water filter plant complex structure; Filter effect is not good, and the defective of easy generation of secondary pollution and deficiency provide a kind of simple in structure; It is little to take up room; Easy to operate, good filtration effect can not produce the integrated defluorination arsenic removal safty of drinking water equipment of secondary pollution.
For realizing above-mentioned purpose; The technical solution of the utility model is: integrated defluorination arsenic removal safty of drinking water equipment, comprise deep well pump, and the water inlet end of said deep well pump is connected with an end of cellucotton film pipe; The other end of cellucotton film pipe is a water inlet; The water side of deep well pump is connected with reverse osmosis cell, and reverse osmosis cell is interior and between deep well pump water side and drinking water delivery port, be provided with reverse osmosis membrane, and reverse osmosis cell is provided with the drinking water delivery port.
Be provided with the underground water delivery port on the outer wall of said reverse osmosis cell and between reverse osmosis membrane and deep well pump water side.
Be filled with fibrage in the pipe of said cellucotton film pipe.
Said deep well pump is connected with controller through the controller connecting line.
The beneficial effect of the utility model is:
1. the utility model has adopted cellucotton film pipe and reverse osmosis membrane, under the effect of deep well pump, has realized the filtration to drinking water, can filter out harmful ions such as fluorine ion in the water, arsenic ion, the water stabilization after the filtration.
2. the utility model compact conformation, it is little to take up room, easy to operate, can adapt to the demand in vast rural area, stronger to the content adaptability of water inlet fluorine, arsenic, and can not produce for the second time and pollute.
Description of drawings
Fig. 1 is the structural representation of the utility model.
Fig. 2 is the structural representation after the utility model is installed.
Among the figure: reverse osmosis membrane 1, deep well pump 2, cellucotton film pipe 3, controller 4, controller connecting line 5, reverse osmosis cell 6, water inlet 7, drinking water delivery port 8, underground water delivery port 9.
The specific embodiment
Below in conjunction with the description of drawings and the specific embodiment the utility model is done further to describe in detail.
Referring to Fig. 1, Fig. 2; The integrated defluorination arsenic removal safty of drinking water equipment of the utility model comprises deep well pump 2, and the water inlet end of said deep well pump 2 is connected with an end of cellucotton film pipe 3; The other end of cellucotton film pipe 3 is a water inlet 7; The water side of deep well pump 2 is connected with reverse osmosis cell 6, and in the reverse osmosis cell 6 and between deep well pump 2 water sides and drinking water delivery port 8, be provided with reverse osmosis membrane 1, reverse osmosis cell 6 is provided with drinking water delivery port 8.
Be provided with underground water delivery port 9 on the outer wall of said reverse osmosis cell 6 and between reverse osmosis membrane 1 and deep well pump 2 water sides.
Be filled with fibrage in the pipe of said cellucotton film pipe 3.
Said deep well pump 2 is connected with controller 4 through controller connecting line 5.
The water inlet end of deep well pump 2 is connected with an end of cellucotton film pipe 3; The other end of cellucotton film pipe 3 is a water inlet 7; Be filled with fibrage in the pipe of cellucotton film pipe 3, cellucotton film pipe 3 is used for water body bulky grain suspension is tackled, and drinking-water is tentatively filtered.The water side of deep well pump 2 is connected with reverse osmosis cell 6, is provided with reverse osmosis membrane 1 in the reverse osmosis cell 6, and reverse osmosis membrane 1 is the domestic type reverse osmosis membrane.Make water pass through reverse osmosis membrane 1 after 2 pairs of water pressurizations of deep well pump, under the effect of reverse osmosis membrane 1, can filter out harmful ions such as fluorine ion, arsenic ion, realize filtration water.Reverse osmosis cell 6 is provided with drinking water delivery port 8, and the water after the filtration uses through the tank that pipeline can be delivered directly to man of peasant household.
Be provided with underground water delivery port 9 on the outer wall of reverse osmosis cell 6 and between reverse osmosis membrane 1 and deep well pump 2 water sides, separated dense water can be discharged through underground water delivery port 9, also can be connected to ground through pipeline and supply the not high place of other water quality requirements to use.Deep well pump 2 is connected with controller 4 through controller connecting line 5, the control that can externally realize deep well pump 2 through operation control 4, and control is simple, and vast rural area ordinary person grasps comparatively fast.
The course of work of the utility model is following: during use equipment is immersed among the water body fully; Starting deep well pump 2 back generation negative pressure is incorporated into well water in the cellucotton film pipe 3; Enter into pressurization in the deep well pump 2 after the filtration; Enter into reverse osmosis cell 6 subsequently, and under hydraulic pressure, filter through reverse osmosis membrane 1, the water purification after the processing is flowed out by drinking water delivery port 8.Compact equipment, easy to operate, and can not produce secondary pollution.

Claims (4)

1. integrated defluorination arsenic removal safty of drinking water equipment; Comprise deep well pump (2); It is characterized in that: the water inlet end of said deep well pump (2) is connected with an end of cellucotton film pipe (3); The other end of cellucotton film pipe (3) is water inlet (7); The water side of deep well pump (2) is connected with reverse osmosis cell (6), and in the reverse osmosis cell (6) and be positioned between deep well pump (2) water side and the drinking water delivery port (8) and be provided with reverse osmosis membrane (1), reverse osmosis cell (6) is provided with drinking water delivery port (8).
2. integrated defluorination arsenic removal safty of drinking water equipment according to claim 1 is characterized in that: on the outer wall of said reverse osmosis cell (6) and be positioned between reverse osmosis membrane (1) and deep well pump (2) water side and be provided with underground water delivery port (9).
3. integrated defluorination arsenic removal safty of drinking water equipment according to claim 1 is characterized in that: be filled with fibrage in the pipe of said cellucotton film pipe (3).
4. integrated defluorination arsenic removal safty of drinking water equipment according to claim 1, it is characterized in that: said deep well pump (2) is connected with controller (4) through controller connecting line (5).
CN2012200202090U 2012-01-17 2012-01-17 Integrated fluoride and arsenic removing safe water dispensing equipment Expired - Fee Related CN202427365U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2012200202090U CN202427365U (en) 2012-01-17 2012-01-17 Integrated fluoride and arsenic removing safe water dispensing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2012200202090U CN202427365U (en) 2012-01-17 2012-01-17 Integrated fluoride and arsenic removing safe water dispensing equipment

Publications (1)

Publication Number Publication Date
CN202427365U true CN202427365U (en) 2012-09-12

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN2012200202090U Expired - Fee Related CN202427365U (en) 2012-01-17 2012-01-17 Integrated fluoride and arsenic removing safe water dispensing equipment

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CN (1) CN202427365U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103288179A (en) * 2013-06-27 2013-09-11 江苏省环境科学研究院 Method for improving reverse osmosis defluorination efficiency

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103288179A (en) * 2013-06-27 2013-09-11 江苏省环境科学研究院 Method for improving reverse osmosis defluorination efficiency
CN103288179B (en) * 2013-06-27 2014-08-27 江苏省环境科学研究院 Method for improving reverse osmosis defluorination efficiency

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C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20120912

Termination date: 20180117