TW201942066A - Filter cartridge and water purification system using the same including a carrying seat and a filter - Google Patents

Abstract

The present invention provides a filter cartridge, which is used for purifying water and for producing a biological water composition containing silicic acid and hydrogen, and includes a carrying seat and a filter material. The carrying seat defines an accommodating space and is provided with a water inlet and a water outlet communicating with the accommodating space. The filter material is filled in the accommodating space of the carrying seat, and includes a vehicle and a plurality of active silicon materials adsorbed on one surface of the vehicle. The vehicle is selected from a porous material, a non-porous material, or a combination of the foregoing. The present invention also provides a water purification system using the aforementioned filter cartridge.

Description

Filter and water purification system using the same

The present invention relates to a filter, in particular to a filter for purifying water and producing a water for organism containing silicic acid and hydrogen, and a water purification system using the same. .

In view of the fact that hydrogen-soluble drinking water is beneficial for neutralizing pathogenic reactive oxygen species or free radical groups existing in the body after drinking in order to reduce organ damage. Therefore, research on hydrogen-soluble drinking water has become a hot research topic in recent years.

Most of the common hydrogen-dissolved drinking water in the interview is mostly dissolved high-purity hydrogen directly in water, or magnesium powder or magnesium ingot to react with pure water to generate hydrogen, which is called hydrogen-dissolved drinking water. However, the former method has problems such as difficulty in obtaining high-purity hydrogen, difficulty in dissolving hydrogen, and safety. The latter method is because magnesium hydroxide remaining in pure water is classified as a drug, which conflicts with some cardiovascular diseases. Once the content is too high, it can easily cause acute drug poisoning and acute renal failure. Or hypermagnesemia.

It can be known from the above description that making drinking water soluble in hydrogen and providing safe hydrogen-dissolved drinking water is a subject to be solved by those skilled in the technical field related to the present invention.

Therefore, a first object of the present invention is to provide a filter for purifying water and producing biological water containing silicic acid and hydrogen.

Therefore, the filter core of the present invention is used for purifying water and producing biological water containing silicic acid and hydrogen. The filter core includes a carrier and a filter material. The carrier defines an accommodation space, and includes a water inlet and a water outlet that communicate with the accommodation space. The filter material is filled in the accommodation space of the carrier, and the filter material includes a carrier and a plurality of active silicon materials. The support is selected from a porous material, a non-porous material, or a combination of the foregoing supports. The active silicon materials are adsorbed on a surface of the carrier.

A second object of the present invention is to provide a water purification system for producing biological water containing silicic acid and hydrogen.

Therefore, the water purification system of the present invention is used to connect with a biological water unit that produces and contains a biological water and produces biological water containing silicic acid and hydrogen. The water purification system includes at least one along a water flow direction. The first filter. The first filter is a filter as described above.

The effect of the present invention is that the active silicon material formed on the surface of the carrier reacts with biological water to generate silicic acid and hydrogen, which increases the amount of hydrogen dissolved in biological water and provides a safe composition of biological water, and contains beneficial solubility for the human body. Silicon.

Before the present invention is described in detail, it should be noted that in the following description, similar elements are represented by the same numbers.

Referring to FIG. 1 and FIG. 2, a first embodiment of the filter 4 of the present invention is used for purifying water and producing a biological water composition 92 (see FIG. 13) containing silicic acid and hydrogen 921, which includes a carrier. 41, and a filter material 42.

The carrier 41 defines an accommodating space 40, and includes an inlet 401 and an outlet 402 which are oppositely disposed and communicate with the accommodating space 40. The position of the inlet 401 is lower than the outlet 402. position.

The filter material 42 of the filter core 4 is filled in the accommodation space 40 of the carrier 41, and includes a carrier 421 and a plurality of active silicon materials 422. The support 421 is selected from a porous material, a non-porous material, or a combination of the foregoing supports 421. The active silicon materials 422 are adsorbed on a surface of the carrier 421.

In the present invention, the so-called biological water is defined as water that can be absorbed by organisms after being taken orally or externally by organisms such as animals and plants, and silicic acid and hydrogen bubbles 921 are biological water as shown in FIG. 13. 9 is formed by mixing with a predetermined amount of active silicon material 422.

The purpose of the carrier 421 is mainly to intercept the active silicon materials 422, and any material that can intercept the active silicon materials 422 is applicable. Therefore, preferably, the carrier 421 suitable for the present invention is selected from the group consisting of activated carbon 4211 shown in FIG. 2, and hollow fiber membrane filter 4212 shown in FIG. 5. Bamboo-charcoal, porphyritic andesites, quartz sand, fibers, ceramics, and a combination of the aforementioned carriers 421; the active silicon material 422 is selected from a particle size Nano silicon, porous silicon, granulated silicon, or Si nanowires between 50 nm and 300 nm. For example, nano-silicon materials can be waste materials such as nano-silicon powder that is discarded after squaring and slicing of silicon ingots in silicon wafer growth plants; porous The silicon material can be materials such as silicon wafers, silicon powder, etc. after acid etching; the granulated silicon material can be, for example, silicon powder obtained by spray granulation; silicon nanowires can be, for example, silicon material subjected to solution etching Income.

What needs to be explained here is that nano-based silicon materials (ie, nano-silicon materials) are highly active in nature, which facilitates rapid reaction with water molecules to generate silicic acid and hydrogen. It needs to be further explained that, generally, the smaller the particle size of the nano-silica material, the greater the activity, the faster the reaction rate between the nano-silica material and the biological water9, and the rate of reaction to generate silicic acid and hydrogen is also faster. Faster. In order to prevent the active silicon material 422 from reacting with the biological water 9 violently and quickly due to its too small particle size, it is preferable that the surface of the nano silicon material has a silicon oxide film.

As shown in FIG. 2, the first filter material 42 of the filter core 4 of the first embodiment of the present invention, the carrier 421 is activated carbon 4211 with a plurality of micropores 4210 distributed on the surface, and the active silicon materials 422 are granules. Nano-silicon materials with a diameter between 100 nm and 250 nm, and the active silicon materials 422 adsorbed on the surface of the support 421 are partially located in the micropores 4210 of the activated carbon 4211.

Preferably, based on the weight percentage of the filter material 42, the content of the carrier 421 is 90% by weight or less, and the content of the active silicon materials 422 is 10% by weight or more. More preferably, the content of the active silicon material 422 is between 10 wt% and 40 wt%, and even more preferably, the content of the active silicon material 422 is between 15 wt% and 30 wt% (that is, the active silicon material The content of the silicon material 422 is more than 20 wt%, and the content of the carrier 421 is less than 80 wt%), so that the filter material 42 can be more compatible with the production of the filtration and biological water composition 92. It should be noted that the higher the content of the active silicon material 422, the less the required carrier 421 to achieve the designed hydrogen and silicon dissolving amount. Therefore, in other embodiments, the active silicon material 422 can also be used as the filter material 42 alone. In other words, the activated silicon material 422 does not have to be used with a carrier 421 such as activated carbon 4211.

Referring to FIG. 3, the first method for manufacturing the first filter material 42 of the filter core 4 according to the first embodiment of the present invention is to add a solvent (for example, alcohol 4222) and these active silicon materials (for example, alcohol 4222) to a container having a stirring function. : Nano-silicon slurry 4220 formed by nano-silicon material) 422, and activated carbon 4211 is mixed into the nano-silicon slurry 4220 and stirred uniformly, so that the active silicon material 422 can pass through the nano-silicon. The turbulence caused by the slurry 4220 while being stirred is embedded in the micropores 4210 of the activated carbon 4211 to be adsorbed on the surface of the activated carbon 4211. After the activated carbon 4211 is uniformly stirred to the nano-silica slurry 4220 and dried to remove the alcohol 4222, the first filter material 42 of the first embodiment shown in FIG. 2 is prepared.

Referring to FIG. 4, a second filter medium 42 of the filter core 4 according to the first embodiment of the present invention is substantially the same as the first filter medium 42. The difference is that the second filter medium 42 further includes a bonding agent.材 (binder) 423. The bonding material 423 combines nano silicon material (ie, activated silicon material 422) and activated carbon 4211 to partially attach the activated silicon material 422 to the activated carbon 4211, and the bonding material 423 and activated carbon 4211 together form a sintered activated carbon ( sintered activated carbon). In detail, the second filter material 42 is a mixture of activated carbon 4211, nanometer silicon material (ie, active silicon material 422) and bonding material 423, and then hot-pressed through a mold to form a green body. Finally, the green embryo is sintered to form the filter material 42. In other embodiments, the first filter material 42 of the first embodiment may be mixed with the bonding material 423 and then pressed and sintered. It is worth mentioning that the sintered bonding material 423 will form a plurality of channels (not shown) for biological water to flow through.

Referring to FIG. 5, a third filter medium 42 of the filter core 4 according to the first embodiment of the present invention is substantially the same as the first filter medium 42 except that the carrier 421 has a tubular structure and The hollow fiber membrane 4212 has micro-holes 4210 passing through its tubular structure, and the pore diameter of the micro-holes 4210 is between 10 nm and 100 nm. The active silicon materials (for example, nano-silicon materials) 422 are adsorbed on the surface of each hollow fiber membrane 4212. The method for manufacturing the third filter medium 42 of the filter core 4 of the first embodiment of the present invention is to mix the active silicon materials 422 in a fluid (not shown) so that the active silicon materials 422 pass through the fluid. The first direction is guided to the surface of each hollow fiber membrane 4212 and adsorbed on the surface of each hollow fiber membrane 4212, and the fluid flows into the micro-holes 4210 along the flow direction to an exit of each hollow fiber membrane 4212 (Not shown) proceed. Of course, in other derivative embodiments, the active silicon material 422 can also be fixed on the hollow fiber membrane 4212 without a fluid-permeable means, for example, fixed through an adhesive material, or active silicon is added during the manufacturing process of the hollow fiber membrane 4212.材 422.

The filter core 4 of the first embodiment of the present invention further includes a dispersed water flow unit and a blocking unit.

The dispersed water flow unit is located in the accommodation space 40 of the carrier 41 and is adjacent to the water inlet 401, and the blocking unit is located in the accommodation space 40 of the carrier 41 and near the water outlet 402. In the filter core 4 of the first embodiment of the present invention, the carrier 421 is activated carbon 4211 uniformly distributed in the accommodating space 40 of the carrier 41, and the active silicon materials 422 are nano silicon materials; In other words, the filter element 4 of the first embodiment uses the first filter material 42 and is filled in the accommodation space 40 of the carrier 41.

It is worth mentioning here that the first filter material 42 used in the filter core 4 of the first embodiment of the present invention can be used for biological water because of the active silicon material 422 embedded in the micro-holes 4210. (Not shown) When reacting with these active silicon materials 422 to generate hydrogen (not shown) and silicic acid, the bio-water dissolved hydrogen is composed of micropores 4210 and flows more in the filter material 42. Contact area to increase the amount of dissolved hydrogen. In addition, the position of the water inlet 401 is lower than the position of the water outlet 402, which helps to slow down the active silicon material 422 being washed away by biological water, and can also increase the amount of dissolved hydrogen.

In addition, it should be noted that, in addition to the filter element 4 of the first embodiment disclosed in FIG. 1 of the present invention, in addition to the first filter material 42 described above, in other derivative embodiments, it can also be used alone in this embodiment. The accommodating space 40 of the carrier 41 is filled with the active silicon material 422 as the filter material 42, so that the biological water composition containing silicic acid and hydrogen can also be produced.

The filter core 4 of the first embodiment of the present invention shown in FIG. 1 can use the first filter material 42 directly, and can also be used from its water inlet 401 in the accommodation space 40 of the carrier 41 before use. A part of the carrier 421 (for example, activated carbon 4211), the activated silicon materials 422, and the remaining carrier 421 (for example, activated carbon 4211) are sequentially filled toward the water outlet 402 thereof. When the biological water 9 shown in FIG. 13 is introduced from the water inlet 401 of the carrier 41 in actual use, the biological water may be dispersed by the activated carbon 421 adjacent to the water inlet 401 to facilitate the biological water Substantially fill the accommodating space 40 and make the active silicon materials 422 move with the biological water flow direction to adhere to the carrier 421, and the remaining activated carbon 4211 near the water outlet 402 can reduce the impact of water volume and Block active silicon 422. Therefore, in the filter core 4 of the first embodiment of the present invention, the carrier 421 located in the accommodating space 40 of the carrier 41 and adjacent to the water inlet 401 is used as the dispersed water flow unit. The carrier 421 in the accommodation space 40 of the carrier 41 and adjacent to the water outlet 402 serves as the blocking unit.

The purpose of the dispersed water flow unit is to prevent the water flow direction from being concentrated at the water inlet 401 and to evenly disperse biological water into the accommodation space 40 of the carrier 41. Therefore, the dispersed water flow unit suitable for the present invention is not limited to the above-mentioned activated carbon 4211, and any glass beads, a partition with holes, or a non-woven fabric having a function of dispersing water flow can be applied. In addition, the purpose of the blocking unit is to stop the active silicon material 422 to reduce the probability that the active silicon material 422 is taken out of the accommodating space 40 from the water outlet 402 by the biological water flow direction. Therefore, the barrier unit applicable to the present invention is not limited to the above-mentioned activated carbon 4211. For example, bamboo charcoal, maifan stone, hollow silk membrane, fiber or quartz sand that can block the activated silicon material 422 adjacent to the water outlet 402 are also all applicable.

It is also worth mentioning that the biological water introduced into the containing space 40 of the filter core 4 can also react with other filter materials that can release trace elements (such as potassium, strontium, selenium) and / or minerals to When biological water reacts with active silicon 422 to generate silicic acid and hydrogen, trace elements are released into the composition of biological water.

Referring to FIG. 6, a second embodiment of a filter element 4 of the present invention is substantially the same as the first embodiment, except that the filter material 42 is a second filter material 42 described in the first embodiment. . It is worth mentioning that combining activated carbon 4211 and activated silicon material 422 through the bonding material 423 of the filter material 42 enables the activated silicon material 422 to be more effectively attached / fixed to the activated carbon 4211 to prevent the filter core from In actual use, the active silicon material 422 is washed by biological water and taken to the water outlet 402 of the carrier 41.

Referring to FIGS. 7 and 8, a third embodiment of the filter 4 of the present invention is substantially the same as the first embodiment, except that the carrier 421 is a combination of activated carbon 4211 and hollow fiber membrane 4212, and the activities The silicon material 422 is a nano silicon material; that is, the filter core 4 of the third embodiment of the present invention uses the third filter material of the first embodiment in addition to the third filter material of the first embodiment. Filter medium 42. In the filter 4 of the third embodiment of the present invention, the activated carbon 4211 is evenly distributed in the accommodation space 40 of the carrier 41 and is close to the water inlet 401 relative to the hollow fiber membrane 4212; the hollow fiber membrane 4212 is distributed In the accommodating space 40 of the carrier 41, the water outlet 402 is close to the activated carbon 4211.

In detail, in addition to the filter element 4 of the third embodiment of the present invention, in addition to the first and third filter materials 42 described above, it can also be used before the use (see FIG. 7). In the installation space 40, a part of the carrier 421 (for example, activated carbon 4211), the activated silicon materials 422, the remaining activated carbon 4211, and the hollow fiber membranes 4212 are sequentially filled from its water inlet 401 to its water outlet 402. Referring again to FIG. 8, when the biological water (not shown) is introduced from the water inlet 401 of the carrier 41 in actual use, the biological water may substantially fill the accommodating space 40 and make the biological water according to its own flow direction. The isoactive silicon material 422 moves with the flow direction of biological water. The partially moved active silicon material 422 can be embedded in the micro-holes 4210 of the activated carbon 4211, so that the micro-holes 4210 can make the biological water with hydrogen dissolved therein have more contact area when flowing in the filter material 42. In order to increase the amount of dissolved hydrogen, the active silicon material 422 that is not embedded in the micropores 4210 can still be taken to the hollow fiber membrane 4212 along with the flow direction of biological water to be adsorbed on the surface of the hollow fiber membrane 4212, so that The composition of biological water in the hollow fiber membrane 4212 continues to react with the active silicon material 422, and an aeration effect occurs there to further increase the amount of dissolved hydrogen. In addition, the hollow fiber membrane 4212 can also intercept possible silicic acid polymerization or precipitation, so that the silicic acid polymerization or precipitation due to supersaturation can be reduced by the biological water that is continuously introduced into the accommodation space 40 of the filter 4 The concentration of silicic acid in biological water continues to dissolve. In brief, the filter core 4 of the third embodiment of the present invention is an integrated filter core.

Referring to FIG. 9, a fourth embodiment of the filter element 4 of the present invention is substantially the same as the third embodiment (also an integrated filter element), except that the filter material 42 is different from the filter element 4 of the present invention. The arrangement relationship in the accommodation space 40 of the carrier 41. Similarly, the carrier 421 is a combination of activated carbon 4211 and hollow fiber membrane 4212, and the activated silicon materials 422 are nano-silicon materials. Activated carbon 4211 is evenly distributed in the accommodation space 40 of the carrier 41 and is close to the water inlet 401 relative to the hollow fiber membrane 4212. The hollow fiber membrane 4212 is located in the accommodation space 40 of the carrier 41 to surround The activated carbon 4211 is close to the water outlet 402 relative to the activated carbon 4211.

In detail, in the filter core 4 of the fourth embodiment of the present invention, the accommodation space 40 is filled with the first filter material 42 of the first embodiment (that is, the activated silicon material 422 is embedded in activated carbon). 4211), and the third filter material 42 of the first embodiment (that is, the active silicon material 422 is adsorbed on the surface of the hollow fiber membranes 4212) surrounds the first of the first embodiment Kind of filter material 42.

Fig. 9 shows a state after use. Similarly, when the filter core 4 of the fourth embodiment of the present invention is used, the arrangement relationship between the activated carbon 4211 and the active silicon material 422 in the accommodating space 40 is similar to that of the first or third embodiment. Therefore, when the filter 4 of the fourth embodiment is actually used to input the biological water (not shown) from the water inlet 401 of the carrier 41, the active silicon materials 422 can also flow with the biological water. Flow through activated carbon 4211 and hollow fiber membrane 4212 to increase the amount of dissolved hydrogen. Details will not be repeated here.

Referring to FIG. 10, a fifth embodiment of the filter element 4 of the present invention is substantially the same as the fourth embodiment (also an integrated filter element), except that the filter material 42 is different from the filter element 4 of the present invention. The arrangement relationship in the accommodation space 40 of the carrier 41 and the arrangement relationship between the water inlet 401 and the water outlet 402. Similarly, the carrier 421 is a combination of activated carbon 4211 and hollow fiber membrane 4212, and the activated silicon materials 422 are nano-silicon materials. In the filter core 4 of the fifth embodiment of the present invention, the water inlet 401 and the water outlet 402 are located on the same side of the carrier 41, and the hollow fiber membrane 4212 is located in the accommodation space 40 of the carrier 41. The relatively activated carbon 4211 is close to the water outlet 402; the activated carbon 4211 is located in the accommodation space 40 of the carrier 41 to surround the hollow fiber membrane 4212, and is relatively close to the water inlet 401 relative to the hollow fiber membrane 4212. In other words, the hollow fiber membrane 4212 is disposed in the center of the accommodating space 40, and the activated carbon 4211 and the active silicon material 422 are disposed around the hollow fiber membrane 4212.

When the filter 4 of the fifth embodiment of the present invention is actually used, the biological water (not shown) is first introduced from the water inlet 401 and flows along the flow direction of the biological water through the surface adsorbed on the activated carbon 4211. The active silicon material 422 reacts with the active silicon material 422 to generate silicic acid and hydrogen, so that after the biological water composed of silicic acid and hydrogen is formed, it is then passed through the micropores of the hollow fiber membrane 4212 along the flow direction of the biological water composition 4210 flows into the hollow fiber membrane 4212 to flow out to the water outlet 402. Among them, the active silicon material 422 can also be taken to the hollow fiber membrane 4212 along with the flow direction of the biological water to be adsorbed on the surface of the hollow fiber membrane 4212.

It is worth mentioning that the water inlet 401 and the water outlet 402 of the filter core 4 in the first to fourth embodiments described above may also be disposed on the same side of the carrier 41 in other embodiments.

Referring to FIG. 11, a sixth embodiment of the filter element 4 of the present invention is substantially the same as the third embodiment, except that the filter element 4 of the sixth embodiment further includes a detachable switch member 43, And the detailed structure of the carrier 41 and the arrangement relationship of the filter material 42.

In detail, the carrier 41 includes a first member 411 and a second member 412 disposed at intervals from each other. The first component 411 and the second component 412 respectively include the water inlet 401 and the water outlet 402, and each component 411, 412 has an interface section 4111, 4121; wherein the interface sections 4111, 4121 face each other and Communicate. The detachable switch member 43 is connected between the first member 411 and the second member 412, and the accommodation space 40 of the carrier 41 is formed by the first member 411, the second member 412, and the detachable switch. The components 43 are collectively defined. Similarly, the carrier 421 is a combination of activated carbon 4211 and hollow fiber membrane 4212, and the activated silicon materials 422 are nano-silicon materials, the activated carbon 4211 is located in the first part 411 of the carrier 41, and the hollow fiber The film 4212 is located in the second member 412 of the carrier 41. In other words, the first filter material 42 of the first embodiment [that is, the active silicon material (such as nano-silicon material) 422 embedded in the micro holes 4210 of the activated carbon 4211] is filled in the first In the component 411, the third filter material 42 of the first embodiment [that is, the active silicon material 422 (such as nanometer silicon material) is adsorbed on the surface of the hollow fiber membranes 4212] is filled in the second component 412 Inside.

In the filter element 4 of the sixth embodiment of the present invention, the detachable switch member 43 is a rotary connection assembly, and the interface section 4111 of the first component 411 and the interface section 4121 of the second component 412 of the carrier 41 An external thread 4112, 4122 and an annular groove 4113, 4123 facing each other are formed correspondingly. The rotary connection assembly includes a through-hole nut 431 formed with an internal thread 4310, and two elastic outer leakage rings 432. The nut 431 has an upper ring groove 4311 and a lower ring groove 4312 which are recessed in opposite directions, and the outer leakage rings 432 are respectively disposed in the upper ring groove 4311 and the lower ring groove 4312. Specifically, the ring grooves 4113 and 4123 of the first member 411 and the second member 412 of the carrier 41 of the sixth embodiment of the present invention are disposed facing each other so as to pass through one of the ring grooves 4113 and 4123 provided in the ring grooves 4113 and 4123. The inner leakage rings 44 are arranged at intervals, and are screwed to the external threads 4112, 4122 of these parts 411, 412 through the internal threads 4310 of the through-hole nuts 431 provided with the external leakage rings 432, thereby defining The accommodating space 40 of the carrier 41 is sealed, and the accommodating space 40 is sealed to avoid leakage of biological water (not shown) in the accommodating space 40.

Although the filter core 4 of the sixth embodiment of the present invention implements the detachable switch member 43 in the form of the rotary connection assembly, in other embodiments, the rotary connection assembly can also be replaced with other The known detachable switch member uses, for example, a non-rotating snap connection using a latch structure.

The state shown in FIG. 11 is that the biological water has not been input into the second part 412 of the carrier 41. Once the filter 4 of the sixth embodiment is actually used, the active silicon materials 422 can also be taken into the second member 412 to be adsorbed to the hollow fiber membranes along with the flow direction of the biological water. 4212 surface.

In addition, it should be added that the filter element 4 of the sixth embodiment of the present invention is a separable filter element. Simply put, when the active silicon material 422 filled in the filter material 42 of the first embodiment in the first component 411 can no longer react with the biological water to generate silicic acid and hydrogen, it only needs to be loosened. Open the through-hole nut 431 of the rotary connection assembly to separate the first member 411 and the second member 412, and replace the filter material 42 inside the first member 411, and then pass through the through-hole nut of the rotary connection assembly 431 engages the interface sections 4111, 4121 of the first component 411 and the second component 412 to reuse the filter core 4 of the sixth embodiment, thereby achieving the purpose of saving costs.

12 and FIG. 13, a first embodiment of the water purification system (or biological water production system) of the present invention is used to connect to a biological water unit 2 produced and containing the biological water 9. The biological water composition 92 containing silicic acid (not shown) and hydrogen bubbles 921 is produced, and the water purification system includes at least one first filter element 4 along a water flow direction F, and optionally includes a filter element having at least one A pipeline unit 7, a degassing unit 3, at least a second filter element 5, and / or an ultraviolet light sterilization unit 6 of a conveying pipeline 72 extending along the water flow direction F; wherein the first filter element 4 The filter element 4 according to any one of the first to sixth embodiments is used. The biological water unit 2 includes a water inlet 201 and a water outlet 202. The equipment suitable as the biological water unit 2 may be a commercially available reverse osmosis (hereinafter referred to as R.O.) pure water machine or other water purification equipment. Of course, it is also possible to directly use natural water, groundwater and other biological water without filtering treatment. Specifically, the water purification system of the present invention can produce the biological water composition 92 under a suitable condition (for example, an R.O. pure water machine is used as the biological water unit 2), and only a single first filter 4 is required.

The degassing unit 3 included selectively is disposed at an upstream position of the first filter element 4 along the flowing water direction, and is sequentially connected to the degassing along the flowing water direction by the pipeline 72 of the pipeline unit 7 The unit is connected to the first filter element 4 and is used to remove the gas in the water. Specifically, the degassing unit 3 includes a carrier 31 defining an accommodation space 30, and a degassing member 32 filled in the accommodation space 30. The degassing unit 3 is used to remove dissolved gases, such as carbon dioxide (CO ₂ ), oxygen (O ₂ ), and nitrogen (N ₂ ), which are originally dissolved in the biological water 9, so as to improve the first The amount of hydrogen dissolved in the biological water 9 in the filter 4. The degassing unit 3 suitable for the water purification system in this embodiment of the present invention may be a membrane-type air extractor (Filter-type Air Extractor), or other filters capable of adsorbing gas.

The second filter element 5 included in the selectivity is disposed at a downstream position of the first filter element 4 along the water flow direction F in an implementation state that does not include the degassing unit 3, and includes a boundary The accommodating space 51 of the accommodating space 50 and a plurality of porous materials 52 filled in the accommodating space 50 of the accommodating space 51. The carrier 51 of the second filter core 5 has a water inlet 501 and a water outlet 502 which are oppositely arranged and communicate with the accommodating space 50. The porous material 52 in the second filter element 5 is selected from activated carbon 521, hollow fiber membrane 522, or a combination of the foregoing porous materials 52. The conveying pipeline 72 of the pipeline unit 7 is sequentially connected to the first filter element 4 and the second filter element 5 along the water flow direction F.

The selective ultraviolet light sterilization unit 6 is provided at a downstream position of the first filter element 4 along the water flow direction F in the state where the deaeration unit 3 and the second filter element 5 are not included. The ultraviolet light sterilization unit 6 is used to sequentially connect the first filter element 4 and the ultraviolet light sterilization unit 6 along the water flow direction F through the transportation pipe 72 of the pipeline unit 7 and is used to sterilize the biological water composition 92 . Specifically, the ultraviolet sterilization unit 6 includes a carrier 61 defining an accommodation space 60 and an ultraviolet light group 62. The carrier 61 has a water inlet 601 and a water outlet 602 that are oppositely connected to the receiving space 60. In other embodiments, a structural state in which an ultraviolet lamp post (not shown) is axially disposed in the accommodating space 60 may also be adopted.

In the water purification system according to the first embodiment of the present invention, a biological water composition 92 containing silicic acid (not shown) and hydrogen bubbles 921 is connected to the biological water unit 2 through a water inlet pipe 71, and a biological water composition 92 is produced. To send the biological water composition 92 through a water outlet pipe 73; wherein the water purification system of the first embodiment includes the degassing unit 3, the first filter 4, and the second along the water flow direction F in this order. The number of filter cores 5 and the ultraviolet light sterilization unit 6 and the number of transport lines 72 of the pipeline unit 7 are five; the number of the first filter cores 4 is two, and they are used as in the first embodiment The number of the filter elements 4 is one; the number of the second filter elements 5 is one, and the second filter element 5 is placed in an upright position. The porous material 52 in the second filter element 5 is a hollow fiber membrane 522.

In other words, the water inlet pipe 71 is connected to the water inlet 201 of the biological water unit 2; the delivery pipes 72 are sequentially connected along the water flow direction F to the water outlet 202 of the biological water unit 2 and the deaeration unit 3 Water inlet 301, water outlet 302 of the degassing unit 3, water inlet 401 of the first filter element 4 located upstream, water outlet 402 of the first filter element 4 located upstream, and the first filter element downstream The water inlet 401 of 4, the water outlet 402 of the first filter 4 and the water inlet 501 of the second filter 5 located downstream, and the water outlet 502 of the second filter 5 and the ultraviolet sterilization unit 6 The water inlet 601; and the water outlet pipe 73 is a water outlet 602 connected to the ultraviolet light sterilization unit 6.

It should be added that, based on the biological water composition 92 itself and its movement in the direction F of the flowing water, a disturbance phenomenon will be generated in essence. However, this disturbance phenomenon will gradually accumulate gas in the biological water composition 92 to affect the fluid flow. Therefore, the purpose of placing the second filter element 5 in an upright position is to allow the hollow fiber membrane 5212 in the receiving space 50 of the carrier 51 of the second filter element 5 to be placed vertically in the receiving space 50 so that The gas accumulated in the accommodating space 50 of the seat 51 of the second filter core 5 is easily discharged from its water outlet 502 and flows to the delivery pipe 72 communicating with the water outlet 502.

Referring again to FIG. 12 and FIG. 13, the method for manufacturing the biological water composition 92 is implemented by using the water purification system of the first embodiment of the present invention, which includes the following steps: inputting the biological water from the water inlet 301 of the degassing unit 3 The biological water 9 produced by the unit 2 is used to remove the CO ₂ , O ₂ and N ₂ in the biological water 9, and the biological water 9 from which the foregoing gas has been removed flows from the water outlet 302 of the degassing unit 3. Through the pipeline unit 7 to the first filter core 4 located upstream; the biological water 9 is input from the water inlet 401 of the first filter core 4 located upstream so that the biological water 9 flows through the water flow direction F The filter material 42 reacts with the active silicon material 422 of the filter material 42 to generate silicic acid and hydrogen, thereby dissolving silicic acid and hydrogen bubbles 921 in the biological water 9, and the biological water 9, silicic acid, hydrogen bubbles 921 and A part of the biological water composition 92 of the active silicon material 422 flows from the water outlet 402 of the first filter core 4 located upstream to the delivery pipe 72 (see FIG. 13) of the pipeline unit 7 to the first filter core located downstream. 4; input the biological water composition 9 from the water inlet 401 of the first filter 4 located downstream 2. The biological water composition 92 and the active silicon material 422 located in the first filter element 4 downstream continue to react to generate silicic acid and hydrogen bubbles 921, thereby increasing the amount of hydrogen dissolved in the biological water composition 92, and The water outlet 402 of the first filter 4 located downstream flows through the pipeline unit 7 to the second filter 5; the biological water composition 92 is input from the water inlet 501 of the second filter 5 to make the organism The water composition 92 flows through the hollow fiber membranes 522 of the second filter element 5 along the water flow direction F and partially or completely filters the part of the active silicon material 422 in the biological water composition 92, and allows the partial or total filtration The biological water composition 92 flows from the water outlet 502 of the second filter 5 through the pipeline unit 7 to the ultraviolet light sterilization unit 6; and the biological water composition 92 is input from the water inlet 601 of the ultraviolet light sterilization unit 6 In the accommodating space 60, the biological water composition 92 is sterilized through the ultraviolet light group 62 to further pass the water outlet pipe 73 to make the biological water composition 92 from the water outlet 602 of the ultraviolet light sterilization unit 6. The biological water composition 92 is output.

It is worth mentioning that the number of the first filter element 4 can be changed. The more the first filter element 4 is, the lower the ORP value is usually. In addition, if the downstream first filter element 4 adopts the filter element 4 with a hollow fiber membrane 4212 in FIGS. 8 to 11, the second filter element 5 can be selectively omitted.

14 and FIG. 15, a second embodiment of the water purification system of the present invention is substantially the same as the first embodiment, except that the water purification system of the second embodiment further includes a discharge unit 74 And two total dissolved solids (referred to as TDS) measurement unit 75, and the water purification system of the second embodiment does not include the degassing unit 3, the number of the first filter element 4 is one, the first The number of the two filter elements 5 is plural, and the contents in the accommodating spaces 50 of the second filter elements 5 are different from the second filter elements 5 of the first embodiment. In the water purification system according to the second embodiment of the present invention, the number of the conveying pipes 72 of the pipeline unit 7 is four, and the number of the second filters 5 is two, which are filled in the second filters. The porous material 52 in the accommodating space 50 of the carrier 51 of 5 is sequentially the activated carbon 521 and the hollow fiber membrane 522 along the water flow direction F (that is, the carrier 51 of the second filter element 5 located at the upstream position). The accommodating space 50 is filled with activated carbon 521, the accommodating space 50 of the carrier 51 of the second filter 5 located at the downstream position is filled with hollow fiber membrane 522), and the second filter is located at the upstream position 5 also includes nanosilver 53 filled in its accommodation space 50.

The discharge unit 74 is disposed behind the second filter element 5 on the pipeline unit 7 and located at a downstream position along the water flow direction F. Specifically, the discharge unit 74 is a pressure relief valve on a transmission line 72 provided between the water outlet 502 of the second filter core 5 connected to the downstream position and the water inlet 601 of the ultraviolet light sterilization unit 6 ( valve) to communicate with the delivery pipe 72 of the pipe unit 7 and to discharge liquid, gas, or a combination of liquid and gas. It should be added that the process of introducing the biological water 9 into the filters 4 and 5 along the flowing water direction F will continuously accumulate gas due to itself and the turbulence generated by it, such that The pressure value in the delivery pipe 72 is too high, which affects the liquid flow. Therefore, the discharge unit (ie, the pressure relief valve) 74 in the water purification system of the second embodiment is mainly intended to exclude the pressure value of the fluid in the conveying pipes 72 due to the accumulation of excessive gas, so as to This increases the liquid flow.

The total dissolved solid measurement units 75 are respectively disposed at an upstream position and a downstream position of the first filter element 4 along the water flow direction F. Specifically, the total dissolved solids measuring unit 75 located at an upstream position is disposed on a conveying pipe 72 connecting the water outlet 202 of the biological water unit 2 and the water inlet 401 of the first filter 4. The total dissolved solids measuring unit 75 located at the downstream position is a conveying pipe provided between the water outlet 502 of the second filter 5 and the water inlet 601 of the ultraviolet sterilization unit 6 connected to the downstream position. It is located on the road 72 and is located downstream of the exclusion unit 74 along the water flow direction F. It should be noted that the total dissolved solids amount (hereinafter referred to as V _t ) measured by the total dissolved solids measurement unit 75 at the downstream position will be greater than the total dissolved solids measurement at the upstream position. The total dissolved solids amount (hereinafter referred to as V ₀ ) measured by the unit 75 will have a total dissolved solids difference (ΔV) therebetween. Therefore, the purpose of adding the total dissolved solids measurement unit 75 in the water purification system of the second embodiment of the present invention is to use the total dissolved solids measurement unit 75 to obtain the total dissolved solids difference (Δ V). Once the total dissolved solids difference (ΔV) is less than a predetermined value set by the user, it means that the amount of dissolvable silicic acid and hydrogen bubbles 921 in the biological water composition 92 has gradually decreased. The requirement of the filter material 42 of the filter core 4.

Referring to FIG. 16, a third embodiment of a water purification system of the present invention is substantially the same as the second embodiment, except that the water purification system of the third embodiment further includes a flow meter 76, and the The discharge unit 74 is disposed on the pipeline unit 7 and is located between the first filter element 4 and the second filter elements 5. The flow meter 76 is disposed upstream of the first filter element 4 along the water flow direction F.

Specifically, the drain unit 74 of the water purification system according to the third embodiment of the present invention is disposed between the water outlet 502 of the second filter element 5 located at the upstream position and the inlet of the second filter element 5 located at the downstream position. The water inlet 501 of the second filter element 5 located on the transmission line 72 between the water outlets 501 and located at the upstream position is lower than the water outlet 502 thereof, and the water inlet 501 of the second filter core 5 located at the downstream position is high于 出 出 水口 502。 In its water outlet 502. It should be noted that, in the water purification system of the third embodiment of the present invention, the discharge unit (vent valve) 74 is disposed in front of the water inlet 501 of the second filter 5 at a downstream position, and the water inlet 501 is higher than The purpose of the water outlet 502 is to improve the exhaust effect and make the gas in the accommodation space 50 of the filter core 5 at the downstream position easier to go up and down to facilitate the discharge of the gas and reduce the accumulated gas.

In addition, in the water purification system according to the third embodiment of the present invention, the flow meter 76 is a transmission line 72 provided between the water outlet 202 of the biological water unit 2 and the water inlet 401 of the first filter 4. Up, and located upstream of the total dissolved solids measuring unit 75 at the upstream position along the water flow direction F. It should be noted here that when the discharge unit 74 at the downstream position does not open the vent valve in time to discharge the accumulated gas, or the filter elements 4 and 5 are blocked, the flow meter 76 located at the upstream detects The water flow speed will drop from the initial 0.9 ~ 2 L / min to about 0.4 L / min, which will seriously affect the speed and quality of the water composition 92 (such as bacteria growth and taste changes). Therefore, the purpose of adding the flow meter 76 to the water purification system of the third embodiment of the present invention is to use the discharge unit 74 to remove the gas accumulated in the conveying pipe 72 in a timely manner when the water flow speed decreases, and / or to match The difference between the total dissolved solids (ΔV) and the use time of the filters 4 and 5 is used to inform the user to replace the filters 4 and 5.

<Specific Example 1 of Biological Water Composition and Production Method>

One of the specific examples 1 of the biological water composition 92 of the present invention and its preparation method is to use the filter 4 of the second embodiment described above [that is, the filter 4 shown in FIG. 6, and the bonding material 423 is combined with an active silicon material (such as nanometer). (Silicon material) 422 and activated carbon 4211, so that part of the activated silicon material 422 is attached to the activated carbon 4211], the filter material 42 in its filter core 4, the biological water produced by the filter core 4 and its biological water The composition method is briefly explained below.

Referring again to FIG. 6, drinking water is introduced from the water inlet 401 of the filter 4, and the drinking water is reacted with the active silicon material 422 in the filter material 42 to generate silicic acid (not shown) and hydrogen, so that silicon is dissolved. The biological water composition 92 of the acid and hydrogen bubbles 921 (see FIG. 13), and the biological water composition of the specific example 1 is caused to flow out from the water outlet 402. In the specific example 1 of the present invention, the specifications and provenance of the active silicon material 422 are nano silicon materials each having a purity and a particle size D50 of 99.35% and about 200 nm, and the nano silicon material is ground to a purity of 9N. The activated carbon 4211 is a coconut shell activated carbon purchased from Goldstar Carbon Technology Co., Ltd., and the particle size of the activated carbon is between 150 and 380 μm. The bonding material 423 is purchased from Tinoca and the model is GUR2122. Ultra high molecular weight polyethylene (PE).

The silicic acid concentration and ORP value of the composition 92 of biological water produced by the production method of the specific example 1 of the present invention are obtained by analyzing the redox potential of the electrode of model EO221 produced by JAQUA and the redox potential analysis produced by Horiba. (ORP), and the silicic acid concentration was measured by Merck colorimetric drugs, and the analysis results are summarized in Table 1 below.

Table 1.

＜ Specific example of the first filter material and its manufacturing method ＞

One specific example of the first filter material of the present invention and the manufacturing method thereof is implemented according to the method of manufacturing the first filter material of the filter core of the first embodiment. The source and specifications of the nano-silicon material used are the same as those described above. Example 1, and the source and specification of the activated carbon is Haycarb's type RWAP 10742 activated carbon (particle size is between 1.7 mm and 0.425 mm, hereinafter referred to as HB activated carbon). The detailed production conditions of the specific example of the first filter medium are described below.

First, add 80 g of nano-silicon material and 99.5% purity alcohol in a stirrer to uniformly stir into a nano-silicon slurry with a solid content of 20%. Then, 270 g of activated carbon is added to the nano-silicon slurry and uniformly stirred, so that the nano-silicon material in the nano-silicon slurry can be embedded in the micropores of the activated carbon. Finally, the alcohol in the nano-silica slurry is dried and removed, so as to obtain the first filter material of the specific example. Based on the weight percentage of the first filter material in this specific example, the activated carbon and the nano-silica material were 77.1 wt% and 22.9 wt%, respectively.

<Specific examples of the filter and its manufacturing method>

Referring again to FIG. 1, a specific example of the filter of the present invention is implemented according to the filter 4 of the first embodiment described above. The source and specifications of the nano-silicon material used are the same as those of the first filter material and its manufacturing method. Specific examples. The detailed manufacturing conditions of the filter of this specific example are explained below.

First, a water outlet of a carrier of the filter core of this specific example of the present invention is sequentially filled with 50 g of activated carbon (bottom layer) and 100 g of nano-silicon material (middle section) in a containing space. And 230 g of activated carbon (upper layer) as the filter material of the specific example; wherein, based on the weight percentage of the filter material of the specific example, the content of the activated carbon and the nano-silica material were each 73.7 wt. % And 26.3 wt%. Then, a delivery pipe is connected to a water inlet and a water outlet of the carrier, respectively. Finally, the drinking water is input from the water inlet of the carrier into the accommodating space, so that the drinking water drives the nano-silicon material to flow around in a direction of the water outlet, so that the nano-silicon material can be embedded into the micro-particles of activated carbon. Inside the hole; when the drinking water is input into the accommodating space to contact the nano-silicon material, the nano-silicon material embedded in the micro-holes of the activated carbon is simultaneously reacted to generate silicic acid and hydrogen It is beneficial to increase the amount of dissolved hydrogen, and the reason for the increase in the amount of dissolved hydrogen has been described in the detailed description of the foregoing invention, and will not be repeated here.

<Specific Example 2 of Biological Water Composition and Production Method>

One specific example 2 of the composition of biological water of the present invention and its preparation method is implemented using the water purification system of the first embodiment); in other words, the composition of biological water of specific example 2 of the present invention and the two methods used in its preparation method The first filter element is implemented according to the method for manufacturing the filter element of the specific example described above; among them, the source and specifications of the nanometer silicon material used in the specific example 2 are also the same as those of the first filter element and its Specific examples of manufacturing methods. The detailed production conditions of the biological water composition and the production method of the specific example 2 of the present invention are described below.

First, drinking water is produced from an R.O. pure water machine of 400P model produced by ADD, so that the drinking water flows from a water outlet of the R.O. pure water machine through a pipeline unit to a membrane deaerator.

Next, the drinking water is input from a water inlet of the membrane degasser to remove CO ₂ , O ₂ and N ₂ in the drinking water, and the drinking water from which the foregoing gas has been removed is removed from the membrane degasser. A water outlet flows through the pipeline unit to the first filter core at an upstream position.

Next, the drinking water is input from an inlet of the first filter element at an upstream position, so that the drinking water flows through its filter material along a direction of water flow and reacts with the nano-silicon material of the filter material to generate silicic acid and hydrogen. So that silicic acid and hydrogen are dissolved in the drinking water, and a biological water containing the drinking water, silicic acid, hydrogen and a part of nano-silicon material is composed, and a part of the first filter element located at an upstream position is formed. The water outlet flows through a conveying pipeline of the pipeline unit to a first filter element located at a downstream position, and further inputs the biological water composition into a water inlet of the first filter element at a downstream position, so that the organism The water composition and the nano-silicon material in the first filter element at the downstream position continue to react to generate silicic acid and hydrogen to thereby increase the amount of dissolved hydrogen, and flow through a water outlet of the first filter element at the downstream position. The pipeline unit is connected to a second filter element.

Subsequently, the biological water composition is input from a water inlet of the second filter element so that the biological water composition flows through the second filter element through a hollow fiber membrane (purchased from SAMPO, and the model number is FJ-V1203BL). ), And partially or completely filter the part of the nano-silica material in the biological water composition, and make the partially or completely filtered biological water composition flow from an outlet of the second filter core through the pipeline unit to a Ultraviolet sterilizer (purchased from KC-FLOW, and the model is 16W-2GPM).

Finally, the biological water composition is input from a water inlet of the ultraviolet sterilizer to perform a sterilization process, and the biological water composition is further output from a water outlet of the ultraviolet sterilizer to output the biological water composition. What needs to be supplemented here is that although the biological water composition of the specific example 2 of the present invention and the two first filters of the water purification system used in the preparation method thereof are as described above. However, the biological water composition of the specific example 2 of the present invention and the filter materials in the two first filters used in the manufacturing method thereof may also be implemented according to the manufacturing method of the first filter material of the specific example described above.

In the specific example 2 of the biological water composition and the manufacturing method thereof of the present invention, the drinking water is input from the water inlet of the first filter element located upstream to the biological water composition flowing out of the water outlet of the ultraviolet sterilizer for 15 days. The prepared biological water composition, its redox potential (ORP) and silicic acid concentration are simply summarized in Table 2 below.

Table 2.

It is worth mentioning that if the new first filter is used, the above data will be better, and the ORP value can be lower than -670 mV.

In addition, referring to FIG. 17, the redox potential (ORP) obtained from the biological water of the specific example 2 of the present invention after opening the bottle and tested through different filling rates shows that when the filling rate in the bottle is only about 23% Although the ORP value after the 432-minute stability test was increased from -570 mV to -100 mV, the ORP value after the 60-minute stability test was still maintained at -500 mV. In addition, when the filling in the bottle is 90%, the ORP value after the 432-minute stability test can still be maintained below -450 mV; when the filling in the bottle is increased to 93.48%, it is passed 432 The ORP value after a one-minute stability test can be maintained at -530 mV. The stability analysis results show that the oxidation-reduction potential (ORP) composition of the biological water of the specific example 2 of the present invention has good stability.

＜ Application example ＞

In order to further confirm that the biological water composition of the specific example 2 of the present invention has the effect of slowing the oxidation rate when added to the article, the applicant filled 100 cc apple juice into two glass bottles with a capacity of 0.2 L, and The two glass bottles were filled with 100 cc of the biological water composition of the specific example 2 (hereinafter referred to as an application example) and general drinking water (hereinafter referred to as a comparative example), and the two glass bottles were closed for a comparison test of oxidation speed. Referring to Figure 18 and the color image shown in the attachment, it can be seen that the apple juice of this comparative example (right glass bottle) has changed its color from yellow orange to dark orange after about 3 hours, confirming that the apple of this comparative example has already Significantly oxidized. In contrast, after about 3 hours, the apple juice of the application example (left glass bottle) of the present invention remains in a yellow-orange state, confirming that the biological water composition of the specific example 2 of the present invention is added to the apple juice to slow down its oxidation. The problem.

In summary, the filter core 4 and the water purification system using the filter core 4 of the present invention utilize active silicon material 422 formed on the surface of the carrier (such as porous materials such as activated carbon 4211 and hollow fiber membrane 4212). It reacts with biological water 9 to generate silicic acid and hydrogen bubbles 921, so that both the amount of dissolved hydrogen and the amount of dissolved silicon in biological water 9 are improved and a safe composition of biological water 92 is provided. Therefore, the purpose of the present invention can be achieved.

However, the above are only examples of the present invention. When the scope of implementation of the present invention cannot be limited by this, any simple equivalent changes and modifications made according to the scope of the patent application and the contents of the patent specification of the present invention are still Within the scope of the invention patent.

2‧‧‧ biological water unit

50‧‧‧ accommodation space

201‧‧‧ Inlet

501‧‧‧ water inlet

202‧‧‧ Outlet

502‧‧‧outlet

3‧‧‧ degassing unit

51‧‧‧ carrier

30‧‧‧ accommodation space

52‧‧‧ Porous material

301‧‧‧ water inlet

521‧‧‧ activated carbon

302‧‧‧outlet

522‧‧‧ hollow fiber membrane

31‧‧‧ carrier

53‧‧‧Nano silver

32‧‧‧ degassing component

6‧‧‧UV sterilization unit

4‧‧‧ filter, first filter

60‧‧‧accommodation space

40‧‧‧accommodation space

601‧‧‧ water inlet

401‧‧‧ water inlet

602‧‧‧outlet

402‧‧‧outlet

61‧‧‧ carrier

41‧‧‧ carrier

62‧‧‧UV light set

411‧‧‧The first part

7‧‧‧Piping unit

4111‧‧‧Interface section

71‧‧‧ water inlet pipe

4112‧‧‧ Male thread

72‧‧‧conveying pipeline

4113‧‧‧Ring groove

73‧‧‧outlet pipe

412‧‧‧Second Part

74‧‧‧Discharge unit

4121‧‧‧Interface section

75‧‧‧Total dissolved solids measurement unit

4122‧‧‧External thread

76‧‧‧Flowmeter

4123‧‧‧Ring groove

42‧‧‧ Filter media

421‧‧‧ carrier

4210‧‧‧Micropore

4211‧‧‧Activated carbon

4212‧‧‧ hollow fiber membrane

422‧‧‧active silicon

9‧‧‧ biological water

4220‧‧‧Nano silicon paste

4222 ‧ ‧ alcohol

423‧‧‧bonding material

43‧‧‧ Removable switch components

431‧‧‧Throughnut

4310‧‧‧Internal thread

Composition of 92‧‧‧ biological water

4311‧‧‧ Upper ring groove

921‧‧‧ Hydrogen Bubble

4312‧‧‧Lower ring groove

432‧‧‧External leakage ring

F‧‧‧flow direction

44‧‧‧Inner leakage ring

5‧‧‧Second Filter

Other features and effects of the present invention will be clearly presented in the embodiments with reference to the drawings, wherein:

1 is a schematic partial cross-sectional view illustrating a first embodiment of the filter core of the present invention;

2 is a schematic front view illustrating a first filter medium of the filter core of the first embodiment of the present invention;

3 is a schematic front view illustrating a method for manufacturing a first filter medium of the filter core according to the first embodiment of the present invention;

4 is a schematic partial cross-sectional view illustrating a second filter medium of the filter core according to the first embodiment of the present invention;

5 is a schematic front view illustrating a third filter material and a manufacturing method thereof for the filter core of the first embodiment of the present invention;

6 is a schematic partial cross-sectional view illustrating a second embodiment of the filter core of the present invention;

7 is a schematic partial sectional view illustrating a state of a third embodiment of the filter core of the present invention before use;

8 is a schematic partial cross-sectional view illustrating a state of the filter core after use according to the third embodiment of the present invention;

9 is a schematic partial cross-sectional view illustrating a fourth embodiment of the filter core of the present invention;

10 is a schematic partial cross-sectional view illustrating a fifth embodiment of the filter core of the present invention;

11 is a schematic partial cross-sectional view illustrating a sixth embodiment of the filter core of the present invention;

12 is a schematic partial cross-sectional view illustrating a first embodiment of the water purification system of the present invention;

13 is a partial cross-sectional view illustrating the composition of biological water produced by the water purification system according to the first embodiment of the present invention;

14 is a schematic partial cross-sectional view illustrating a second embodiment of the water purification system of the present invention;

15 is a partially enlarged schematic view of FIG. 14, illustrating a detailed structure of a second filter element of the water purification system according to the second embodiment of the present invention;

16 is a schematic partial cross-sectional view illustrating a third embodiment of the water purification system of the present invention;

FIG. 17 is a graph of oxidation-reduction potential (ORP) versus time, illustrating the stability of the biological water composition produced by the water purification system according to the first embodiment of the present invention under different filling rates ;and

FIG. 18 is a grayscale image illustrating the test result of slowing down the oxidation rate according to the specific example 2 of the biological water composition of the present invention.

Claims (31)

A filter core is used for purifying water and producing biological water containing silicic acid and hydrogen, and comprises: A carrier seat defining a containing space and including a water inlet and a water outlet communicating with the containing space; and A filter material is filled in the accommodation space of the carrier, and the filter material includes: A carrier selected from a porous material, a non-porous material, or a combination of the foregoing carriers, and A plurality of active silicon materials are adsorbed on one surface of the carrier. The filter of claim 1, wherein the carrier is selected from the group consisting of activated carbon, hollow fiber membrane, bamboo charcoal, maifanite, quartz sand, and a combination of the aforementioned carriers; The silicon material is selected from nano-silica materials, porous silicon materials, or granulated silicon materials with a particle size between 50 nm and 300 nm. The filter of claim 1, wherein the carrier is selected from the group consisting of activated carbon, hollow fiber membrane, bamboo charcoal, maifanite, quartz sand, fiber, ceramic, and a combination of the aforementioned carriers ; These active silicon materials are selected from nanometer silicon materials, porous silicon materials, granulated silicon materials, or silicon nanowires with a particle size between 50 nm and 300 nm. The filter core according to claim 2, wherein the carrier is activated carbon with a plurality of micropores distributed on the surface, and the activated silicon material adsorbed on the surface of the carrier is located in the micropores of the activated carbon. The filter core according to claim 4, wherein the filter material further comprises a bonding material, the bonding material combines nano silicon material and activated carbon, and the bonding material and activated carbon together form a sintered activated carbon. The filter core according to claim 2, wherein the carrier is a hollow fiber membrane having a tubular structure and having a plurality of micropores penetrating through the tubular structure. The filter core according to claim 1, wherein, based on the weight percentage of the filter material, the content of the carrier is 90 wt% or less, and the content of the active silicon materials is 10 wt% or more. The filter core according to claim 1, wherein, based on the weight percentage of the filter material, the content of the carrier is 80 wt% or less, and the content of the active silicon materials is 20 wt% or more. The filter core according to claim 1, wherein the position of the water inlet is lower than the position of the water outlet. The filter core according to claim 1, further comprising a dispersed water flow unit, the dispersed water flow unit is located in the accommodating space of the carrier and adjacent to the water inlet. The filter core according to claim 10, wherein the carrier in the accommodation space of the carrier and adjacent to the water inlet is used as the dispersed water flow unit. The filter core according to claim 1, further comprising a blocking unit, the blocking unit is located in the accommodating space of the carrier and adjacent to the water outlet. The filter element according to claim 12, wherein the carrier is located in the accommodation space of the carrier and adjacent to the water outlet as the blocking unit. The filter core according to claim 1, wherein the carrier is activated carbon uniformly distributed in the accommodating space of the carrier, and the activated silicon materials are nano-silicon materials. The filter according to claim 1, wherein the carrier is a combination of activated carbon and hollow fiber membrane, and the activated silicon materials are nano-silicon materials, and the activated carbon is evenly distributed in the accommodation space of the carrier. It is relatively close to the water inlet with respect to the hollow fiber membrane. The hollow fiber membrane is distributed in the accommodating space of the carrier and is closer to the water outlet with respect to activated carbon. The filter according to claim 1, wherein the carrier is a combination of activated carbon and hollow fiber membrane, and the activated silicon materials are nano-silicon materials, and the activated carbon is evenly distributed in the accommodation space of the carrier. The hollow fiber membrane is located near the water inlet with respect to the hollow fiber membrane. The hollow fiber membrane is located in the accommodating space of the carrier to surround the activated carbon and is closer to the water outlet with respect to the activated carbon. The filter according to claim 1, wherein the carrier is a combination of activated carbon and hollow fiber membrane, and the active silicon material is nano-silicon material, and the hollow fiber membrane is located in the accommodation space of the carrier. The relative activated carbon is close to the water outlet. The activated carbon is located in the accommodating space of the carrier to surround the hollow fiber membrane and is relatively close to the water inlet with respect to the hollow fiber membrane. The filter element according to claim 1, further comprising a detachable switch member. The carrier has a first component and a second component disposed at a distance from each other. The first component and the second component respectively include the inlet and outlet. The water outlet and the water outlet, the removable switch member is connected between the first member and the second member, and the accommodation space of the carrier is composed of the first member, the second member, and the removable switch member. The carrier is a combination of activated carbon and hollow fiber membrane, and the active silicon material is nano silicon material, the activated carbon is located in the first part of the carrier, and the hollow fiber membrane is located in The second part of the carrier. The utility model relates to a water purification system, which is used for connecting with a biological water unit produced and containing a biological water and producing biological water containing silicic acid and hydrogen. The water purification system comprises: At least one first filter is a filter as described in claim 1. The water purification system according to claim 19, further comprising a pipeline unit and at least one second filter; The second filter element is disposed at a downstream position of the first filter element along the direction of the water flow, and includes a carrier defining an accommodation space, and a plurality of holes filled in the accommodation space of the carrier. Material, the carrier of the second filter core has a water inlet and a water outlet in communication with its containing space; and The pipeline unit has at least one conveying pipeline sequentially connecting the first filter element and the second filter element along the water flow direction. The water purification system according to claim 20, wherein the porous material in the accommodating space of the carrier of the second filter is selected from activated carbon, hollow fiber membrane, or a combination of the foregoing porous materials. The water purification system according to claim 20, wherein the number of the second filters is plural, and the porous material filled in the accommodating space of the carriers of the second filters depends on the direction of the water flow. The sequence is activated carbon and hollow fiber membrane. The water purification system according to claim 21 or 22, wherein the second filter element further comprises nanosilver filled in the corresponding accommodation space. The water purification system according to claim 20, further comprising a drainage unit, the drainage unit is disposed on the pipeline unit and located behind the second filter element along the water flow direction, and the drainage unit communicates with the pipeline unit and is used. To discharge liquid, gas, or a combination of liquid and gas. The water purification system according to claim 20, further comprising a drainage unit, the drainage unit is disposed on the pipeline unit and is located between the first filter element and the second filter element, and the drainage unit communicates with the pipeline The unit is also used to discharge liquid, gas, or a combination of liquid and gas. The water purification system according to claim 20, 24 or 25, wherein the second filter element is placed in an upright position. The water purification system according to claim 20, 24 or 25, wherein the water inlet of the second filter element is higher than its water outlet. The water purification system according to claim 19, further comprising a degassing unit, the degassing unit is disposed at an upstream position of the first filter element along the water flow direction, and is a conveying pipe borrowed from a pipeline unit The road sequentially connects the deaeration unit and the first filter element along the flowing water direction, and is used for removing gas in the water. The water purification system according to claim 19, further comprising an ultraviolet light sterilization unit, the ultraviolet light sterilization unit is disposed at a downstream position of the first filter element along the direction of the water flow, and is borrowed from a pipeline unit. A transmission pipeline sequentially connects the first filter element and the ultraviolet light sterilization unit along the direction of the water flow, and is used to sterilize the biological water composition. The water purification system according to claim 19, further comprising two total dissolved solids measurement units, which are respectively disposed at an upstream position of the first filter element and a total dissolved solids measurement unit along the water flow direction. Downstream location. The water purification system according to claim 19, further comprising a flow meter, the flow meter is disposed at an upstream position of the first filter element along the water flow direction.