KR20150007128A - filter for a water purifier and the water purifier including the same - Google Patents
filter for a water purifier and the water purifier including the same Download PDFInfo
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- KR20150007128A KR20150007128A KR1020130081134A KR20130081134A KR20150007128A KR 20150007128 A KR20150007128 A KR 20150007128A KR 1020130081134 A KR1020130081134 A KR 1020130081134A KR 20130081134 A KR20130081134 A KR 20130081134A KR 20150007128 A KR20150007128 A KR 20150007128A
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- Prior art keywords
- filter
- water
- activated carbon
- iron hydroxide
- synthetic iron
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 329
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 207
- 229910001385 heavy metal Inorganic materials 0.000 claims abstract description 81
- 239000008213 purified water Substances 0.000 claims abstract description 79
- 235000014413 iron hydroxide Nutrition 0.000 claims abstract description 54
- 239000012528 membrane Substances 0.000 claims abstract description 26
- 239000000463 material Substances 0.000 claims abstract description 25
- 239000012510 hollow fiber Substances 0.000 claims abstract description 15
- NCNCGGDMXMBVIA-UHFFFAOYSA-L iron(ii) hydroxide Chemical compound [OH-].[OH-].[Fe+2] NCNCGGDMXMBVIA-UHFFFAOYSA-L 0.000 claims abstract description 12
- 229910006540 α-FeOOH Inorganic materials 0.000 claims abstract 2
- -1 iron hydroxide compound Chemical class 0.000 claims description 81
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 claims description 30
- 238000000034 method Methods 0.000 claims description 22
- 239000011230 binding agent Substances 0.000 claims description 20
- 239000004698 Polyethylene Substances 0.000 claims description 13
- 229920000573 polyethylene Polymers 0.000 claims description 13
- 150000001875 compounds Chemical class 0.000 claims description 8
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N iron oxide Inorganic materials [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 claims description 7
- 229910002588 FeOOH Inorganic materials 0.000 claims description 6
- 238000006243 chemical reaction Methods 0.000 claims description 6
- WKPSFPXMYGFAQW-UHFFFAOYSA-N iron;hydrate Chemical compound O.[Fe] WKPSFPXMYGFAQW-UHFFFAOYSA-N 0.000 claims description 4
- 239000000843 powder Substances 0.000 claims description 4
- 125000000524 functional group Chemical group 0.000 claims description 3
- FIMJSWFMQJGVAM-UHFFFAOYSA-N chloroform;hydrate Chemical compound O.ClC(Cl)Cl FIMJSWFMQJGVAM-UHFFFAOYSA-N 0.000 claims 1
- 229910052799 carbon Inorganic materials 0.000 description 19
- 239000000498 cooling water Substances 0.000 description 18
- 235000013759 synthetic iron oxide Nutrition 0.000 description 17
- 230000000694 effects Effects 0.000 description 14
- 238000009826 distribution Methods 0.000 description 12
- 235000020188 drinking water Nutrition 0.000 description 11
- 239000003651 drinking water Substances 0.000 description 11
- 101100327917 Caenorhabditis elegans chup-1 gene Proteins 0.000 description 9
- 238000001816 cooling Methods 0.000 description 9
- 238000010438 heat treatment Methods 0.000 description 9
- 238000000746 purification Methods 0.000 description 9
- 239000000571 coke Substances 0.000 description 8
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 7
- 230000007423 decrease Effects 0.000 description 6
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 6
- 239000003673 groundwater Substances 0.000 description 5
- 230000001965 increasing effect Effects 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 239000008399 tap water Substances 0.000 description 5
- 235000020679 tap water Nutrition 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000000356 contaminant Substances 0.000 description 3
- 239000013049 sediment Substances 0.000 description 3
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 2
- BUGBHKTXTAQXES-UHFFFAOYSA-N Selenium Chemical compound [Se] BUGBHKTXTAQXES-UHFFFAOYSA-N 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 229910052785 arsenic Inorganic materials 0.000 description 2
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 230000001186 cumulative effect Effects 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 230000007257 malfunction Effects 0.000 description 2
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 2
- 229910052753 mercury Inorganic materials 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 229910052711 selenium Inorganic materials 0.000 description 2
- 239000011669 selenium Substances 0.000 description 2
- 229940126062 Compound A Drugs 0.000 description 1
- NLDMNSXOCDLTTB-UHFFFAOYSA-N Heterophylliin A Natural products O1C2COC(=O)C3=CC(O)=C(O)C(O)=C3C3=C(O)C(O)=C(O)C=C3C(=O)OC2C(OC(=O)C=2C=C(O)C(O)=C(O)C=2)C(O)C1OC(=O)C1=CC(O)=C(O)C(O)=C1 NLDMNSXOCDLTTB-UHFFFAOYSA-N 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 235000013361 beverage Nutrition 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000008094 contradictory effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 238000005429 filling process Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 150000004679 hydroxides Chemical class 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- YOBAEOGBNPPUQV-UHFFFAOYSA-N iron;trihydrate Chemical compound O.O.O.[Fe].[Fe] YOBAEOGBNPPUQV-UHFFFAOYSA-N 0.000 description 1
- 150000002736 metal compounds Chemical class 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- RECVMTHOQWMYFX-UHFFFAOYSA-N oxygen(1+) dihydride Chemical compound [OH2+] RECVMTHOQWMYFX-UHFFFAOYSA-N 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000009827 uniform distribution Methods 0.000 description 1
- 239000012855 volatile organic compound Substances 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D35/00—Filtering devices having features not specifically covered by groups B01D24/00 - B01D33/00, or for applications not specifically covered by groups B01D24/00 - B01D33/00; Auxiliary devices for filtration; Filter housing constructions
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
-
- 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
-
- 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
- C02F1/58—Treatment of water, waste water, or sewage by removing specified dissolved compounds
- C02F1/62—Heavy metal compounds
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Water Treatment By Sorption (AREA)
Abstract
Description
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a filter for a water purifier, and more particularly, to a heavy metal removal filter for a water purifier that can effectively remove heavy metals in water and a water purifier including the same.
A water purifier is a device that purifies raw water such as tap water or ground water. That is, it refers to an apparatus for converting raw water into drinking water through various water purification methods.
In order to generate an integer, it is possible to pass through processes such as precipitation, filtration and sterilization, and it is general that harmful substances are removed through these processes.
In general, the water purifier may be equipped with various filters to purify the raw water. These filters can be classified into a sediment filter, an activated carbon filter, a UF hollow fiber membrane filter, an RO membrane filter or the like according to their functions.
The sediment filter may be a filter for precipitating large contaminants or suspended matters in raw water, and the activated carbon filter may be a filter for adsorbing and removing small contaminants, residual chlorine, volatile organic compounds, and odor generating factors .
Generally, two activated carbon filters may be provided. That is, a pre-activated carbon filter provided on the raw water side and a pre-activated carbon filter provided on the purified water side may be provided. The post-activated carbon filter may be provided to improve the taste of water by removing odor inducing substances that mainly affect the taste of purified water.
Both the UF hollow fiber membrane filter and the RO membrane filter are generally used selectively.
RO membrane filters can be used to effectively remove heavy metals, ionic substances and microorganisms by applying reverse osmosis membranes. However, such RO membrane filters are expensive and have a problem of discarding a large amount of raw water. In addition, there is a problem that minerals and components useful for the human body are also removed.
On the other hand, UF hollow fiber membrane filters can effectively remove ionic substances and microorganisms while maintaining the beneficial minerals in the human body. In addition, it is possible to minimize the raw water that is inexpensive and wasted as compared with the RO membrane filter. For example, only 40% of the raw water flowing into the RO membrane filter can be converted to an integer, and the raw water flowing into the UF hollow fiber membrane filter can be converted to a 100% integer.
However, there is a problem that it is difficult to effectively remove heavy metals through the UF hollow fiber membrane filter. Accordingly, there is a problem that it is difficult to provide a water purifier that can use tap water or ground water in a contaminated area as raw water.
In recent years, demand for water purifiers has increased significantly. Therefore, there are problems that various requirements are generated and it is difficult to satisfy at the same time.
For example, it is possible to remove heavy metals by applying an RO membrane filter, but it is difficult to secure the flow rate of purified water. That is, it takes a very long time to obtain a desired amount of purified water.
On the other hand, UF hollow fiber membrane filter can secure high flow rate, but it is difficult to use tap water in groundwater or contaminated area as raw water because it is difficult to remove heavy metals in water.
Therefore, removal of heavy metals and securing of high flow rate were inevitably regarded as contradictory problems. This is because it is difficult to obtain a high flow rate when RO membrane filter is used to remove heavy metals and heavy metal removal is difficult when UF hollow fiber membrane filter is used to secure high flow rate.
The present invention basically aims to solve the problem of the conventional water purifier described above.
It is an object of the present invention to provide a water purifier having a compact and slim water purifier and a high performance filter.
According to an embodiment of the present invention, there is provided a water purifier filter and a water purifier which can secure a high flow rate and are excellent in the removal of heavy metals in water.
According to one embodiment of the present invention, there is provided a water purifier capable of using tap water or ground water in a contaminated area as raw water.
According to one embodiment of the present invention, there is provided a water purifier capable of securing a high flow rate, removing heavy metals in water, and effectively removing chloroform without changing the structure or piping of a conventional water purifier.
A filter for a water purifier and a water purifier capable of reducing the time and cost required for the manufacturing process through an embodiment of the present invention.
According to one embodiment of the present invention, there is provided a water purifier having a high flow rate and excellent removal of heavy metals.
According to an aspect of the present invention, there is provided a filter device comprising: a filter housing having an inlet and an outlet; And a filter module provided in the filter housing for purifying water supplied through the inlet port to supply the purified water to the outflow port. In order to remove heavy metals in the water, the material of the filter module is a synthetic iron hydroxide (? FeOOH) compound A filter for a water purifier can be provided.
The synthetic iron hydroxide compound is represented by the following formula (1)
(One)
Lt; / RTI > The synthetic iron hydroxide compound is represented by the following formula (2)
(2)
It is preferable to remove the heavy metal (A) in the water through the chemical reaction according to the chemical reaction.
The synthetic iron hydroxide compound may be beoxide
Preferably, the filter module material comprises granular or powdered activated carbon. Therefore, it is possible to effectively remove heavy metals as well as chloroform in water through the filter.
The synthetic iron hydroxide compound is in powder or granular form, and the synthetic iron hydroxide compound and the activated carbon can be filled in the filter module.
The filter module may include a filter block, and the filter block may further include a binder for connecting the synthetic iron hydroxide compound and activated carbon to each other to impart rigidity thereto.
The synthetic hydro iron oxide compound in the filter block is preferably less than 30 wt%, and the activated carbon is preferably 30 wt% or more. Specifically, the synthetic hydro iron oxide compound in the filter block is preferably 10 wt% or more and less than 30 wt%, and the activated carbon is preferably 33 wt% or more and less than 53 wt%.
The binder material is preferably polyethylene. The polyethylene in the filter block is preferably 34 to 40% by weight. More specifically, the polyethylene in the filter block is preferably 37% by weight. Therefore, it is possible to effectively increase the ratio of the synthetic hydro iron oxide compound and the activated carbon associated with the purified water, while effectively performing the binder function.
According to an aspect of the present invention, there is provided a water purifier in which a shear activated carbon filter, a UF hollow fiber membrane filter, and a rear end activated carbon filter are sequentially connected to generate purified water from raw water, As the material of the activated carbon filter, a water purifier including activated carbon for removing chloroform in water and synthetic iron hydroxide (? -FeuOH) compound for removing heavy metals in water may be provided.
Preferably, the water purifier is a direct water type water purifier in which the purified water directly flows out from the external water source. Therefore, it is possible to satisfy the effect of removing heavy metals and at the same time to secure an effective flow rate of purified water.
In the filter material, the weight percentage of the activated carbon and the synthetic iron hydroxide compound is preferably determined in consideration of the flow rate condition and the criteria for the chloroform removal condition.
It is preferable that the weight percentage of the synthetic iron hydroxide compound in the material of the rear end activated carbon filter is determined so as to satisfy a removal rate of 90% or more with respect to mercury, lead, hexavalent chrome, arsenic, selenium, iron and aluminum.
The increase in the weight percentage of the synthetic iron hydroxide compound for heavy metal removal shows a decrease in the purified water flow rate. In addition, the decrease in weight percent of the synthetic iron hydroxide compound indicates a decrease in the heavy metal removal effect. Therefore, in order to sufficiently carry out the heavy metal removal effect, the weight percentage of the synthetic iron hydroxide compound is preferably 10% by weight or more.
The synthetic iron hydroxide compound may be beoxide
The rear end activated carbon filter or the front end activated carbon filter may include a filter housing having an inlet and an outlet; And a filter block provided in the filter housing for supplying purified water to the outlet through the inlet.
Preferably, the filter block is formed in a hollow cylindrical shape and includes the activated carbon and a synthetic iron hydroxide compound. Therefore, the rear end activated carbon filter or the front end activated carbon filter may be a filter for removing heavy metals. Of course, both can be heavy metal removal filters, and either one can be a heavy metal removal filter.
Preferably, the filter block includes a binder that connects the activated carbon and the synthetic iron hydroxide compound to each other to impart rigidity thereto.
The synthetic hydro iron oxide compound in the filter block is preferably less than 30 wt%, and the activated carbon is preferably 30 wt% or more.
Preferably, the material of the binder is polyethylene, and the polyethylene in the filter block is 34 to 40 wt%.
In order to achieve the above object, according to an embodiment of the present invention, there is provided a water purifier in which a shear activated carbon filter, a UF hollow fiber membrane filter, and a rear end activated carbon filter are sequentially connected to generate an integer from raw water, The filter material of the rear end activated carbon filter includes synthetic iron hydroxide (? FeOOH) compound for removal of activated carbon and water heavy metal, and the amount of the synthetic iron hydroxide compound in the rear end activated carbon filter and the amount of the synthetic hydroxy iron compound The water purifier can be provided.
It is preferable that the amount of the synthetic iron hydroxide compound in the rear end activated carbon filter is larger than the amount of the synthetic iron hydroxide in the front end activated carbon filter.
According to an embodiment of the present invention, a water purifier having a high performance filter performance can be provided, while providing a compact and slim water purifier.
According to one embodiment of the present invention, it is possible to provide a filter for a water purifier and a water purifier that can secure a high flow rate and are excellent in heavy metal removal performance in water.
According to an embodiment of the present invention, it is possible to provide a water purifier that can use tap water or ground water in a contaminated area as raw water.
According to one embodiment of the present invention, it is possible to provide a water purifier capable of securing a high flow rate, removing heavy metals in water, and effectively removing chloroform without changing the structure or piping of a conventional water purifier.
According to one embodiment of the present invention, it is possible to provide a filter for a water purifier and a water purifier which can reduce the time and cost required for the manufacturing process.
According to one embodiment of the present invention, it is possible to provide a direct water-type purifier excellent in the removal of heavy metals with high flow rate.
1 is a perspective view illustrating an example of a water purifier according to an embodiment of the present invention;
FIG. 2 is a piping construction diagram showing an example of piping configuration of the water purifier shown in FIG. 1; FIG.
3 is a cross-sectional view of a filter according to one embodiment of the present invention;
FIG. 4 is an example of a conjugate bonding equation showing the principle of heavy metal removal of a heavy metal removal material in the filter of FIG. 3;
FIGS. 5 and 6 are graphs showing the flow rates according to the weight percentages of the heavy metal removal material in the filter of FIG. 3;
FIGS. 7 and 8 are graphs showing the chloroform removal ratio according to the weight percentage of the heavy metal removal material in the filter of FIG. 3; And
9 is a table showing the effect of removing heavy metals in the filter of Fig.
Hereinafter, a filter for a water purifier and a water purifier according to an embodiment of the present invention will be described in detail with reference to the accompanying drawings.
1 shows an example of a water purifier which can be applied to the embodiment of the present invention.
The
The
Specifically, the user lifts the cup 1 so that the upper portion of the cup 1 is positioned below the
The user can drink the water stored in the cup 1 and throw the remaining water into the
As described above, the drinking water may be either purified water, cold water or hot water. Of course, it may be various forms of beverage. Accordingly, a
For example, the user may select cold water through the
As described above, the general drinking water supply device is provided such that drinking water is supplied by a user's operation such as the operation of the
Hereinafter, an example of the piping configuration of the above-described water purifier described with reference to Fig. 2 will be described.
As shown in FIG. 2, the raw water flowing into the
Specifically, the
A constant flow valve (21) may be provided between the external water supply (20) and the front end of the filter (30). The amount of raw water (flow rate) can be supplied to the
The purified water generated by the raw water can be discharged to the outside through the purified
Here, the purified
The
As described above, the water purifier can basically be an apparatus for generating and supplying an integer. However, it may be provided to supply cold water or hot water as well as an integer for user satisfaction. Such cold water or hot water can basically be generated using the above constants. That is, the cold water or the hot water may be an integer, and may additionally be an integer which is cooled or heated.
On the other hand, the water purifier may be a device for supplying only cold water or hot water using an integer. In this case, it is possible to omit piping configurations at the downstream end of the branch point C in the purified
As shown in FIG. 2, according to the embodiment of the present invention, a water purifier capable of supplying cold water can be provided. That is, it is possible to provide a water purifier capable of generating cold water by cooling the purified water and capable of leaving the cold water.
In order to generate cold water through the purified water, a
The cold water pipe (50) may be branched from the purified water pipe (40). At this time, the
The purified water bypassed from the purified
The
On the other hand, in order to prevent freezing of the
A cooling water pipe 80 for supplying cooling water to the inside of the cold water tank may be provided. Through the cooling water pipe 80, cold water or purified water can be supplied as cooling water to the cold water tank.
The cooling water pipe 80 may be provided with a cooling water valve 81. When cooling water is required, the cooling water valve 81 may be opened to allow the cooling water to flow into the water
Meanwhile, the
When the user presses the lever to exit the cold water, cold water is discharged from the
FIG. 2 shows an embodiment in which cold water and purified water are discharged through a
The
More specifically, the
Accordingly, the
Accordingly, cold water or purified water can be supplied to the
Further, in this embodiment, it is possible to provide a water purifier capable of generating hot water using an integer and supplying hot water. A
As shown in FIG. 2, the
The purified water supplied from the purified
Therefore, the hot water can be taken out to the outside as the hot
In this embodiment, it is possible to provide a water purifier capable of selectively leaving purified water, hot water and cold water through a single
As described above, only the constants can be supplied through the purifier according to the present embodiment. In addition, a water purifier supplied with only cold water and hot water can be provided. In addition, a water purifier supplied with only cold water and purified water may be provided.
However, as shown in FIG. 2, it is most preferable to provide a water purifier capable of selectively supplying cold water, hot water, and purified water through the water purifier according to the present embodiment. This is because it can meet various user demands.
On the other hand, as described above, various forms of heading can be performed through the single
For example, the user may select the cold water mode via the
In the above description of the piping, the branch may be a branch of the pipe or the flow path itself, and may include a branch through a fitting.
Hereinafter, a filter for a water purifier according to an embodiment of the present invention will be described in detail with reference to FIG. For convenience of explanation, the case where the filter is the
As shown, the
The filter (33) may comprise a housing (34, 35). That is, it may include a housing forming an internal space. Therefore, the
Specifically, the
More specifically, the inlet (36) and the outlet (37) may be provided in the cover (33). Therefore, it is very easy to mount and replace the filter due to the position of the inlet and outlet, assuming that the filter must be replaced periodically.
The purified water flowing into the housings (34, 35) is purified while passing through the filter module (38). In other words, harmful substances contained in water or raw water can be removed through the
According to the present embodiment, it is possible to provide a heavy metal removal filter for a water purifier excellent in the removal effect of heavy metals in water and a water purifier including the same. For this purpose, it is preferable that the material of the filter module includes a synthetic iron hydroxide (? FeOOH) compound.
The filter module is preferably a filter module in which water is penetrated by a pressure difference between a front end and a rear end. This means that the purified water flowing into the housing can be discharged to the outside of the housing through the
The synthetic iron hydroxide (? - FeOOH) compound may contain a functional group represented by the following formula (1).
(One)
That is, a plurality of Fe may ionically bond with a hydroxyl group (OH), and each Fe (Fe) may include a functional group ionically or covalently bonded to one oxygen (O).
As an example of such a synthetic iron hydroxide compound, trade
The synthetic iron hydroxide compound can remove heavy metals in water through a chemical reaction formula represented by the following formula (2).
(2)
Here, A means a heavy metal, and the heavy metal is dissolved in water in the form of a water-soluble compound.
Through the chemical reaction between the water-soluble heavy metal compound and the synthetic iron hydroxide compound, water and hydroxide ion are generated. In addition, the heavy metal A has a strong ionic or covalent bond with the synthetic iron hydroxide compound. Therefore, the removed heavy metal can be prevented from again dissolving in water. The purified water from which the heavy metal is removed through the filter module flows out of the filter housings (34, 35) through the outlet (37).
As shown in FIG. 9, according to this embodiment, it can be seen that there is an excellent heavy metal removal effect. When the performance criterion of heavy metal removal rate is 90%, the performance is satisfied in all seven heavy metals.
That is, it can be seen that a removal rate of at least 94% can be achieved even when the concentration of heavy metals is different for mercury, lead, hexavalent chrome, arsenic, selenium, iron and aluminum.
This heavy metal removal effect is very effective. This is because, as will be described later, a sufficient flow rate of purified water can be ensured and at the same time, this heavy metal removal effect can be achieved. Thus, it is possible to effectively remove heavy metals while achieving a sufficient purified flow rate that can not be expected in conventional RO membrane filters.
The synthetic iron oxide compound may be formed in the form of a granule or a powder and may be filled in the
On the other hand, in general, the water purifier filter configuration includes a free (front end)
Increasing the number of filters means that the improvement of the water purification performance can be expected, but the flow rate of the purified water is reduced. Thus, it may not be desirable for the above-described filter for heavy metal removal to be further added to a general filter configuration.
Also, existing water purifiers have limited space in which the filter arrangement can be located, so adding a new filter may not be easy.
Similarly, it is not preferable to omit the conventional filter, for example, the UF hollow
In order to solve such a problem, a heavy metal removal filter as a carbon filter may be provided in this embodiment. This makes it possible to satisfy the filter configuration of the basic water purifier and to prevent the decrease in the flow rate of the purified water due to the increase in the number of filters. In addition, not only the heavy metal removal effect but also the inherent functions and effects as a carbon filter can be expected.
Specifically, either the free (shear) carbon filter or the post (rear end) carbon filter may be a heavy metal removal filter. Of course, both can be heavy metal removal filters. In other words, in this embodiment, a heavy metal removal filter based on a carbon filter and a water purifier including the same can be provided. However, for the sake of convenience, a post-carbon filter as a heavy metal removal filter will be described.
For this purpose, it is preferable that the material of the
The synthetic iron oxide compound and the activated carbon may be uniformly mixed with each other and then filled into the filter module or the filter housing. However, such a filling operation requires a lot of working time and can not be said to be an easy task. Therefore, it is preferable that the filter module is formed in a block shape and positioned inside the housing (34, 35). That is, it may be desirable to form the
In particular, the
Accordingly, after the entire filter block is inserted into the
On the other hand, the
3, the purified water flowing from the circumferential surface of the
As described above, it has been explained through the embodiment of the present invention that a heavy metal removal effect, a sufficient water flow rate, and a function of a free carbon filter can be secured.
However, it can be said that it is very difficult to produce a filter block having rigidity through a synthetic iron oxide compound and activated carbon. Therefore, it is preferable that the material of the filter module includes a binder which connects the synthetic iron oxide compound and activated carbon to each other to give rigidity. Here, the binder may function to make the filter module become one rigid body rather than improving the water purification performance.
On the other hand, the weight percentages of the materials of the
For example, an increase in weight percent of the synthetic iron oxide compound means a decrease in the flow rate of purified water, which means a reduction in weight% of the activated carbon. This reduction in the weight% of activated carbon means that the performance of the free carbon filter is reduced, and in particular, the removal performance of chloroform (CHCL 3 ) is lowered. Therefore, it is preferable that the weight percentages of the synthetic iron oxide compound and the activated carbon are determined in consideration of the criteria for the constant flow rate condition and the chloroform removal condition.
On the other hand, the range of the weight percentage of the binder which imparts stiffness to the
Therefore, according to this embodiment, the weight percentage of the binder is 34 to 40 wt%, preferably 37 wt%. Such a binder may be polyethylene.
Hereinafter, when the weight% of the binder is substantially 37%, the water flow rate and chloroform removal performance according to the weight percentage change of synthetic iron oxide and activated carbon will be described.
5 and 6 are graphs showing the flow rate of purified water according to the weight% of the synthetic iron oxide compound. As shown in FIG. 5, when the weight percentage of the synthetic iron oxide compound is small, the purified water flow rate is satisfactory. However, it can be seen that the flow rate is reduced to less than 1.5 L / min when the cumulative flow rate reaches 30% by weight and reaches 3500 L. As shown in FIG. 6, when the synthetic iron oxide compound is 50% by weight, the purified water flow rate becomes smaller as the purified water flow rate is substantially less than 0.9 L / min and the cumulative flow rate increases.
Therefore, it is preferable that the synthetic iron oxide compound is less than 30% by weight through FIG. 5 and FIG. In addition, the synthetic iron oxide compound is preferably 10% by weight or more in order to provide sufficient heavy metal removal effect.
7 and 8 are graphs showing the chloroform removal performance according to the weight% of activated carbon.
As shown in FIG. 7, when the weight percentage of activated carbon is 30% by weight, it is understood that the removal standard is 80% even when the chloroform removal rate is 3000L. However, it can be seen that the removal rate gradually approaches 80%. Of course, when the weight percentage of activated carbon is smaller than 30, the chloroform removal performance will be further lowered. Therefore, it can be seen from FIG. 6 that the weight percentage of activated carbon is preferably more than 30%.
As shown in FIG. 8, when the weight percentage of activated carbon increases to 50, the chloroform removal performance is further increased.
As shown in FIGS. 5 to 8, the synthetic iron hydroxide compound is preferably less than 30% by weight in consideration of securing the flow rate of purified water, and preferably 30% by weight or more, more preferably 33% by weight or more, More desirable. In order to secure the removal of heavy metals, it is preferable that the synthetic iron hydroxide compound is 10 wt% or more.
Therefore, it becomes possible to simultaneously remove the heavy metal, secure the flow rate of the purified water, and remove the chloroform through the composition ratio (% by weight) of the synthetic iron hydroxide compound, the activated carbon and the binder.
In addition, it is possible to provide a filter having a filter block shape, which is very easy to manufacture and handle, and a water purifier including the same.
On the other hand, the filter block can be formed by mixing the above-mentioned materials uniformly and then heating them in a mold. By heating in the mold, the binder, for example polyethylene, is melted and the synthetic hydroxy iron chemistry and activated carbon are bound to the polyethylene. Therefore, a filter block having overall rigidity can be formed.
In the above-described embodiments, the synthetic iron hydroxide compound for heavy metal removal is basically included in the rear end activated carbon filter. Of course, the synthetic iron hydroxide compound may be included in the shear activated carbon filter or both.
The shear activated carbon filter is provided at the front end of the rear end activated carbon filter to remove contaminants of relatively large particles. Therefore, the replacement cycle of the shear activated carbon filter is generally faster than the replacement cycle of the rear end activated carbon filter.
In addition, as described above, it can be seen that the flow rate of the purified water decreases as the weight percentage of the synthetic iron hydroxide compound in the rear end activated carbon filter is increased. Therefore, there is a limit to increase the weight percentage of the synthetic iron hydroxide compound in one filter for effective removal of heavy metals.
In this embodiment, it is possible to provide a water purifier in which the synthetic iron hydroxide compound is applied to both the shear activated carbon filter and the post-stage activated carbon filter, taking into consideration that the activated carbon filter and the activated carbon filter use activated carbon as a raw material.
Therefore, the amount of the synthetic iron hydroxide compound in any one specific filter can be reduced while increasing the amount of the synthetic iron hydroxide compound in the entire filter portion. Therefore, it is possible to secure an effective flow rate of the purified water and to remove heavy metals. That is, the amounts of the synthetic iron hydroxide compounds can be the same or different from each other.
On the other hand, in consideration of the replacement period of the filter, and the inherent functions of the front end activated carbon filter and the rear end activated carbon filter, it may be preferable to make the amounts of the synthetic iron hydroxide compounds different from each other. For example, the amount of the synthetic iron hydroxide compound in the shear activated carbon filter may be preferably less than the amount of the synthetic hydroxy iron compound in the rear end activated carbon filter. This is because, in general, the replacement cycle of the shear activated carbon filter is relatively short.
Therefore, it is possible to additionally remove heavy metals in addition to the inherent purification function in the shear activated carbon filter. In addition, since the amount of the synthetic iron hydroxide compound is relatively small, the flow rate of purified water can be secured. Similarly, heavy metal removal can be effectively performed together with the inherent purification function of improving the water taste in the rear end activated carbon filter. In addition, since the heavy metal is partially removed from the shear activated carbon filter, effective heavy metal removal is possible even if the amount of the synthetic iron hydroxide compound is relatively small.
As a result, it is possible to secure the flow rate of purified water and effectively remove heavy metals by applying both effective and unnecessary synthetic hydroxides to both the front and rear activated carbon filters. Of course, inherent integer functions can also be performed effectively.
30: filter 31: free carbon filter
32: UF filter 33: Post carbon filter (heavy metal removal filter)
Claims (22)
And a filter module provided in the filter housing for supplying purified water to the outlet through the inlet,
In order to remove heavy metals in water, the material of the filter module includes a synthetic iron hydroxide (? FeOOH) compound.
The synthetic iron hydroxide compound is represented by the following formula (1)
(One)
And the functional group of the water purifier.
The synthetic iron hydroxide compound is represented by the following formula (2)
(2)
Wherein the heavy metal (A) in the water is removed through a chemical reaction according to the chemical reaction.
Wherein the synthetic iron hydroxide compound is beoxide E 33.
Characterized in that, in order to remove water chloroform, the filter module comprises granular or powdered activated carbon.
Wherein the synthetic iron hydroxide compound is in powder or granular form, and the synthetic iron hydroxide compound and the activated carbon are filled in the filter module.
Wherein the filter module includes a filter block, and the filter block further comprises a binder for connecting the synthetic iron hydroxide compound and activated carbon to each other to impart rigidity thereto.
Wherein the synthetic hydro iron oxide compound in the filter block is less than 30 wt%, and the activated carbon is not less than 30 wt%.
Wherein the synthetic hydro iron oxide compound in the filter block is 10 wt% or more and less than 30 wt%, and the activated carbon is 33 wt% or more and less than 53 wt%.
Wherein the binder material is polyethylene.
Wherein the polyethylene in the filter block is 34 to 40 wt%.
Wherein the polyethylene in the filter block is 37 wt.%.
Wherein the filter material of at least one of the shear activated carbon filter or the rear end activated carbon filter includes activated carbon for removing chloroform in water and synthetic hydroxy iron (α-FeOOH) compound for removing heavy metals in water.
Wherein the water purifier is a direct water type water purifier in which the purified water is directly taken out by directly using the water pressure of the external water source.
Wherein the synthetic iron hydroxide compound is beoxide E 33.
Wherein the shear activated carbon filter or the post-
A filter housing having an inlet and an outlet; And
And a filter block provided in the filter housing for supplying purified water to the outlet through the inlet.
Wherein the filter block is formed in a hollow cylindrical shape, and comprises the activated carbon and the synthetic iron hydroxide compound.
Wherein the filter block includes a binder that connects the activated carbon and the synthetic iron hydroxide compound to each other to impart rigidity thereto.
Wherein the synthetic hydro iron oxide compound in the filter block is less than 30 wt%, and the activated carbon is not less than 30 wt%.
Wherein the material of the binder is polyethylene, and the polyethylene in the filter block is 34 to 40 wt%.
Wherein the filter material of the front end activated carbon filter and the rear end activated carbon filter includes a synthetic iron hydroxide (? FeOOH) compound for removing activated carbon and heavy metals in water, and the amount of the synthetic iron hydroxide compound in the rear end activated carbon filter Wherein the amounts of the synthetic iron hydroxide compounds are different from each other.
Wherein the amount of the synthetic iron hydroxide compound in the rear end activated carbon filter is larger than the amount of the synthetic iron hydroxide compound in the front end activated carbon filter.
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
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WO2018106031A1 (en) * | 2016-12-06 | 2018-06-14 | 엘지전자 주식회사 | Water purifier filter, and water purifier comprising same |
KR20190090655A (en) * | 2018-01-25 | 2019-08-02 | 엘지전자 주식회사 | filter for water purifier and water purifier using thereof |
KR20210127105A (en) * | 2020-04-13 | 2021-10-21 | 폴 코포레이션 | Adapter for filter device and method of use |
CN114763279A (en) * | 2021-01-13 | 2022-07-19 | Lg电子株式会社 | Filter module for drinking device |
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2013
- 2013-07-10 KR KR1020130081134A patent/KR20150007128A/en active Search and Examination
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
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WO2018106031A1 (en) * | 2016-12-06 | 2018-06-14 | 엘지전자 주식회사 | Water purifier filter, and water purifier comprising same |
KR20180064841A (en) * | 2016-12-06 | 2018-06-15 | 엘지전자 주식회사 | filter for water purifier and water purifier using thereof |
US20190389740A1 (en) * | 2016-12-06 | 2019-12-26 | Lg Electronics Inc. | Water purifier filter, and water purifier comprising same |
US11731884B2 (en) | 2016-12-06 | 2023-08-22 | Lg Electronics Inc. | Water purifier filter, and water purifier comprising same |
KR20190090655A (en) * | 2018-01-25 | 2019-08-02 | 엘지전자 주식회사 | filter for water purifier and water purifier using thereof |
KR20210127105A (en) * | 2020-04-13 | 2021-10-21 | 폴 코포레이션 | Adapter for filter device and method of use |
CN114763279A (en) * | 2021-01-13 | 2022-07-19 | Lg电子株式会社 | Filter module for drinking device |
CN114763279B (en) * | 2021-01-13 | 2023-11-28 | Lg电子株式会社 | Filter module for drinking device |
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