CN111867700A - Integrated composite filter module for water purifier - Google Patents
Integrated composite filter module for water purifier Download PDFInfo
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- CN111867700A CN111867700A CN201980020279.0A CN201980020279A CN111867700A CN 111867700 A CN111867700 A CN 111867700A CN 201980020279 A CN201980020279 A CN 201980020279A CN 111867700 A CN111867700 A CN 111867700A
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- 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
- B01D35/30—Filter housing constructions
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- 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
- B01D39/20—Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
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- 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
- B01D39/20—Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
- B01D39/2055—Carbonaceous material
- B01D39/2058—Carbonaceous material the material being particulate
- B01D39/2062—Bonded, e.g. activated carbon blocks
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
- B01D61/025—Reverse osmosis; Hyperfiltration
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
- B01D63/10—Spiral-wound membrane modules
- B01D63/12—Spiral-wound membrane modules comprising multiple spiral-wound assemblies
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- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/06—Organic material
- B01D71/56—Polyamides, e.g. polyester-amides
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- 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
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
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- 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
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
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Abstract
Description
技术领域technical field
本发明涉及净水器用一体型复合过滤器模块,更详细地,涉及如下的净水器用一体型复合过滤器模块是,即,可确保优秀的盐去除率及渗透流量,同时明显地减少净水器的体积。The present invention relates to an integrated composite filter module for a water purifier, and more particularly, to an integrated composite filter module for a water purifier that can ensure excellent salt removal rate and permeate flow rate while significantly reducing purified water volume of the device.
背景技术Background technique
随着净化及污水处理技术的发展,处理技术的方向正从现有的沙子过滤方式转变为利用分离膜的膜过滤方式。With the development of purification and sewage treatment technology, the direction of treatment technology is changing from the existing sand filtration method to the membrane filtration method using separation membranes.
这种分离膜技术是根据膜的气孔大小、气孔分布以及膜表面电荷几乎完全分离去除存在于处理水中的处理对象物质的高度分离技术。This separation membrane technology is a high-level separation technology that almost completely separates and removes the treatment target substance present in the treated water based on the pore size, pore distribution, and membrane surface charge of the membrane.
根据气孔大小,上述分离膜分类为精密过滤膜(MF膜)、超滤膜系统(UF膜)、纳米分离膜(NF膜)及反渗透膜(RO膜),在水处理领域中,其适用范围扩大至与优质饮水及工业用水的生产、下/废水处理及再利用、与无放流系统开发相关的净化生产工序等,作为在21世纪备受瞩目的核心技术之一广泛普及。实际上,大多数国民将经净化处理后供给的自来水再次通过净水器进行处理来饮用,因此,需要进一步开发与此有关的技术。According to the size of pores, the above separation membranes are classified into precision filtration membranes (MF membranes), ultrafiltration membrane systems (UF membranes), nano-separation membranes (NF membranes) and reverse osmosis membranes (RO membranes). The scope is expanded to the production of high-quality drinking water and industrial water, wastewater treatment and reuse, and purification production processes related to the development of non-discharge systems, etc., and is widely used as one of the core technologies that attract attention in the 21st century. In fact, the tap water supplied after being purified is treated by a water purifier for drinking in most of the citizens, and therefore, further development of technologies related to this is required.
净水器系统由分离膜模块、前处理及后处理过滤器、泵、配管、罐及其他辅助装置组成,组成上述系统的要素中最重要部分是分离膜模块。作为分离膜模块的种类,平板型、中空纤维型、管状型、螺旋缠绕型等被商业化,主要对每单位面积的分离膜插入密度高,可以去除水中离子的螺旋缠绕型分离膜模块进行研究。而且,最近正在积极进行将净水器系统简化的研究。The water purifier system consists of a separation membrane module, pre-treatment and post-treatment filters, pumps, piping, tanks and other auxiliary devices. The most important part of the elements that make up the above system is the separation membrane module. As the types of separation membrane modules, flat plate type, hollow fiber type, tubular type, spiral wound type, etc. are commercialized, and research is mainly on spiral wound separation membrane modules that have high insertion density of separation membrane per unit area and can remove ions from water. . Moreover, recently, research to simplify the water purifier system is being actively conducted.
现有的反渗透净水器结构由取水阀、沉淀物过滤器、前置活性炭过滤器、升压泵、聚酰胺系复合膜、后置活性炭过滤器、反流防止阀、生活用水调节阀及净水调节阀等组成。The structure of the existing reverse osmosis water purifier consists of a water intake valve, a sediment filter, a front activated carbon filter, a booster pump, a polyamide composite membrane, a rear activated carbon filter, a backflow prevention valve, a domestic water control valve and Water purification valve and other components.
沉淀物过滤器起到从原水中去除浮游物、沙子、锈残留物及苔藓等较大杂质的功能,前置活性炭过滤器从原水中去除农药成分及致癌物质等挥发性有机化合物,作为最重要的功能,为了防止后端的聚酰胺复合膜因残留氯而被氧化分解,因而去除残留氯。聚酰胺复合膜起到过滤掉原水中含有的有机污染物质、无机污染物质、细菌、病毒、包含重金属等的离子性物质的功能,后置活性炭过滤器起到去除原水中含有的气态物质来去除水的异味,提高水的味道的功能。The sediment filter functions to remove large impurities such as suspended matter, sand, rust residues and moss from the raw water, and the pre-activated carbon filter removes volatile organic compounds such as pesticides and carcinogens from the raw water. In order to prevent the polyamide composite membrane at the rear end from being oxidatively decomposed due to residual chlorine, the residual chlorine is removed. The polyamide composite membrane has the function of filtering out organic pollutants, inorganic pollutants, bacteria, viruses, ionic substances including heavy metals, etc. contained in the raw water, and the activated carbon filter behind it can remove gaseous substances contained in the raw water. The odor of water, the function of improving the taste of water.
由以往的沉淀物过滤器、前置活性炭过滤器、聚酰胺复合膜及后置活性炭过滤器组成的反渗透净水器过滤器由4个过滤器组成,从而,因体积较大而很难在狭窄的空间使用,且很难适用于需要超薄设计的应用。The reverse osmosis water purifier filter composed of the previous sediment filter, pre-activated carbon filter, polyamide composite membrane and post-activated carbon filter consists of 4 filters, so it is difficult to filter in the filter due to its large size. Used in tight spaces and difficult to apply to applications that require ultra-thin designs.
并且,由于难以确定过滤器寿命或更换时间,以及安装在反渗透净水器过滤器部的过滤器(沉淀物过滤器、前置活性炭过滤器、聚酰胺复合膜、后置活性炭过滤器)的复杂性,存在使用人员很难自行更换的问题。Also, because it is difficult to determine the filter life or replacement time, and the filter (sediment filter, pre-activated carbon filter, polyamide composite membrane, post-activated carbon filter) installed in the filter part of the reverse osmosis water purifier. Complexity, there is a problem that it is difficult for users to replace by themselves.
作为解决这些问题的专利,在韩国公开专利公报第10-2004-0042180的情况下,涉及上述说明的简化的过滤器外罩,将沉淀物过滤器及前置活性炭过滤器、反渗透分离膜过滤器、后置活性炭过滤器及相互连接的多个配管最小化来将其全部收容在一个过滤器外罩中,从而,与以往相比,净水器的体积减少,可以使消费者轻松更换过滤器。向上述过滤器外罩插入的多个过滤器通过调整容积来使交换周期一致,因此,消费者可以轻松更换过滤器外罩本身。但是,过滤器外罩内部的沉淀物过滤器、前置活性炭过滤器、反渗透过滤器及后置活性炭过滤器由各自的外罩组成,从而,减少净水器体积方面受限。As a patent for solving these problems, Korean Laid-Open Patent Publication No. 10-2004-0042180 relates to the simplified filter housing described above, which incorporates a sediment filter, a pre-activated carbon filter, and a reverse osmosis separation membrane filter. , The rear activated carbon filter and multiple interconnected pipes are minimized to accommodate all of them in one filter housing, so that the volume of the water purifier is reduced compared to the past, and the filter can be easily replaced by consumers. Since a plurality of filters inserted into the above-mentioned filter housings are adjusted in volume to make the exchange cycle uniform, consumers can easily replace the filter housings themselves. However, the sediment filter, the pre-activated carbon filter, the reverse osmosis filter, and the rear activated carbon filter inside the filter housing are composed of their respective housings, so that there is a limitation in reducing the volume of the water purifier.
发明内容SUMMARY OF THE INVENTION
技术问题technical problem
本发明是考虑到上述问题后提出,本发明的目的在于,提供如下的净水器用一体型复合过滤器模块,即,可确保优秀的盐去除率及渗透流量,同时明显地减小净水器的体积。The present invention has been made in consideration of the above-mentioned problems, and an object of the present invention is to provide an integrated composite filter module for a water purifier which can ensure excellent salt removal rate and permeate flow rate, and at the same time reduce the water purifier significantly. volume of.
并且,本发明的另一个目在于,提供包括一体型复合过滤器模块的尺寸显著小的净水器。Also, another object of the present invention is to provide a water purifier having a remarkably small size including an integrated composite filter module.
技术方案Technical solutions
为了解决上述问题,本发明提供净水器用一体型复合过滤器模块,上述净水器用一体型复合过滤器模块包括:第一过滤部,包括外部外罩及沉淀物过滤器,上述外部外罩设置有使原水流入的流入口,上述沉淀物过滤器设置于上述外部外罩内;以及第二过滤部,配置于上述第一过滤部的内侧,用于对通过上述第一过滤部进行第一次过滤的水进行二次过滤,第二过滤部包括:内部外罩,设置有生产水排出口及浓缩水排出口;聚酰胺反渗透膜模块;以及后置活性炭过滤器,设置于上述聚酰胺反渗透膜模块的内侧。In order to solve the above-mentioned problems, the present invention provides an integrated composite filter module for a water purifier. The integrated composite filter module for a water purifier includes: a first filter part including an outer cover and a sediment filter, and the outer cover is provided with a an inflow port into which raw water flows, the sediment filter is installed in the outer cover; and a second filter part is arranged inside the first filter part and is used to filter the water that has passed through the first filter part for the first time For secondary filtration, the second filtration part includes: an inner cover, which is provided with a production water discharge port and a concentrated water discharge port; a polyamide reverse osmosis membrane module; inside.
根据本发明的一实施例,上述聚酰胺反渗透膜模块可以为耐氯性聚酰胺反渗透膜模块。According to an embodiment of the present invention, the above-mentioned polyamide reverse osmosis membrane module may be a chlorine-resistant polyamide reverse osmosis membrane module.
并且,根据本发明的一实施例,上述原水可沿着设置于上述外部外罩的内侧面与上沉淀物过滤器的外侧面之间的原水流路进行移动,经第一次过滤的水可沿着设置于上述沉淀物过滤器的内侧面与上述内部外罩的外侧面之间的渗透水流路进行移动。并且,根据本发明的一实施例,上述后置活性炭过滤器可处于在上述聚酰胺反渗透膜模块的中心缩管(central pipe)内侧填充活性炭的形态。In addition, according to an embodiment of the present invention, the raw water can move along the raw water flow path provided between the inner surface of the outer cover and the outer surface of the upper sediment filter, and the water filtered for the first time can move along the It moves according to the permeated water flow path provided between the inner surface of the sediment filter and the outer surface of the inner cover. Furthermore, according to an embodiment of the present invention, the rear activated carbon filter may be in a form in which activated carbon is filled inside the central pipe of the polyamide reverse osmosis membrane module.
并且,据本发明的一实施例,上述内部外罩的内侧面和上述聚酰胺反渗透膜模块的外侧面之间可形成具有规定厚度的密封部件。Furthermore, according to an embodiment of the present invention, a sealing member having a predetermined thickness may be formed between the inner surface of the inner housing and the outer surface of the polyamide reverse osmosis membrane module.
并且,据本发明的一实施例,在常温状态下,当处于0.5ppm的残留氯浓度、250μS/cm的传导度及40psi的压力条件时,通过上述流入口流入的原水渗透流量可以为12.0GFD以上。Furthermore, according to an embodiment of the present invention, under normal temperature conditions, when the residual chlorine concentration is 0.5 ppm, the conductivity is 250 μS/cm, and the pressure is 40 psi, the permeation flow rate of the raw water flowing through the inflow port can be 12.0 GFD above.
并且,据本发明的一实施例,上述沉淀物过滤器可以包括用于去除上述原水内的挥发性有机物质的碳材料。Also, according to an embodiment of the present invention, the above-mentioned sediment filter may include a carbon material for removing volatile organic substances in the above-mentioned raw water.
并且,据本发明的一实施例,本发明提供包括净水器用一体型复合过滤器模块的净水器。Furthermore, according to an embodiment of the present invention, the present invention provides a water purifier including an integrated composite filter module for a water purifier.
发明的效果effect of invention
本发明的净水器用一体型复合过滤器模块具有如下的效果,即,可确保优秀的盐去除率及渗透流量,同时明显地减少净水器的体积,从而,也能够在狭窄的空间使用。The integrated composite filter module for a water purifier of the present invention has the effect of ensuring an excellent salt removal rate and permeation flow rate, while significantly reducing the volume of the water purifier, so that it can be used even in a narrow space.
附图说明Description of drawings
图1为本发明一实施例的净水器用一体型复合过滤器模块的剖面立体图及X-X'剖视图。1 is a cross-sectional perspective view and an XX' cross-sectional view of an integrated composite filter module for a water purifier according to an embodiment of the present invention.
图2为本发明一实施例的净水器用一体型复合过滤器模块中所包括的聚酰胺反渗透膜模块的剖面分解立体图。2 is a cross-sectional exploded perspective view of a polyamide reverse osmosis membrane module included in an integrated composite filter module for a water purifier according to an embodiment of the present invention.
具体实施方式Detailed ways
以下,参照附图,详细说明本发明的实施例,以使本发明所属技术领域的普通技术人员可以轻松实施本发明。本发明可体现为多种不同的形态,本发明并不局限于在此说明的实施例。Hereinafter, the embodiments of the present invention will be described in detail with reference to the accompanying drawings, so that those skilled in the art to which the present invention pertains can easily implement the present invention. The present invention may be embodied in many different forms, and the present invention is not limited to the embodiments described herein.
本发明的净水器用一体型复合过滤器模块10包括:第一过滤部,包括外部外罩及沉淀物过滤器,上述外部外罩11设置有使原水流入的流入口19a,上述沉淀物过滤器13设置于上述外部外罩11内;第二过滤部,配置于上述第一过滤部的内侧,用于对通过上述第一过滤部进行第一次过滤的水进行二次过滤,上述第二过滤部包括:内部外罩15,设置有生产水排出口19b及浓缩水排出口19c;聚酰胺反渗透膜模块17;以及后置活性炭过滤器18,设置于上述聚酰胺反渗透膜模块17的内侧。The integrated composite filter module 10 for a water purifier of the present invention includes: a first filter part including an outer cover and a sediment filter, the
另一方面,上述聚酰胺反渗透膜模块17可以为耐氯性聚酰胺反渗透膜模块,更详细地,本发明可提供如下的一体型复合过滤器模块,即,可以使用耐氯性聚酰胺反渗透膜模块来省略前置活性炭过滤器,在第一过滤部内设置可同时执行基于反渗透膜的过滤及基于后置活性炭过滤器的残留氯去除功能的第二过滤部,确保可以使从通过第一过滤部过滤的水直接向第二过滤部的空间移动,优选地,通过上述沉淀物过滤器第一次过滤的水通过设置于上述内部外罩的外侧面及沉淀物过滤器的内侧面之间的渗透水流路直接向上述聚酰胺反渗透膜模块流入,由此,将现有串联配置的多个净水器用过滤器一体化来显著减少净水器的体积,同时,可确保优秀的渗透流量及盐去除率。On the other hand, the above-mentioned polyamide reverse
以下,参照作为本发明优选一实施例的一体型复合过滤器模块的剖面立体图的图1,说明上述一体型复合过滤器模块。Hereinafter, the integrated composite filter module described above will be described with reference to FIG. 1 , which is a cross-sectional perspective view of an integrated composite filter module according to a preferred embodiment of the present invention.
首先,可通过外部外罩11的流入口19a供给原水,作为一例,自来水。通过上述流入口19a流入的原水通过设置于外部外罩11的内侧面及沉淀物过滤器13外侧面之间的原水流路12进行移动并连续通过沉淀物过滤器13进行第一次过滤。First, raw water, for example, tap water, can be supplied through the
上述外部外罩的材料可以不受限制地使用本发明所属技术领域中通常用于净水器用过滤器的外罩的材料,外部外罩的形态可以根据第一过滤部及第二过滤部中所包括的各结构的形态变更成多种形态,作为一例,可呈圆形管形态。The material of the above-mentioned outer cover can be used without limitation as the material generally used for the outer cover of the filter for water purifiers in the technical field to which the present invention pertains. The form of the structure can be changed into various forms, and as an example, the form of a circular tube can be adopted.
上述沉淀物过滤器的材料可以使用本发明所属技术领域中通常用于净水器用沉淀物过滤器的材料,形状可呈圆形管形态,但不限于此。上述沉淀物过滤器可去除水中的浮游物质、沙子、锈残留物及苔藓等较大杂质,上述沉淀物过滤器可包含碳材料,用于去除上述原水内的挥发性有机物。上述碳材料可以是本发明所属技术领域中用于去除挥发性有机物质的材料,作为一例,可以为活性炭或活性炭粉末,但不限于此。The material of the above-mentioned sediment filter can be the material commonly used in the sediment filter for water purifiers in the technical field to which the present invention pertains, and the shape can be in the form of a circular tube, but is not limited thereto. The above-mentioned sediment filter can remove large impurities such as floating matter, sand, rust residue and moss in the water, and the above-mentioned sediment filter can contain carbon material for removing volatile organic compounds in the above-mentioned raw water. The above-mentioned carbon material can be a material used for removing volatile organic substances in the technical field of the present invention. As an example, it can be activated carbon or activated carbon powder, but it is not limited thereto.
第一次过滤的水可通过设置于内部外罩15的外侧面及沉淀物过滤器13的内侧面之间的渗透水流路14向上述内部外罩15的末端移动来向第二过滤部的聚酰胺反渗透膜模块17流入。The water filtered for the first time can move to the end of the
并且,在上述内部外罩15的内侧面与上述聚酰胺反渗透膜模块之间可形成密封部件16,因此,通过沉淀物过滤器第一次过滤的水可以没有损失地向第二过滤部的反渗透膜模块进行移动。In addition, since the
上述内部外罩的材料可以没有限制地使用本发明所属技术领域中通常用于反渗透膜模块的外罩的材料。As the material of the above-mentioned inner casing, the material generally used for the casing of the reverse osmosis membrane module in the technical field to which the present invention pertains can be used without limitation.
优选地,上述密封部件可以是乙烯丙烯三元共聚物(Etyhlene PropylenTerpolymer)材料的盐水密封件(brine seal),但不限于此。Preferably, the above-mentioned sealing member may be a brine seal of ethylene propylene terpolymer (Etyhlene Propylen Terpolymer) material, but is not limited thereto.
上述耐氯性聚酰胺反渗透膜模块过滤在从沉淀物过滤器流入的原水中去除有机污染物质、无机污染物质、细菌、病毒、包含重金属等的离子性物质。并且,与现有聚酰胺反渗透膜相比,对氯的耐久性强,从而可以省略去除残留氯成分的前置活性炭过滤器,可通过设置于能够去除一部分残留氯的耐氯性聚酰胺反渗透膜模块内的中心缩管来对包含残留氯的水进行二次过滤。The chlorine-resistant polyamide reverse osmosis membrane module filtration removes organic contaminants, inorganic contaminants, bacteria, viruses, and ionic substances including heavy metals and the like in the raw water flowing from the sediment filter. In addition, compared with the conventional polyamide reverse osmosis membrane, the durability against chlorine is strong, so that the pre-activated carbon filter for removing residual chlorine can be omitted, and a chlorine-resistant polyamide reverse osmosis membrane that can remove a part of residual chlorine can be installed. Permeate the central shrink tube in the membrane module to perform secondary filtration of water containing residual chlorine.
优选地,上述聚酰胺反渗透膜模块可以包括将原水的残留氯渗透20%以上的烷基化的聚酰胺复合膜,当上述烷基化的聚酰胺复合膜使浓度为500ppm至2000ppm的次氯酸钠溶液通过1小时至24小时时,可以维持至少85%的去除性能。在第二次过滤的水中所包含的微量残留氯可以去除存在于后置活性炭过滤器内的微生物或病毒等,同时,还可去除气态物质,去除水的异味,并提高水的味道。Preferably, the above-mentioned polyamide reverse osmosis membrane module may include an alkylated polyamide composite membrane that permeates more than 20% of the residual chlorine in the raw water, when the above-mentioned alkylated polyamide composite membrane makes a sodium hypochlorite solution with a concentration of 500 ppm to 2000 ppm At least 85% removal performance can be maintained through 1 hour to 24 hours. The trace residual chlorine contained in the second filtered water can remove microorganisms or viruses, etc. existing in the post-activated carbon filter, and at the same time, it can also remove gaseous substances, remove the odor of water, and improve the taste of water.
上述聚酰胺反渗透膜模块的形状可以使用本发明所属技术领域中通常使用的反渗透模块的结构,作为对其的非限制性的例,上述反渗透膜可以与形成流路的隔片一同以螺旋缠绕型卷绕在中心缩管,为了在被卷绕的膜的两端卷绕的分离膜的形状稳定性而可以包括端部盖。The shape of the above-mentioned polyamide reverse osmosis membrane module can be the structure of a reverse osmosis module commonly used in the technical field to which the present invention pertains. The spiral wound type is wound around a central shrink tube, and may include end caps for the purpose of dimensional stability of the separation membrane wound around both ends of the wound membrane.
图二为本发明一实施例的净水器用一体型复合过滤器模块中所包括的聚酰胺反渗透膜模块20的剖面分解立体图。FIG. 2 is a cross-sectional exploded perspective view of the polyamide reverse
参照图2,聚酰胺反渗透膜21能够以中心缩管24为中心,以螺旋缠绕型卷绕,在卷绕的聚酰胺反渗透膜21之间可设置:外部隔片23,起到第一次过滤的水的流路作用和执行提高反渗透膜的外侧面的接触效率的功能;以及内部隔片22,用于使从反渗透膜渗透的水向设置于中心缩管24内的后置活性炭过滤器25有效地移动。Referring to FIG. 2 , the polyamide
上述外部隔片23及内部隔片22的材料及形状可以使用本发明所属技术领域中公知的反渗透膜模块的结构。The material and shape of the
残留氯浓度为0.5ppm,传导度为250μS/㎝的自来水,当上述原水以40psi的压力条件流入时,原水渗透流量可以为12.0GFD以上。For tap water with a residual chlorine concentration of 0.5 ppm and a conductivity of 250 μS/cm, when the above-mentioned raw water flows in at a pressure of 40 psi, the raw water permeation flow rate can be 12.0 GFD or more.
接着,通过上述聚酰胺反渗透膜模块17第二次过滤的水向后置活性炭过滤器18进行移动,可在后置活性炭过滤器18末端去除微量残留氯的生产水通过在内部外罩15下端设置的生产水排出口19b排出。并且,在第二次过滤水中,除生产水之外的浓缩水可以通过设置在内壳15下端的浓缩水排出口19c来排出。Next, the water filtered for the second time by the above-mentioned polyamide reverse
上述后置活性炭过滤器18可处于在上述聚酰胺反渗透膜模块17的中心缩管内填充活性炭的形态。上述活性炭的粒径及填充率可以使用本发明所属技术领域中通常使用的后置活性炭过滤器的结构。The above-mentioned rear activated
并且,在本发明净水器用一体型复合过滤器模块中,在常温状态下,当处于0.5ppm的残留氯浓度、250μS/cm的传导度及40psi的压力条件时,通过上述流入口流入的原水渗透流量可以为12.0GFD以上。In addition, in the integrated composite filter module for a water purifier of the present invention, under normal temperature conditions, the raw water flowing in through the inflow port is under the conditions of a residual chlorine concentration of 0.5 ppm, a conductivity of 250 μS/cm, and a pressure of 40 psi. The permeate flow may be above 12.0 GFD.
另一方面,本发明提供包括本发明的净水器用一体型复合过滤器模块的净水器。除本发明的净水器中所包括的净水器用一体型复合过滤器模块之外,本体、排水管、排放管及滴水盘等结构可以使用本发明所属技术领域中通常使用的公知结构,代替现有的串联式净水器过滤器,可以使用本发明的净水器用一体型复合过滤器模块来体现体积明显小于现有净水器的紧凑净水器。On the other hand, the present invention provides a water purifier including the integrated composite filter module for a water purifier of the present invention. In addition to the integrated composite filter module for a water purifier included in the water purifier of the present invention, structures such as the main body, the drain pipe, the drain pipe, and the drip tray can be replaced by well-known structures commonly used in the technical field to which the present invention pertains. The existing in-line water purifier filter can use the integrated composite filter module for the water purifier of the present invention to embody a compact water purifier whose volume is significantly smaller than the existing water purifier.
准备例1Preparation example 1
使用直径为1.8英寸,有效膜面积为4.8ft2的螺旋缠绕型模块形态的耐氯性聚酰胺膜来制造耐氯性聚酰胺反渗透膜模块。A chlorine-resistant polyamide reverse osmosis membrane module was manufactured using a chlorine-resistant polyamide membrane in the form of a spiral wound module having a diameter of 1.8 inches and an effective membrane area of 4.8 ft 2 .
实施例1Example 1
向在准备例1中制造的耐氯性聚酰胺反渗透膜模块内的中心缩管内填充活性炭,结合上述反渗透膜模块内的设置后置活性炭过滤器的内部外罩与包括沉淀物过滤器的外部外罩来制造一体型复合过滤器模块。Activated carbon was filled into the central shrinkage tube in the chlorine-resistant polyamide reverse osmosis membrane module manufactured in Preparation Example 1, and the inner cover provided with the rear activated carbon filter in the reverse osmosis membrane module described above was combined with the outer cover including the sediment filter. housing to manufacture an integrated composite filter module.
比较例1Comparative Example 1
将沉淀物过滤器、在准备例1中制造的耐氯性聚酰胺反渗透膜模块及后置活性炭过滤器串联配置,通过排水管连接各个过滤器来制造过滤器模块。The sediment filter, the chlorine-resistant polyamide reverse osmosis membrane module produced in Preparation Example 1, and the post-installed activated carbon filter were arranged in series, and the filters were connected by a drain pipe to produce a filter module.
实验例1Experimental example 1
计算出除在实施例及比较例中制造的过滤器模块的配管之外的体积并呈现在以下表1中。The volumes other than the piping of the filter modules manufactured in the Examples and Comparative Examples were calculated and presented in Table 1 below.
【表1】【Table 1】
参照上述表1,沉淀物过滤器、反渗透膜模块及后置活性炭过滤器串联配置的比较例1的过滤器模块体积约为一体型复合过滤器模块(实施例1)体积的192%,从而可以确认体积明显大于一体型复合过滤器模块。Referring to the above Table 1, the volume of the filter module of Comparative Example 1 in which the sediment filter, the reverse osmosis membrane module and the rear activated carbon filter are arranged in series is about 192% of the volume of the one-piece composite filter module (Example 1). It can be confirmed that the volume is significantly larger than the one-piece composite filter module.
实验例2Experimental example 2
1)盐去除率1) Salt removal rate
使用在实施例1及比较例1中制造的过滤器模块,将在常温状态下,残留氯浓度为0.5ppm,传导度为250μS/cm的自来水作为原水来使其在40psi的压力条件下进行工作。上述工作方式如下,即,在反复进行工作12小时后,停止12小时的行程,并工作60天。最后,测定盐去除率并将结果呈现在以下表2中。The filter modules manufactured in Example 1 and Comparative Example 1 were used, and tap water with a residual chlorine concentration of 0.5 ppm and a conductivity of 250 μS/cm at room temperature was used as raw water to operate under a pressure of 40 psi. . The above-mentioned operation method is as follows, that is, after repeating the operation for 12 hours, the 12-hour trip is stopped, and the operation is continued for 60 days. Finally, the salt removal rate was determined and the results are presented in Table 2 below.
【表2】【Table 2】
参照上述表2,可以确认实施例1的一体型复合过滤器模块即使以非常小的体积也可以具有与各过滤器串联配置的比较例1相同水平的盐去除率。Referring to Table 2 above, it can be confirmed that the integrated composite filter module of Example 1 can have the same level of salt removal rate as that of Comparative Example 1 in which each filter is arranged in series even in a very small volume.
2)测定生产流量2) Determination of production flow
使用在实施例1及比较例1中制造的过滤器模块,将在常温状态下,残留氯浓度为0.5ppm,传导度为250μS/cm的自来水作为原水来使其在40psi的压力条件下进行工作。上述工作方式如下,即,在反复进行工作12小时后,停止12小时的行程,并工作60天。最后,测定盐去除率并将结果呈现在以下表3中。The filter modules manufactured in Example 1 and Comparative Example 1 were used, and tap water with a residual chlorine concentration of 0.5 ppm and a conductivity of 250 μS/cm at room temperature was used as raw water to operate under a pressure of 40 psi. . The above-mentioned operation method is as follows, that is, after repeating the operation for 12 hours, the 12-hour trip is stopped, and the operation is continued for 60 days. Finally, the salt removal rate was determined and the results are presented in Table 3 below.
【表3】【table 3】
参照上述表3,与各个过滤器串联配置的比较例1的模块相比,可以确认实施例1的一体型复合过滤器模块即使以非常小的体积,初期生产水流量及60日后生产水流量为显著高的120%的水平。这是因为在各过滤器串联配置的情况下,因当从各过滤器排出的水向下一步骤的过滤器移动时,在配管中发生的压力损失而导致生产水流量的减少,在各过滤器由一体型复合过滤器模块组成的情况下,将因在配管中发生的压力损失而导致的生产水流量的减少最小化,从而可以提高生产水的流量。Referring to the above Table 3, compared with the module of Comparative Example 1 in which each filter is arranged in series, it can be confirmed that even if the integrated composite filter module of Example 1 has a very small volume, the initial production water flow rate and the production water flow rate after 60 days are: A significantly higher level of 120%. This is because when the filters are arranged in series, when the water discharged from each filter moves to the filter of the next step, the flow rate of produced water decreases due to the pressure loss that occurs in the piping. When the filter is composed of an integrated composite filter module, the reduction in the flow rate of the produced water due to the pressure loss occurring in the piping can be minimized, and the flow rate of the produced water can be increased.
以上,说明了本发明的一实施例,但本发明的思想并不限于在本说明书中提出的实施例,理解本发明思想的本发明所属技术领域的普通技术人员在相同思想的范围内,可通过结构要素的附加、变更、删除、追加等可以轻易提出其他实施例,但这也属于本发明的思想范围内。An embodiment of the present invention has been described above, but the idea of the present invention is not limited to the embodiment proposed in this specification. Those of ordinary skill in the technical field to which the present invention pertains who understand the idea of the present invention may, within the scope of the same idea, Other embodiments can be easily proposed by addition, change, deletion, addition, etc. of structural elements, but this also falls within the scope of the idea of the present invention.
Claims (8)
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| KR1020180162014A KR20200073633A (en) | 2018-12-14 | 2018-12-14 | Interated type complex filter module for separating water purifier |
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| PCT/KR2019/017611 WO2020122642A1 (en) | 2018-12-14 | 2019-12-12 | Integrated composite filter module for water purifier |
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| US20240367109A1 (en) * | 2021-07-28 | 2024-11-07 | Coway Co., Ltd. | Water purifier having composite filter |
| KR20240100561A (en) * | 2022-12-22 | 2024-07-02 | 주식회사 코텍코리아 | Filter module including post-processing filter function |
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| CN201320422Y (en) * | 2008-12-04 | 2009-10-07 | 宁波灏钻科技有限公司 | Rear sterilizing filter element |
| CN101734808A (en) * | 2008-11-11 | 2010-06-16 | 熊津化学有限公司 | Reverse osmosis water purifier having simple filter configuration |
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| KR100494593B1 (en) | 2002-11-13 | 2005-06-13 | 웅진코웨이주식회사 | Reverse osmotic water purifier having filter housing of unity type |
| KR101869799B1 (en) * | 2016-11-30 | 2018-07-20 | 금오공과대학교 산학협력단 | manufacturing method of forward osmosis filter using carbon nano-material |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN102026712A (en) * | 2008-05-15 | 2011-04-20 | 熊津豪威株式会社 | Spiral wound filter |
| CN101734808A (en) * | 2008-11-11 | 2010-06-16 | 熊津化学有限公司 | Reverse osmosis water purifier having simple filter configuration |
| CN201320422Y (en) * | 2008-12-04 | 2009-10-07 | 宁波灏钻科技有限公司 | Rear sterilizing filter element |
| CN202705130U (en) * | 2012-07-06 | 2013-01-30 | 慈溪市润鑫电器有限公司 | Combined type filter element of water purifier |
| KR20170052711A (en) * | 2015-11-03 | 2017-05-15 | 금오공과대학교 산학협력단 | Hybrid forward osmosis membrane for seawater desalination, Filter containing the same, and Forward osmosis type seawater desalination system using the same |
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