TW201138638A - Antibacterial treating agent for processing water, method for producing antibacterial treating agent for processing water and method for processing water - Google Patents

Antibacterial treating agent for processing water, method for producing antibacterial treating agent for processing water and method for processing water Download PDF

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TW201138638A
TW201138638A TW100108461A TW100108461A TW201138638A TW 201138638 A TW201138638 A TW 201138638A TW 100108461 A TW100108461 A TW 100108461A TW 100108461 A TW100108461 A TW 100108461A TW 201138638 A TW201138638 A TW 201138638A
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silver
water
antibacterial
formula
agent
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TW100108461A
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Chinese (zh)
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TWI482592B (en
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Koji Sugiura
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Toagosei Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/50Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
    • C02F1/505Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment by oligodynamic treatment
    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01NPRESERVATION OF BODIES OF HUMANS OR ANIMALS OR PLANTS OR PARTS THEREOF; BIOCIDES, e.g. AS DISINFECTANTS, AS PESTICIDES OR AS HERBICIDES; PEST REPELLANTS OR ATTRACTANTS; PLANT GROWTH REGULATORS
    • A01N59/00Biocides, pest repellants or attractants, or plant growth regulators containing elements or inorganic compounds
    • A01N59/16Heavy metals; Compounds thereof
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/42Treatment of water, waste water, or sewage by ion-exchange

Abstract

Provided of this invention are an antibacterial treating agent, which can dissolve out the decided proper concentration of silver ions and give antibacterial treatments for fresh water such as drinking water or circulating water etc., and sustain the ability for dissolving out the silver ions chronically, and a method for processing water, which used the said antibacterial treating agent. An antibacterial treating agent for processing water, characterized in consisting of resin compositions, which contain resins having a standard moisture percentage of 1 to 10 weight% ruling by JIS L 0105: 2006, and 1 to 30 weight% of silver substituted phosphoric acid zirconium represented by formula [1] as antibacterial agent, AgaMbZrcHfd(PO4)3.NH2O [1] in formula [1], M is at least one ion choose from the group, which consists of alkali metal ions, alkali earth metal ions, ammonium ions, hydrogen ions, and oxonium ions, a, b, and c are independent integers individually, d is 0 or a integer, n is 0or a integer smaller than 2, all a, b, c, and d satisfy the relationships of the formula [A], when the valence number of M is 1, they satisfy the formula [B], when the valence number of M is 2, they satisfy the formula [C]. 1.75 < c+d < 2.25 [A] a+b+4 (c+d)=9 [B] a+2b+4(c+d)=9 [C]

Description

201138638 六、發明說明: 【發明所屬之技術領域】 本發明係關於一種水處理用抗菌處理劑及其製造方 法,前述水處理用抗菌處理劑,其特徵爲由含有特定之標 準水分百分率之樹脂與特定之銀系無機抗菌劑的樹脂組成 物而成。又關於一種水處理方法,其係藉由將本發明之水 處理用抗菌處理劑與各種水接觸進行水之抗菌處理。 【先前技術】 作爲水處理用抗菌劑,因用途或對象水、通水量等不 同已有種種業經提案。例如:作爲水處理用,業經提案有 一種水處理用載銀抗菌劑,其係於不破壞沸石結晶構造程 度之pH的處理液中,將銀離子支載於可固液分離之任意大 小的沸石粒子或沸石系加工品而成(參照例如專利文獻 1 )。又,業經提案有藉由將一種玻璃水處理劑,其係由組 成中含有一價銀離子之溶解性玻璃而成,添加於冷卻塔、 貯水槽、游泳池、太陽能系統、及灌溉用水等,以防止黏 質物(slime )或藻類等之水生細菌及水生生物之發生(參 照例如專利文獻2 )。 又,業經提案有一種抗菌性水處理用媒體,其係由纖 維中含有抗菌劑之複數條短纖維相互纏繞之纖維塊而成, 前述抗菌劑係將具有抗菌性能之金屬或金屬離子支載於磷 酸鹽而得到(參照例如專利文獻3)。 又,揭示有一種水處理用濾器,其係用於自水去除污 201138638 染物質之水處理用濾器,其特徵爲將一倂支載有活性碳與 具有抗菌性之金屬離子的沸石,藉由高分子量多孔質聚合 物而成之黏結劑(b i n d e 1·)予以固化(參照例如專利文獻 4 );或一種淨水劑,其係由支載、鍵結有銀之磷酸銷化合 物與活性碳而成之抗菌性優良者(參照例如專利文獻5 )。 其他’業經提案有一種抑制水生菌增殖之抗菌樹脂成 形物’其特徵爲將含有銀系無機抗菌劑、鹼金屬及/或鹼土 金屬之鹵鹽、及聚烯烴系樹脂之混合物熔融混合並形成樹 脂組成物,且藉由對此施予水處理,使樹脂組成物成爲細 微多孔。顯示使用此技術將銀沸石混合於聚烯烴者,相較 於單純將銀沸石混合於聚醯胺者,高濃度之銀持續溶出(參 照例如專利文獻6 )。 先前技術文獻 專利文獻 專利文獻1:日本特開2001-278715號公報; 專利文獻2 :日本特開昭62-2 1 0098號公報; 專利文獻3 :日本特開平8- 1 55480號公報; 專利文獻4 :日本特開2 〇 〇 6 - 9 5 5 1 7號公報; 專利文獻5 :日本特開平7_2 2298 3號公報; 專利文獻6:日本特開2008-174576號公報。 【發明內容】 發明欲解決之課題 若直接將如專利文獻1記述之沸石粒子添加於水中, 201138638 無論如何使粒子硬化亦經不起長期使用,除了有效成分之 銀以外,有沸石粉末之掉粉或脫落,且因銀溶出量之變動 大,故銀濃度不安定。另一方面,如專利文獻2記述之溶 解性玻璃亦相同,除了有效成分之銀以外,有玻璃成分之 溶解,且水溶液中之銀濃度難以控制。即使水未經或較少 更換,玻璃亦持續溶解,故具有因銀持續繼續溶解而使處 理水中之銀濃度顯著增加的問題。對於飲用用途或循環水 等之清淨水而言,最佳係僅適量溶出抗菌成分之微量銀離 子,並不溶出、溶解除必要外之其他物質者。 又,專利文獻3記述之發明中,即使將銀支載於藉由 抗菌劑與環境之平衡而得以控制溶出銀濃度之非離子交換 體之磷酸鹽,亦無法控制銀溶出濃度。又,短纖維具有絲 線鬆脫而混入水中之問題。 又,亦有如專利文獻4、專利文獻5使用活性碳之提 案。若使用活性碳,除了爲黑色以外,且亦一倂吸附污染 物質以外者,故用途受到限定,並具有若活性碳之吸附能 飽和時會將污染物質釋出於水中之問題。 專利文獻6記述之發明中,因聚烯烴之親水性低,藉 由水處理所得到之微細多孔僅非常鄰近於成形品之表面, 故僅表面附近之銀可被利用,且即使可得到初期之持續性 亦無法得到長期之持續性。又,因銀沸石之細孔大,離子 交換性之控制能絕對稱不上精密,故溶.出銀濃度稱不上得 以被嚴密控制。 201138638 如此,雖得以短期表現抗菌性,但於水中之長期持續 性與一定銀濃度之控制並非容易,故適合水處理用之抗菌 劑的技術尙未經揭示。 本發明之課題係提供一種水處理用抗菌處理劑,其係 得以對於飲用水或循環水等之清淨水(f r e s h w a t e 1·),溶出 無過與不及之一定濃度的銀離子並予以抗菌處理,且銀溶 出能得以長期持續;一種水處理用抗菌處理劑之製造方 法;以及一種使用該水處理用抗菌處理劑之水處理方法。 解決課題之手段 本發明之上述課題係藉由下述〈1〉 、 〈6〉、及〈7〉 記述之手段予以解決。與較佳實施形態之〈2〉〜〈5〉一 倂記述於下。 〈1〉一種水處理用抗菌處理劑,其特徵爲由含有·· ns L 0 1 05 : 2006規定之標準水分百分率爲1〜1〇重量%之樹脂、 及1〜30重量%之作爲抗菌劑並以式〔1〕表示之經銀取代 之磷酸銷的樹脂組成物而成,BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an antibacterial treatment agent for water treatment and a method for producing the same, and the antibacterial treatment agent for water treatment characterized by a resin containing a specific standard moisture percentage and A resin composition of a specific silver-based inorganic antibacterial agent. Further, a water treatment method for performing an antibacterial treatment of water by bringing the antibacterial treatment agent for water treatment of the present invention into contact with various kinds of water. [Prior Art] As an antibacterial agent for water treatment, various applications have been proposed depending on the use, the target water, and the amount of water to be used. For example, as a water treatment, a silver-loaded antibacterial agent for water treatment is proposed, which is supported in a treatment liquid having a pH which does not impair the crystal structure of the zeolite, and supports silver ions in a zeolite of any size capable of solid-liquid separation. The pellet or the zeolite is processed (see, for example, Patent Document 1). Further, it has been proposed to add a glass water treatment agent to a cooling tower, a water storage tank, a swimming pool, a solar energy system, and irrigation water by using a soluble glass containing monovalent silver ions in the composition. The occurrence of aquatic bacteria and aquatic organisms such as slime or algae is prevented (see, for example, Patent Document 2). Further, there has been proposed an antibacterial water treatment medium which is obtained by a fiber block in which a plurality of short fibers containing an antibacterial agent are intertwined with each other, and the antibacterial agent supports a metal or metal ion having an antibacterial property. It is obtained by phosphate (refer to, for example, Patent Document 3). Further, there is disclosed a water treatment filter for use in a water treatment filter for decontaminating 201138638 dyed material from water, characterized in that a zeolite supporting activated carbon and an antibacterial metal ion is used. A binder (binde 1·) made of a high molecular weight porous polymer is cured (see, for example, Patent Document 4); or a water purifying agent which is supported by a phosphoric acid compound and activated carbon bonded with silver. It is excellent in antibacterial property (see, for example, Patent Document 5). Others have proposed an antibacterial resin molded article for inhibiting the growth of aquatic bacteria, which is characterized in that a mixture containing a silver-based inorganic antibacterial agent, an alkali metal and/or an alkaline earth metal halide salt, and a polyolefin resin is melt-mixed to form a resin. The composition was subjected to water treatment to make the resin composition finely porous. When silver zeolite is mixed with polyolefin by this technique, a high concentration of silver is continuously eluted as compared with a case where silver zeolite is simply mixed with polyamine (see, for example, Patent Document 6). CITATION LIST Patent Literature Patent Literature 1: Japanese Laid-Open Patent Publication No. 2001-278715; Patent Document 2: Japanese Laid-Open Patent Publication No. Hei. (4) Japanese Patent Laid-Open Publication No. Hei. No. Hei. No. Hei. No. Hei. No. 2008-174576. DISCLOSURE OF THE INVENTION PROBLEM TO BE SOLVED BY THE INVENTION If zeolite particles described in Patent Document 1 are directly added to water, 201138638 will not be able to withstand long-term use in any case, and in addition to the silver of the active ingredient, there is a powder of zeolite powder. Or shedding, and the silver concentration is not stable due to the large variation in the amount of silver dissolved. On the other hand, the dissolvable glass described in Patent Document 2 is also the same, and in addition to the silver of the active ingredient, the glass component is dissolved, and the concentration of silver in the aqueous solution is difficult to control. Even if the water is not replaced or replaced, the glass continues to dissolve, so that the silver concentration in the treated water is remarkably increased due to the continued dissolution of the silver. For clean water such as drinking water or circulating water, it is preferable to dissolve a small amount of silver ions of the antibacterial component in an appropriate amount, and do not dissolve or dissolve other substances other than necessary. Further, in the invention described in Patent Document 3, even if the silver is supported on the phosphate of the non-ion exchanger which controls the concentration of the eluted silver by the balance between the antibacterial agent and the environment, the silver elution concentration cannot be controlled. Further, the short fibers have a problem that the threads are loosened and mixed into the water. Further, there are proposals for using activated carbon in Patent Document 4 and Patent Document 5. If activated carbon is used, it is not limited to black, and it is also used for adsorption of pollutants. Therefore, the use is limited, and there is a problem that if the adsorption of activated carbon is saturated, the pollutants are released into the water. In the invention described in Patent Document 6, since the hydrophilicity of the polyolefin is low, the fine pores obtained by the water treatment are only very close to the surface of the molded article, so that only the silver in the vicinity of the surface can be utilized, and even if the initial stage can be obtained Sustainability cannot be sustained in the long run. Further, since the fine pores of the silver zeolite are large, the control of the ion exchange property can never be called precision, so the concentration of the dissolved silver can not be strictly controlled. 201138638 In this way, although the antibacterial property is exhibited in the short term, the long-term persistence in water and the control of a certain silver concentration are not easy, so the technique suitable for the antibacterial agent for water treatment has not been disclosed. An object of the present invention is to provide an antibacterial treatment agent for water treatment, which is capable of dissolving a certain concentration of silver ions in a clean water (freshwate 1·) such as drinking water or circulating water, and performing antibacterial treatment. And silver dissolution can be sustained for a long period of time; a method for producing an antibacterial treatment agent for water treatment; and a water treatment method using the antibacterial treatment agent for water treatment. Means for Solving the Problems The above problems of the present invention are solved by the following descriptions of <1>, <6>, and <7>. The <2> to <5> of the preferred embodiment are described below. <1> An antibacterial treatment agent for water treatment, which comprises a resin having a standard moisture percentage of 1 to 1% by weight, and 1 to 30% by weight, as an antibacterial agent, as specified in ns L 0 105 :2006 And a resin composition of a phosphoric acid-substituted phosphoric acid pin represented by the formula [1],

AgaMbZi-cHfd(P〇〇3. nH2〇 〔1〕 式〔1〕中,Μ爲至少一種選自於鹼金屬離子、鹼土金屬離 子、銨離子、氫離子及經離子所構成之群組的離子;a、b 及c分別爲獨立之整數;d爲〇或整數;n爲〇或2以下之 整數;a、b、c、及d係滿足於式〔a〕之關係;μ爲1價 時,係滿足於式〔Β〕;Μ爲2價時,係滿足於式〔C〕。 1.75&lt; c + d&lt; 2.25 〔A] 201138638 a+b+4(c+d)=9 〔B〕 a+2b+4(c+d) = 9 [ C ) 〈2〉如上述〈1〉記述之水處理用抗菌處理劑,宜中軟 經銀取代之磷酸鉻的銀含有率爲4〜13重量%。 〈3〉如上述〈1〉記述之水處理用抗菌處理劑,其中前% 處理劑之比表面積爲5〜100cm2/g。 〈4〉如上述〈1〉記述之水處理用抗菌處理劑,其中% 成 前述樹脂組成物的樹脂之50〜99重量%爲聚酿胺樹脂。 〈5〉如上述〈4〉記述之水處理用抗菌處理劑,其中前述 聚醯胺樹脂爲耐綸 6。 〈6〉一種如上述〈1〉至〈5〉中任一項記述之水處理用抗 菌處理劑之製造方法,其係包含將前述抗菌劑與前述樹脂 予以混合之步驟。 〈7〉一種水處理方法,其係包含使如上述〈1〉至〈5〉中 任一項記述之水處理用抗菌處理劑與水接觸之步驟。 發明之效果 根據本發明,得以提供一種水處理用抗菌處理劑,其 係得以對於飮用水或循環水等之清淨水,溶出無過與不及 之一定濃度的銀離子並予以抗菌處理,且銀溶出能得以長 期持續;一種水處理用抗菌處理劑之製造方法;以及一種 使用該水處理用抗菌處理劑之水處理方法。 【實施方式】 發明之實施形態 201138638 以下,針對本發明加以詳細說明。 又,本發明中,表示數値範圍之「下限〜上限」之記 述係表示「下限以上、上限以下」;「上限〜下限」之記 述係表示「上限以下、下限以上」。即,表示包含上限及 下限之數値範圍。 (水處理用抗菌處理劑) 本發明之水處理用抗菌劑,其特徵爲由含有:標準水 分百分率1〜10重量%之樹脂、及相對於樹脂組成物之全 重量之1〜30重量%之下述式〔1〕所示之特定之經銀取代 之磷酸锆(以下,有時亦僅稱「經銀取代之磷酸鉻j )的 樹脂組成物而成,AgaMbZi-cHfd (P〇〇3. nH2〇 [1] In the formula [1], hydrazine is at least one selected from the group consisting of alkali metal ions, alkaline earth metal ions, ammonium ions, hydrogen ions, and ions. ; a, b, and c are independent integers; d is 〇 or an integer; n is 〇 or an integer less than 2; a, b, c, and d are satisfied with the relationship of the formula [a]; , is satisfied by the formula [Β]; when Μ is 2, it satisfies the formula [C]. 1.75 &lt; c + d &lt; 2.25 [A] 201138638 a+b+4(c+d)=9 [B] a+2b+4(c+d) = 9 [ C ) <2> The antibacterial treatment agent for water treatment described in <1> above, the silver content of the chromium phosphate substituted with soft silver is preferably 4 to 13 by weight. %. <3> The antibacterial treatment agent for water treatment described in the above <1>, wherein the pre-% treatment agent has a specific surface area of 5 to 100 cm 2 /g. (4) The antibacterial treatment agent for water treatment described in the above <1>, wherein 50% to 99% by weight of the resin of the resin composition is a polyamine resin. <5> The antibacterial treatment agent for water treatment according to the above <4>, wherein the polyamine resin is nylon 6. The method for producing an antibacterial treatment agent for water treatment according to any one of the above items <1> to <5>, which comprises the step of mixing the antibacterial agent with the resin. (7) A water treatment method comprising the step of bringing the antibacterial treatment agent for water treatment described in any one of the above <1> to <5> into contact with water. Advantageous Effects of Invention According to the present invention, it is possible to provide an antibacterial treatment agent for water treatment which is capable of dissolving a certain concentration of silver ions in an aqueous solution such as hydrazine water or circulating water, and performing antibacterial treatment, and silver. The dissolution can be sustained for a long period of time; a method for producing an antibacterial treatment agent for water treatment; and a water treatment method using the antibacterial treatment agent for water treatment. [Embodiment] Embodiments of the Invention 201138638 Hereinafter, the present invention will be described in detail. Further, in the present invention, the description of the "lower limit to the upper limit" indicating the range of the number is indicated as "above the lower limit and the upper limit"; and the description of the "upper limit to the lower limit" means "the upper limit is equal to or lower than the lower limit". That is, the range including the upper limit and the lower limit is indicated. (Antibacterial treatment agent for water treatment) The antibacterial agent for water treatment of the present invention is characterized in that it contains a resin having a standard moisture percentage of 1 to 10% by weight and 1 to 30% by weight based on the total weight of the resin composition. a specific silver-substituted zirconium phosphate (hereinafter, sometimes referred to as "silver-substituted chromium phosphate j") represented by the following formula [1],

AgaMbZrcHfd(P〇4)3 · nH2〇 〔 1〕 上述式〔1〕中,Μ爲一種以上選自於鹼金屬離子、鹼土金 屬離子、銨離子、氫離子及經離子之群組的離子;a、b及 c分別爲獨立之整數;d爲0或整數;η爲0或2以下之整 數; a ' b ' c 、及 d係滿足於式〔 A〕之 關係;Μ 爲1價時 係滿足於式 〔B ; ];M爲2價時: ,係滿 足於式〔 c〕。 1.75 &lt; c + d &lt; 2.25 [ A〕 a + b + ^ “ c + d ) = 9 ( B〕 a + 2b + 4( c + d ) = 9 C C〕 本發明中所謂水處理,意指針對於直接或經調理、混 合、溶解等之步驟後而被攝取至活體內的水(飲用水)、 或循環冷卻水或各種觀賞用水、食品藥品等之生產線清淨 201138638 水等,被要求爲無害、清潔之水(清淨水) 於本發明中,係對於上述之水溶出無過與不 的銀離子並予以抗菌處理。又,所謂抗菌處 細菌增殖之處理。 本發明之水處理用抗菌處理劑,係得以 之水中所含的離子濃度維持一定之銀濃度, 銀溶出持續性。因此,對於飲用水或循環水 即使因通水或水之消費等而有水之更換,得 對於抗菌作用而言無過與不及之銀離子,且 菌效果。 本發明使用之經銀取代之磷酸锆係一種 劑,且較佳者係成爲其主鏈之磷酸鉻爲具有 造之結晶質。隣酸銷有非晶質者與成爲2次 3次元網孔構造之結晶質者。其中又以成爲 造之結晶質磷酸鉻,因耐熱性、耐藥品性、 及低熱膨脹性等優異故較佳。其中又以藉由 方晶之磷酸鉻以銀離子取代所得到之經銀取 不僅表現優異抗菌效果,且因耐久性或離子 加工時之變色或安全性亦優異,故進一步較 作爲本發明中使用之經銀取代之磷酸鉻 法,可藉由對於下述式〔2〕所示之磷酸锆 莫耳,使用含有式〔2〕之係數bl乘以0.6〜 硝酸銀的水溶液予以離子交換後並予以熱處 進行抗菌,而 及之一定濃度 理,意指抑制 根據處理對象 且具有長期之 等之清淨水, 以於水中實現 維持長期之抗 銀系無機抗菌 3次元網孔構 元層狀構造或 3次元網孔構 耐放射線性、 對於六平面立 代之磷酸锆, 選擇性、樹脂 佳。 的具體合成方 :合物,其每1 0.99之當量之 理而得到。 -10- 201138638 N a b 丨 A c 丨 Zr e H f r (P 〇 4) 3 · η Η 2 Ο 〔2〕 式〔2〕中’ A係銨離子及/或氫離子,bl、cl、e、及f各自 爲獨立之整數’且1.75&lt; (e+f) &lt;2.25,並爲滿足bl+cl + 4(e+f)=9 之數。 ' 式〔2〕所示之磷酸銷化合物之合成方法,可列舉使各 種原料於水溶液中反應之溼式法或水熱法。式〔2〕中A係 銨離子之磷酸銷化合物,可藉由將含有指定量之鉻化合 物、氨或其鹽、草酸或其鹽、或磷酸或其鹽等之水溶液, 以氫氧化鈉(以下,有時亦稱作「苛性鹼」)或氨水將pΗ 調整爲1〜4左右後’以70°C以上之溫度加熱而合成得到。 又,前述加熱溫度較佳爲2 0 (TC以下。 又,式〔2〕中A係氫離子之磷酸锆化合物,可藉由將 含有指定量之銷化合物、草酸或其鹽、或磷酸或其鹽等之 水溶液,以苛性鹼將p Η調整爲1〜4左右後,以7 0。(:以上 之溫度加熱而得到之磷酸銷,進一步於鹽酸、硝酸、或硫 酸等之水溶液中攪拌而使支載氫離子而合成得到。又,前 述加熱溫度較佳爲200°C以下。 又,氫離子之支載,可與藉由硝酸銀之銀離子之支載 同時實施,或亦可於銀離子支載後實施。藉由將合成後之 磷酸鉻化合物,進一步予以濾出並水洗至指定之導電度爲 止後,予以乾燥並輕輕粉碎,可得到白色之微粒子磷酸锆 化合物。又,若係於超過100°C之加壓下合成之水熱法,合 成式〔2〕所示之磷酸锆化合物可不使用草酸或其鹽。 -11 - 201138638 可作爲式〔2〕所示之磷酸锆化合物之合成原料使用的 磷酸鉻化合物,可列舉水溶性或酸可溶性之锆鹽。例示有 例如:硝酸鉻、醋酸锆、硫酸鉻、鹼性硫酸鍩、硫酸氧锆、 及氧氯化鉻等,且若考慮反應性或經濟性等,氧氯化锆較 佳。 可作爲式〔2〕所示之磷酸锆化合物之合成原料使用的 給化合物,有水溶性或酸可溶性之給鹽,例示有例如:氯 化鈴、氧氯化鈴、及乙氧化飴等,亦例示有含有給之銷化 合物。相對於锆化合物所含有之給含有率較佳爲〇.丨〜5莫 耳%、更佳爲使用如此含有微量給之氧氯化鉻。 可作爲式〔2〕所示之磷酸锆化合物之合成原料的草酸 或其鹽,例示有:草酸二水合物、草酸鈉、草酸銨、草酸 氫鈉、及草酸氫銨等,且較佳爲草酸二水合物。 可作爲式〔2〕所示之磷酸锆化合物之合成原料使用的 氨或其鹽’例示有:氯化銨、硝酸銨、硫酸銨、氨水、草 酸銨、及磷酸銨等,且較佳爲氯化銨或氨水。 可作爲式〔2〕所示之磷酸锆化合物之合成原料使用的 磷酸或其鹽,較佳爲可溶性或酸可溶性之鹽,具體例示有: 磷酸、磷酸鈉、磷酸氫鈉、磷酸氫銨、及磷酸銨等,且更 佳爲磷酸。又,較佳爲以60〜85重量%左右之濃度的水溶 液作爲該磷酸之濃度。 合成式〔2〕所示之磷酸銷化合物時之磷酸或其鹽與锆 化合物的莫耳比(以鉻化合物爲丨),較佳爲大於1 5未滿 -12- 201138638 2、更佳爲1.51以上未滿1.71、進一步更佳爲1.52以上1.67 以下’特別佳爲1 · 5 2以上1 · 6 5以下。 又,合成式〔2〕所示之磷酸銷時之磷酸或其鹽與氨或 其鹽的莫耳比(以氨或其鹽爲1),較佳爲〇.3〜10、更佳 爲1〜1 0 '特別佳爲2〜5。 合成式〔2〕所示之磷酸鍩時之磷酸或其鹽與草酸或其 鹽的莫耳比(以草酸或其鹽爲1),較佳爲1〜6、更佳爲 1_5〜5、進一步更佳爲1.51〜4、特別佳爲1.52〜3.5。即, 式〔2〕所示之磷酸鉻化合物,藉由含有草酸或其鹽之溼式 法或水熱法,得以較佳合成。 水熱法時不必含有草酸或其鹽,另一方面,溼式法容 易控制粒徑,可得到中値粒徑爲〇. 1 μ m以上5 // m以下範 圍之粒徑分布一致的磷酸锆化合物之結晶。 合成式〔2〕所示之磷酸鍩化合物時之反應漿料中的固 體成分濃度’較佳爲3重量%以上,若就經濟性等考慮效 率時’更佳爲7〜20重量%之間。 合成式〔2〕所示之磷酸銷化合物時之pH,較佳爲1 以上4以下、更佳爲ι·3〜35、進一步更佳爲ι.8〜3〇、特 別佳爲2.0〜3.0。爲調整此PH,較佳爲使用氫氧化鈉、氫 氧化鉀或氨水等,更佳爲使用氫氧化鈉。 又’合成式〔2〕所示之磷酸锆時之合成溫度,較高則 反應快’得以確實進行故較佳,但另一方面,合成裝置之 Μ ^費用或用於加熱之能源,則以將合成溫度設定較低較 -13- 201138638 爲有利。較佳爲下限70°C以上、更佳爲80t以上、進一步 更佳爲9 0 °C以上、特別佳爲9 5 °C以上。又,作爲合成溫度 之上限’較佳爲150°C以下、更佳爲1201以下。 合成式〔2〕所示之磷酸锆化合物時,較佳爲原料被均 質地予以混合’且予以攪拌以使反應得以均勻進行。 式〔2〕所示之磷酸鉻化合物之合成時間係因合成溫度 而異。作爲本發明中使用之碟酸銷化合物之合成時間,例 如較佳爲4小時〜7 2時間、更佳爲8小時〜7 2小時、特別 佳爲1Ό小時〜48小時。 式〔2〕所示之磷酸銷化合物之粒徑係藉由雷射繞射式 粒徑分布儀’經由體積基準之測定以定義中値粒徑。式〔2〕 所示之磷酸锆化合物之中値粒徑,較佳爲更佳 爲0.1〜4ym、進一步更佳爲〇2〜3ym、特別佳爲0.3〜2 # m。又,若考慮加工成各種製品之加工性則非僅中値粒 徑,最大粒徑亦重要。因此,式〔2〕所示之磷酸鉻化合物 之最大粒徑,較佳爲成爲10μιη以下、更佳爲6&quot;m以下、 特別佳爲4从m以下。下限値〇. i从m以上較佳。 可用以作爲本發明中使用之經銀取代之磷酸锆化合物 的原料之式〔2〕所不的磷酸銷化合物,具體可例示下述者。AgaMbZrcHfd(P〇4)3 · nH2〇[1] In the above formula [1], hydrazine is one or more ions selected from the group consisting of alkali metal ions, alkaline earth metal ions, ammonium ions, hydrogen ions, and ions; , b and c are independent integers; d is 0 or an integer; η is an integer of 0 or less; a ' b ' c and d are satisfied with the relationship of the formula [A]; In the formula [B; ]; M is a divalent:: is satisfied by the formula [c]. 1.75 &lt; c + d &lt; 2.25 [ A] a + b + ^ " c + d ) = 9 ( B ] a + 2b + 4( c + d ) = 9 CC] In the present invention, the so-called water treatment, meaning pointer It is required to clean the water (drinking water) that has been ingested into the living body directly after conditioning, mixing, dissolving, etc., or circulating cooling water or a variety of ornamental water, food and medicine, etc., 201138638 water, etc., is required to be harmless, Clean water (purified water) In the present invention, the silver ions which are not dissolved in the above-mentioned water are subjected to antibacterial treatment, and the antibacterial treatment of bacteria is also carried out. The antibacterial treatment agent for water treatment of the present invention The concentration of ions contained in the water is maintained at a certain concentration of silver, and the dissolution of silver is continued. Therefore, for the drinking water or circulating water, even if water is replaced by water or water consumption, it is necessary for the antibacterial effect. Silver ions are not incompatible with the effect of bacteria. The silver-substituted zirconium phosphate-based agent used in the present invention, and preferably the chromium phosphate in its main chain has a crystalline crystal. Crystals and become 2 times 3 It is a crystallized structure of a meta-mesh structure, and it is preferably made of crystalline chromium phosphate which is excellent in heat resistance, chemical resistance, and low thermal expansion property, among which silver is made of chromium crystals by cubic crystals. The silver extraction obtained by ion substitution not only exhibits an excellent antibacterial effect, but also is excellent in discoloration or safety during durability or ion processing, so that it can be further used as a silver-substituted chromium phosphate method used in the present invention. For the zirconium phosphate molar represented by the following formula [2], an aqueous solution containing the coefficient bl of the formula [2] and multiplied by 0.6 to silver nitrate is ion-exchanged and subjected to heat treatment for antibacterial treatment, and a certain concentration is determined. It means suppressing the clean water according to the treatment object and having a long-term basis, in order to achieve long-term anti-silver inorganic antibacterial 3-dimensional mesh structure layer structure or 3-dimensional mesh structure radiation resistance in the water, for six planes Instead of zirconium phosphate, the selectivity, the resin is good, the specific synthesis of the compound, which is obtained for every 0.99 equivalents. -10- 201138638 N ab 丨A c 丨Zr e H fr (P 〇4) 3 · η Η 2 Ο [2] In the formula [2], 'A series ammonium ion and/or hydrogen ion, bl, cl, e, and f are each an independent integer' and 1.75 &lt; (e+f) &lt; 2.25, And a method of synthesizing a phosphoric acid pin compound represented by the formula [2], and a wet method or a hydrothermal method for reacting various raw materials in an aqueous solution The phosphoric acid compound of the A-based ammonium ion in the formula [2] may be sodium hydroxide by using an aqueous solution containing a specified amount of a chromium compound, ammonia or a salt thereof, oxalic acid or a salt thereof, or phosphoric acid or a salt thereof. Hereinafter, it may be referred to as "caustic alkali" or ammonia water, and pΗ is adjusted to about 1 to 4, and then it is synthesized by heating at a temperature of 70 ° C or higher. Further, the heating temperature is preferably 20 or less (TC or less). Further, the zirconium phosphate compound of the A-type hydrogen ion in the formula [2] may contain a specified amount of a pin compound, oxalic acid or a salt thereof, or phosphoric acid or An aqueous solution of a salt or the like is adjusted to have a pH of about 1 to 4 with caustic alkali, and then the phosphoric acid pin obtained by heating at a temperature of the above is further stirred in an aqueous solution of hydrochloric acid, nitric acid or sulfuric acid. The hydrogen ion is supported and synthesized. Further, the heating temperature is preferably 200 ° C or less. Further, the hydrogen ion support may be carried out simultaneously with the support of the silver ion by silver nitrate, or may be performed on the silver ion branch. After the loading, the synthesized chromium phosphate compound is further filtered and washed with water to a predetermined conductivity, dried, and lightly pulverized to obtain a white fine particle zirconium phosphate compound. The hydrothermal method synthesized under the pressure of 100 ° C can synthesize the zirconium phosphate compound represented by the formula [2] without using oxalic acid or a salt thereof. -11 - 201138638 It can be used as a synthetic raw material of the zirconium phosphate compound represented by the formula [2]. Phosphorus used Examples of the chromium compound include water-soluble or acid-soluble zirconium salts, and examples thereof include chromium nitrate, zirconium acetate, chromium sulfate, basic barium sulfate, zirconyl sulfate, and chromium oxychloride, and if reactivity or economy is considered. The oxyzirconium oxychloride is preferred as the compound for use as a synthetic raw material of the zirconium phosphate compound represented by the formula [2], and is a water-soluble or acid-soluble salt, and is exemplified by, for example, chlorinated bell and oxychloride. The compounding bell, the cerium oxide, and the like are also exemplified to contain the compound which is supplied with the compound. The content of the compound contained in the zirconium compound is preferably 〇.丨5 5 mol%, more preferably the oxygen is used in such a manner. The oxalic acid or a salt thereof which can be used as a synthetic raw material of the zirconium phosphate compound represented by the formula [2], and examples thereof include oxalic acid dihydrate, sodium oxalate, ammonium oxalate, sodium hydrogen oxalate, and ammonium hydrogen oxalate, and the like. An oxalic acid dihydrate is preferred. The ammonia or a salt thereof which can be used as a synthetic raw material of the zirconium phosphate compound represented by the formula [2] is exemplified by ammonium chloride, ammonium nitrate, ammonium sulfate, ammonia water, ammonium oxalate, and phosphoric acid. Ammonium, etc., and preferably chlorine Ammonium or ammonia water. Phosphoric acid or a salt thereof which can be used as a synthetic raw material of the zirconium phosphate compound represented by the formula [2] is preferably a soluble or acid-soluble salt, and specific examples thereof include phosphoric acid, sodium phosphate, sodium hydrogen phosphate, and phosphoric acid. Ammonium hydroxide, ammonium phosphate, etc., and more preferably phosphoric acid. Further, an aqueous solution having a concentration of about 60 to 85% by weight is preferably used as the concentration of the phosphoric acid. Phosphoric acid in the case of synthesizing a phosphoric acid compound represented by the formula [2] Or the molar ratio of the salt thereof to the zirconium compound (the chromium compound is ruthenium), preferably more than 1 5 under -12-201138638 2. More preferably 1.51 or more and less than 1.71, further preferably 1.52 or more and 1.67 or less. In particular, it is preferably 1 · 5 2 or more and 1 6 5 or less. Further, the molar ratio of phosphoric acid or a salt thereof to ammonia or a salt thereof in synthesizing a phosphoric acid pin represented by the formula [2] (1 or 6 with ammonia or a salt thereof) Preferably, it is 〇. 3 to 10, more preferably 1 to 1 0 'particularly preferably 2 to 5. The molar ratio of the phosphoric acid or the salt thereof to the oxalic acid or the salt thereof in the synthesis of the hydrazine phosphate represented by the formula [2] (the oxalic acid or the salt thereof is 1), preferably 1 to 6, more preferably 1 to 5 to 5, further More preferably, it is 1.51 to 4, and particularly preferably 1.52 to 3.5. Namely, the chromium phosphate compound represented by the formula [2] can be preferably synthesized by a wet method or a hydrothermal method containing oxalic acid or a salt thereof. In the hydrothermal method, it is not necessary to contain oxalic acid or a salt thereof. On the other hand, the wet method can easily control the particle diameter, and a zirconium phosphate having a uniform particle size distribution in the range of μ. 1 μ m or more and 5 // m or less can be obtained. Crystallization of the compound. When the yttrium phosphate compound represented by the formula [2] is synthesized, the concentration of the solid content in the reaction slurry is preferably 3% by weight or more, and more preferably 7 to 20% by weight in consideration of economy and the like. The pH at the time of synthesizing the phosphoric acid pin compound represented by the formula [2] is preferably 1 or more and 4 or less, more preferably 1⁄3 to 35, still more preferably 1 to 3 Å, and particularly preferably 2.0 to 3.0. In order to adjust this pH, it is preferred to use sodium hydroxide, potassium hydroxide or ammonia water, and it is more preferred to use sodium hydroxide. Further, when the synthesis temperature of the zirconium phosphate represented by the formula [2] is higher, the reaction is faster, and it is preferable to carry out the reaction. However, on the other hand, the cost of the synthesis device or the energy for heating is It is advantageous to set the synthesis temperature lower than -13-201138638. The lower limit is preferably 70 ° C or higher, more preferably 80 t or higher, still more preferably 90 ° C or higher, and particularly preferably 95 ° C or higher. Further, the upper limit ' of the synthesis temperature is preferably 150 ° C or less, more preferably 1201 or less. In the case of synthesizing the zirconium phosphate compound represented by the formula [2], it is preferred that the raw materials are uniformly mixed 'and stirred to allow the reaction to proceed uniformly. The synthesis time of the chromium phosphate compound represented by the formula [2] varies depending on the synthesis temperature. The synthesis time of the acid-storing compound used in the present invention is, for example, preferably 4 hours to 7 2 hours, more preferably 8 hours to 7 2 hours, particularly preferably 1 hour to 48 hours. The particle size of the phosphoric acid pin compound represented by the formula [2] is determined by a volume measurement based on a laser diffraction type particle size distribution analyzer to define a median particle diameter. The zirconium phosphate compound represented by the formula [2] preferably has a ruthenium particle diameter of 0.1 to 4 μm, more preferably 〇 2 to 3 μm, particularly preferably 0.3 to 2 # m. Further, considering the processability of processing into various products, the median diameter is not limited, and the maximum particle size is also important. Therefore, the maximum particle diameter of the chromium phosphate compound represented by the formula [2] is preferably 10 μm or less, more preferably 6 &quot; m or less, and particularly preferably 4 or less. The lower limit 値〇. i is preferably from m or more. The phosphoric acid pin compound which is not used in the formula [2] which is a raw material of the silver-substituted zirconium phosphate compound used in the present invention can be specifically exemplified below.

Na〇.〇7(NH4)〇.85zr2 〇Hf〇 02(p〇4)j , 〇 65H2〇Na〇.〇7(NH4)〇.85zr2 〇Hf〇 02(p〇4)j , 〇 65H2〇

Na〇.i2(NH4)〇.65zr2 olHf〇 〇3(p〇4)3 # 〇 85H2qNa〇.i2(NH4)〇.65zr2 olHf〇 〇3(p〇4)3 # 〇 85H2q

Na〇.i9(NH4)〇.65zr2 〇3Hf〇 0l(p〇4)3 , 0.75H2ONa〇.i9(NH4)〇.65zr2 〇3Hf〇 0l(p〇4)3 , 0.75H2O

Na〇.2i(NH〇〇.75Zri.”Hf〇.〇2(P〇4)3 · 〇 6H2C) -14- 201138638Na〇.2i(NH〇〇.75Zri.”Hf〇.〇2(P〇4)3 · 〇 6H2C) -14- 201138638

Na〇.27(NH4)0.75Zl*l.92Hf〇.15(P〇4)3 · 0.75H2〇Na〇.27(NH4)0.75Zl*l.92Hf〇.15(P〇4)3 · 0.75H2〇

Na〇.29(NH4)0.55Zl-1.92Hf〇.〇5(P〇4)3 · 0·5Η2〇Na〇.29(NH4)0.55Zl-1.92Hf〇.〇5(P〇4)3 · 0·5Η2〇

N a 0 . 5 7 ( N Η 4 ) 0 . 5 5 Z r 1 . 9 5 H f 0 . 0 2 ( P Ο 4 ) 3 · O.35H2ON a 0 . 5 7 ( N Η 4 ) 0 . 5 5 Z r 1 . 9 5 H f 0 . 0 2 ( P Ο 4 ) 3 · O.35H2O

Na〇.70(NH4)0.85Zr 丨.99Hf〇.〇l(P〇4)3 · O.4H2O N a 0. 07 H 0 . 8 5 Z r 2 . oH f 0 . 0 2 ( P 0 4 ) 3 · 0.65H2〇 N a 0 . 1 2 H 0 . 6 5 Z r 2 . 0 1 H f 0 . 0 3 ( P 0 4 ) 3 · O.85H2O Na〇.19H〇.6 5Zr2.03Hf〇.〇l(P〇4)3 * O.75H2ONa〇.70(NH4)0.85Zr 丨.99Hf〇.〇l(P〇4)3 · O.4H2O N a 0. 07 H 0 . 8 5 Z r 2 . oH f 0 . 0 2 ( P 0 4 3 · 0.65H2〇N a 0 . 1 2 H 0 . 6 5 Z r 2 . 0 1 H f 0 . 0 3 ( P 0 4 ) 3 · O.85H2O Na〇.19H〇.6 5Zr2.03Hf〇 .〇l(P〇4)3 * O.75H2O

Na〇.2lH〇.75Zri.99Hf〇.02(P〇4)3 · 0.6H2〇 N a 0 . 2 7 H 0 . 7 5 Z r 1 . 9 2 H f 0 . 1 5 ( P 0 4 ) 3 B 0.75H2〇 N a 0 . 29 H 0 . 5 5 Z r 1 - 9 2 H f 0 .0 5 ( P 0 4 ) 3 * 0.5H2〇Na〇.2lH〇.75Zri.99Hf〇.02(P〇4)3 · 0.6H2〇N a 0 . 2 7 H 0 . 7 5 Z r 1 . 9 2 H f 0 . 1 5 ( P 0 4 ) 3 B 0.75H2〇N a 0 . 29 H 0 . 5 5 Z r 1 - 9 2 H f 0 .0 5 ( P 0 4 ) 3 * 0.5H2〇

N a 0 . 5 7 H 0 . 5 5 Z r 1 . 9 5 H f 0 . 0 2 ( P 0 4 ) 3 # 0.35H2〇 N a 0 . 7 0 H 0 . 8 5 Z r 1 . 9 9 H f 0 . 0 1 ( P 0 4 ) 3 · O.4H2O 可藉由對於此等之磷酸锆化合物交換銀離子後並加以 熱處理而得到式〔1〕之經銀取代之磷酸锆。銀離子交換方 法,係將磷酸锆化合物浸漬於含有硝酸銀之水溶液。使上 述水溶液之硝酸銀含有量愈多,因將所得到之銀系無機抗 菌劑混合於樹脂使用時較不易變色故較佳。另一方面,因 過於太多則過剩之銀離子將殘留於水溶液就經濟上而言不 佳。較佳爲對於每1莫耳之式〔2〕所示之磷酸鉻化合物, 使用含有式〔2〕之係數bl乘以0_6〜〇 99莫耳量的硝酸銀 之水溶液,更佳爲對於每1莫耳之磷酸锆,使用含有式〔2〕 之係數bl乘以0_ 7〜0.98莫耳量的硝酸銀之水溶液。將磷 酸錯化合物浸漬於硝酸銀水溶液之量,只要對於水溶液得 -15- 201138638 以均句混合之濃度皆可’具體而g ’使式〔2〕所示之憐酸 锆化合物係與水溶液之合計量中之2 0重量%以下較佳。 含有銀離子之水溶液之調整,以使用去離子水中溶解 有硝酸銀之水溶液較佳。離子交換時之水溶液溫度,較佳 爲0〜100°C、更佳爲20〜80°C。因所進行之此離子交換係 快速,故浸漬時間雖亦可爲5分鐘以內,但爲得到均勻且 闻銀離子交換率,較佳爲30分鐘〜5小時。較佳爲銀離子 交換結束後藉由去離子水等將其予以水洗。水洗係以進行 至測定濾液之導電度爲500 μ S以下爲止較佳。水洗後過據 乾燥、並進一步藉由於適切之溫度下予以熱處理,可得到 式〔1〕所示之銀系無機抗菌劑。 式〔1〕中a係表示銀之含有量。若a値小,經銀取代 之磷酸锆中之銀含有率變低;若a値大,銀之含有率變高。 銀含有率愈高則提升持續性,故較佳。 另一方面’銀離子對於熱及暴露於光不安定,具有立 即被還原爲金屬銀而引起著色等,長期間之安定性的問 題。即使爲可安定支載銀離子之磷酸錐,高銀含有率仍有 變色性或生產性等之疑慮而有必要適切調整銀含有率。 又’ a値係由於磷酸锆中之銀含有率因其他成分之種類或 比率而有所變動’因此以控制銀含有率而非a値應用上較 容易。較佳爲經銀取代之磷酸锆中之銀含有率爲2重量% 以上15重量%以下、更佳爲4重量%以上13重量%以下、 特別佳爲6重量%以上1 2重量%以下。又,此時之較佳a -16 - 201138638 値 ( 爲 又 種 鋰 佳 在 子 中 爲 各 此 10 限 支 水 爲0.05以上〇.7以下。 式〔1〕中 ’ c 及 d 係滿足 i.75&lt;c+d&lt;2.25、a+b+4 c + d) = 9之數。c較佳爲大於ι.75且爲21以下、更佳 1.85以上2.07以下、進一步更佳爲1.9以上2.〇3以下。 (1爲0_005〜〇.2、較佳爲〇.01〜〇2、更佳爲〇.〇15〜〇.15。 式〔1〕中’ b爲0.01〜2、較佳爲〇.〇1〜丨.95。 式〔丨〕中’Μ亦可含有1種或複數種、較佳爲1〜5 、更佳爲1〜3種。較佳之μ可例示:鈉離子、鉀離子、 離子、鎂離子、鋅離子、銨離子、氫離子、及鍟離子。 式〔1〕中,η較佳爲1以下、更佳爲〇 〇丨〜〇 5、特別 爲0.03〜0.3之範圍。n大於2時,含有水分之絕對量多, 混合於各種材料時之加熱時等恐發生發泡或水解等。 此等經銀取代之磷酸锆’較佳者爲可得到白色之微粒 結晶’且藉由雷射粒徑分布儀並根據體積基準所測定之 値粒徑爲0.1〜30// m。更佳爲(^〜彳私m、進—步更佳 0.2〜3 m。、特別佳爲〇_3〜2 y m。又,若考慮加工成 種製品之加工性則非僅中値粒徑,最大粒徑亦重要。因 ’較佳爲使式〔2〕所示之磷酸銷化合物之最大粒徑成爲 V m以下、更佳爲6 /2 m以下、特別佳爲4 μ m以下。下 値0. 1 /z m以上較佳。 本發明中使用之經銀取代之憐酸錶,相較於多數其他 載體,因銀離子之支載性高,故對於離子濃度低之清淨 ’具有銀離子之釋出變少的傾向。另一方面,對於離子 -17- 201138638 濃度高之被污染水,銀離子則容易釋出,故其 應水污染度之銀離子的釋出量係自動調節、抗 續性良好、亦不易引起因過剩之銀離子釋出所驾 本發明中之經銀取代之磷酸銷,較佳者爲 經銀取代之磷酸锆的結晶性,經由粉末X射線 由歸因於經銀取代之磷酸锆結晶之尖峰強度予 由粉末X射線繞射分析並於50kV/120mA之測 以C u Κ α線測定時,檢測出歸因於六平面立方 之尖峰’即約略2 0 = 20.2°之尖峰強度較佳爲 上、更佳爲2,000cps以上、特別佳爲2,500cps 述尖峰強度愈高,結晶性高且銀離子之支載力 以防止因銀離子之游離所導致之變色。 本發明中使用之經銀取代之磷酸锆係高純 銀取代之磷酸锆的純度’可藉由粉末X射線繞 歸因於經銀取代之磷酸錐結晶之尖峰以外的 峰’並進一步經藉由螢光X射線分析確認含有 由螢光X射線分析所檢測出之歸因於經銀取代 成分之合計量,較佳爲96%以上1〇〇%以下、 以上100%以下。 本發明中使用之經銀取代之磷酸鉻的具體 如下:N a 0 . 5 7 H 0 . 5 5 Z r 1 . 9 5 H f 0 . 0 2 ( P 0 4 ) 3 # 0.35H2〇N a 0 . 7 0 H 0 . 8 5 Z r 1 . 9 9 H f 0 . 0 1 ( P 0 4 ) 3 · O.4H2O The silver-substituted zirconium phosphate of the formula [1] can be obtained by exchanging silver ions for these zirconium phosphate compounds and then heat-treating them. The silver ion exchange method is a method of immersing a zirconium phosphate compound in an aqueous solution containing silver nitrate. It is preferred that the silver nitrate content of the aqueous solution is increased as the obtained silver-based inorganic antibacterial agent is less likely to be discolored when it is used in the resin. On the other hand, if too much is too much, it will be economically unsatisfactory for excess silver ions to remain in the aqueous solution. Preferably, for every 1 part of the chromium phosphate compound represented by the formula [2], an aqueous solution containing a coefficient bl of the formula [2] and multiplied by 0-6 to 〇99 moles of silver nitrate is used, more preferably for every 1 mole. The zirconium phosphate of the ear is an aqueous solution of silver nitrate containing a coefficient bl of the formula [2] and multiplied by 0-7 to 0.98 moles. The amount of the phosphoric acid-discriminating compound is immersed in the aqueous solution of silver nitrate, and the concentration of the zirconium-containing compound represented by the formula [2] and the aqueous solution can be 'specifically and g' as long as the concentration of the aqueous solution is -15-201138638. It is preferably 20% by weight or less. The adjustment of the aqueous solution containing silver ions is preferably carried out using an aqueous solution in which silver nitrate is dissolved in deionized water. The temperature of the aqueous solution at the time of ion exchange is preferably 0 to 100 ° C, more preferably 20 to 80 ° C. Since the ion exchange system is fast, the immersion time can be within 5 minutes, but it is preferably 30 minutes to 5 hours in order to obtain a uniform silver ion exchange rate. Preferably, after the end of the silver ion exchange, it is washed with water by deionized water or the like. The washing is preferably carried out until the conductivity of the filtrate is 500 μS or less. After the water washing, it is dried, and further heat-treated at a suitable temperature to obtain a silver-based inorganic antibacterial agent represented by the formula [1]. In the formula [1], a represents the content of silver. If a is small, the silver content in the zirconium phosphate substituted by silver becomes low; if a is large, the silver content becomes high. The higher the silver content rate, the more sustainable it is, so it is better. On the other hand, silver ions are unstable to heat and exposure to light, and are immediately reduced to metallic silver to cause coloring, etc., and have a long period of stability. Even in the case of a phosphoric acid cone which can stably hold silver ions, the high silver content rate is still doubtful of discoloration or productivity, and it is necessary to appropriately adjust the silver content. Further, since the silver content in zirconium phosphate varies depending on the type or ratio of other components, it is easier to control the silver content rate instead of a. The silver content in the zirconium phosphate substituted by silver is preferably 2% by weight or more and 15% by weight or less, more preferably 4% by weight or more and 13% by weight or less, particularly preferably 6% by weight or more and 12% by weight or less. Further, at this time, it is preferable that a -16 - 201138638 値 (for the other kind of lithium, the water limit for each of the 10 limits is 0.05 or more 〇.7 or less. In the formula [1], the 'c and d systems satisfy i. 75&lt;c+d&lt;2.25, a+b+4 c + d) = 9 number. c is preferably greater than ι.75 and is 21 or less, more preferably 1.85 or more and 2.07 or less, still more preferably 1.9 or more and 2. 〇3 or less. (1 is 0_005~〇.2, preferably 〇.01~〇2, more preferably 〇.〇15~〇.15. In the formula [1], 'b is 0.01~2, preferably 〇.〇1丨.95. In the formula [丨], Μ can also contain one or more kinds, preferably 1 to 5, more preferably 1 to 3. Preferred μ can be exemplified by sodium ion, potassium ion, ion, Magnesium ions, zinc ions, ammonium ions, hydrogen ions, and cesium ions. In the formula [1], η is preferably 1 or less, more preferably 〇〇丨 〇 〇 5, particularly 0.03 to 0.3. n is greater than 2 When the amount of water contained is large, the amount of water contained in the various materials may be foamed or hydrolyzed during heating, etc. The silver-substituted zirconium phosphate is preferably a white crystal crystallization, and The particle size distribution meter and the particle size measured according to the volume reference are 0.1 to 30//m. More preferably (^~彳m, the step is more preferably 0.2 to 3 m., especially preferably 〇_3) ~2 ym. In addition, considering the processability of processing into a product, it is not only the median particle size, but also the maximum particle size. It is preferable to make the maximum particle size of the phosphoric acid pin compound represented by the formula [2] Below V m More preferably, it is 6 /2 m or less, particularly preferably 4 μm or less. The lower 値0. 1 /zm or more is preferable. The silver-substituted pity acid table used in the present invention is compared with most other carriers due to silver ions. Since the support is high, the cleansing with low ion concentration tends to have less release of silver ions. On the other hand, for contaminated water with a high concentration of ion-17-201138638, silver ions are easily released, so The release amount of silver ions in the degree of water pollution is automatically adjusted, the resistance is good, and it is not easy to cause the silver-substituted phosphoric acid pin in the present invention due to the excess silver ion release, and the silver ion is preferably replaced by silver. The crystallinity of zirconium phosphate is determined by powder X-rays from the peak intensity of the zirconium phosphate crystals substituted by silver, and is measured by powder X-ray diffraction and measured by C u Κ α line at 50 kV/120 mA. The peak intensity attributed to the peak of the six-plane cube is about 20 = 20.2°, preferably upper, more preferably 2,000 cps or more, particularly preferably 2,500 cps. The higher the peak intensity, the higher the crystallinity and the silver ion Supporting force to prevent the release of silver ions The purity of the silver-substituted zirconium phosphate-substituted high-purity silver-substituted zirconium phosphate used in the present invention can be obtained by powder X-rays around a peak other than the peak of the silver-substituted phosphoric acid cone crystal and further It is confirmed by fluorescence X-ray analysis that the total amount of the silver-substituted component detected by the fluorescent X-ray analysis is preferably 96% or more and 1% by mass or less and 100% or less. The specific use of silver substituted chromium phosphate is as follows:

Ag〇.〇5Na〇.22H〇.,(H3〇)〇.5 5 2 r2.〇Hf〇.〇2(P〇4)3 · 〇·Ag〇.〇5Na〇.22H〇.,(H3〇)〇.5 5 2 r2.〇Hf〇.〇2(P〇4)3 · 〇·

Ag〇.17Na〇.32H〇.35Zr2.03Hf0.0|(p〇4)3 . 0.05H2O 特徵有:因 菌效果之持 I致之變色。 結晶性1¾。 繞射,可藉 以判定。藉 定條件下, 晶之磷酸锆 1,5 0 0 c p s 以 以上。因前 變高,故得 度較佳。經 射確認有無 不純物之尖 成分量。藉 之磷酸锆的 更佳爲99% 例,可例示 15H2〇 -18- 201138638Ag〇.17Na〇.32H〇.35Zr2.03Hf0.0|(p〇4)3 . The characteristics of 0.05H2O are: the discoloration caused by the effect of the bacteria. Crystallinity 13⁄4. Diffraction can be judged. Under the conditions, the crystal zirconium phosphate 1,5 0 0 c p s or more. Because it gets higher before, it gets better. The amount of the component of the impurity is determined by the injection. More preferably, 99% of zirconium phosphate can be exemplified by 15H2〇 -18- 201138638

Ag〇.17Na〇.64H〇.33Zr)-92Hf〇.05(P〇4)3 · 0 15H2〇 Ag〇.45Na〇.47H〇.2Zri.95Hf〇.02(P〇4)3 · Q Ag〇.55Na〇.iH〇.2(H3〇)〇.i5Zri.99Hf〇.01(p〇4)3 . 〇.15H2〇 Ag〇.05Na〇.32(NH4)〇.2H〇.35Zr2.〇Hf〇.〇2(P〇4)3 . 〇 15H2〇 Ag〇.l〇Na〇.2lH〇.28(H3〇)〇.25Zr2.〇lHf〇.〇3(P〇4)3 . O.IOH2O AgO.i7Na0.20Li0.i5Ho.3Zl. 1.92Hf〇.l〇(P〇4)3 · Q 15PJ2Q Ag〇.17Na〇.l〇Mg〇.l〇H〇.25Zn.92Hf〇.i5(p〇4)3 . Q !5f{2〇 A g 0 1 7 Zn 0 . 20N a 0 . 2 5 H 0 . 3 Z r 1 . 9 2H f 0 . 0 5 ( P〇 4 ) 3 . Q I5H2O A g 0 4 5 Z n 0 . 2 7 K 0 1 H 0 . 3 Z r 1 . 9 5 H f 0 . 0 2 ( P 〇 4 ) 3 · Q 1 5 H 2 QAg〇.17Na〇.64H〇.33Zr)-92Hf〇.05(P〇4)3 · 0 15H2〇Ag〇.45Na〇.47H〇.2Zri.95Hf〇.02(P〇4)3 · Q Ag 〇.55Na〇.iH〇.2(H3〇)〇.i5Zri.99Hf〇.01(p〇4)3 . 〇.15H2〇Ag〇.05Na〇.32(NH4)〇.2H〇.35Zr2.〇 Hf〇.〇2(P〇4)3 . 〇15H2〇Ag〇.l〇Na〇.2lH〇.28(H3〇)〇.25Zr2.〇lHf〇.〇3(P〇4)3 . IOH2O AgO.i7Na0.20Li0.i5Ho.3Zl. 1.92Hf〇.l〇(P〇4)3 · Q 15PJ2Q Ag〇.17Na〇.l〇Mg〇.l〇H〇.25Zn.92Hf〇.i5(p 〇4)3 . Q !5f{2〇A g 0 1 7 Zn 0 . 20N a 0 . 2 5 H 0 . 3 Z r 1 . 9 2H f 0 . 0 5 ( P〇4 ) 3 . Q I5H2O A g 0 4 5 Z n 0 . 2 7 K 0 1 H 0 . 3 Z r 1 . 9 5 H f 0 . 0 2 ( P 〇4 ) 3 · Q 1 5 H 2 Q

Ag〇.55K〇.lH〇.l(H3〇)0.25Zri.99Hf〇,OI(p〇4)3 ·〇.15H2〇 藉由將本發明中使用之經銀取代之磷酸鉻與樹脂予以 混合可容易得到抗菌性樹脂組成物。本發明之水處理用抗 菌處理劑之製造方法’其特徵爲含有將前述抗菌劑與前述 樹脂予以混合之步驟。將經銀取代之磷酸锆混合至樹脂並 製成抗菌性樹脂成形品之加工方法,可採用任何習知方 法、可列舉例如以下(1 )〜(4 )之4個製造方法。 (1 )使用爲使經銀取代之磷酸锆與樹脂易於附著之添加 劑、或爲提升分散性之分散劑,並以混合機將九狀 樹脂或粉狀樹脂直接予以混合之方法。 (2 )如前述般予以混合並以壓出成形機壓成九狀後,將該 成形物混合於九狀樹脂之方法。 (3 )使用蠟將經銀取代之磷酸锆成形爲高濃度之九狀 後,將該九狀成形物混合於九狀樹脂之方法。 Ι:ϊ -19- 201138638 (4 )調製糊漿狀組成物,其係將經銀取代之磷酸锆分散混 合於多元醇等之高黏度的液狀物,之後將該糊獎混 合於九狀樹脂之方法。 此等之方法中,使用分散劑或多元醇等之親水性物質 時,較佳爲使樹脂組成物中之親水性物質超過〇重量%未 滿5 %、更佳爲超過0重量%未滿1重量%。本發明中必須 使用一定之標準水分百分率的樹脂,係因若倂用其他之親 水性物質時’恐有樹脂組成物之親水性變得過高而銀之溶 出量變多、或親水性成分先溶出而改變處理劑之物性之虞。 本發明中,經銀取代之磷酸銷至樹脂組成物的混合量, 係相對於樹脂組成物之全重量的1〜3 0重量%。就控制銀 溶出至水中之濃度及持續性變高之觀點而言,混合量係以 高濃度較佳;惟就加工捏合於樹脂時之分散性或加工容易 性而言,混合量係愈少較佳。較佳混合量爲2〜2 5重量%、 更佳爲3〜20重量% 用於加工本發明之水處理用抗菌處理劑之成形方法並 無限制,得以使用既有之方法或裝置。例示有例如:射出 成形(機)、壓出成形(機)、吹塑成形(blow molding) (機)、及熱壓成形(機)等。其中又以射出成形(機) 除了形狀之安定性外,因受熱經歷少故較佳。受熱經壓愈 少樹脂之熱劣化少、故無樹脂之分解成分等溶出於水中之 虞。 所謂用於本發明之水處理用抗菌處理劑之樹脂的標準 -20- 201138638 水分百分率,係指將纖維製品之物理試驗方法通則ns L 0 1 0 5 : 2006中所規定之絕乾狀態(將試驗片放置於1〇5 °C ± 2 °C之熱風乾燥機中成爲恆量狀態)的重量,與標準狀態(溫 度20 °C ±2 °C、相對溼度65% ±4 % )之狀態下成爲恆量之試 驗片的重量差作爲標準水分量,且以上述絕乾狀態之重量 爲基準並以百分率表示者,並得以使用與】IS L 1 03 0-2 : 2005表1之纖維之公定水分百分率相同之定義。 用於本發明之樹脂的標準水分百分率愈高,銀之溶出量 變多故抗菌效果容易表現,惟若溶出量過多則易引起變色 之問題。另一方面,前述水分百分率愈低則溶出量變低, 抗菌效果雖不易表現但減少變色之虞。此效果亦因所組合 之抗菌劑而大受影響。本發明中使用之樹脂係前述水分百 分率爲1.0重量%以上10重量%以下、較佳爲2重量%以 上9重量%以下、進一步較佳爲3重量%以上8.5重量% 以下、特別佳爲4重量%以上8重量%以下。 作爲一般樹脂之標準水分百分率,聚丙烯爲〇.〇、聚乙 烯0.0、氯乙烯0.0、亞乙烯0·0、聚酯〇·3〜0.4、胺甲酸乙 酯1、丙烯酸酯1.2〜2.0、聚縮醛2.0、聚醯胺3.5〜5.0、 乙酸酯6〜7、嫘縈12〜14’由標準水分百分率之値而言’ 最佳之樹脂爲聚醯胺。聚醯胺一般亦被稱爲耐綸,其種類 有耐綸 6、66、46、MDX6、61、9T、610、612、11、12 等’ 此等可單獨或混合使用。其中就廣用性、成形性、銀溶出 量之控制性等而言’特別佳爲耐綸6。亦可與其他種類之 201138638 耐綸混合使用,此時混合率較佳爲50%以上100%以下。 進一步,相同樹脂中愈低密度者因容易溶出故較佳。 樹脂之密度,已知對於樹脂硬度等有影響。作爲標準 樹脂密度的中心値,已知聚丙烯0.90〜0.91、聚乙烯0.92 〜0.93、氯乙烯1.30〜1.35、耐綸 1.12〜1.14、胺甲酸乙 酯1.20、丙烯酸酯1.17〜1.2、聚縮醛1.42等之數値,但包 含此等範圍在內,均發現有相同樹脂中高密度者銀不易溶 出;低密度者銀容易溶出之傾向。 又,在不損及本發明之效果的程度下,可倂用標準水 分百分率不在1.0〜10之範圍內的樹脂。所謂不損及效果 之程度,較佳爲所使用之樹脂全體量的40重量%以下、更 佳爲2 0 %以下、特別佳爲1 0重量%以下。 得以將金屬皂等之分散劑用於本發明之水處理用抗菌 處理劑。較佳之分散劑爲金屬皂,係硬脂酸鋅、硬脂酸鈣、 硬脂酸鎂等,更佳爲硬脂酸鎂。 用於本發明之水處理用抗菌處理劑之樹脂組成物中, 爲改善捏合至樹脂之加工性或其他物性,可因應必要混合 各種之添加劑。作爲具體例有:氧化鋅或氧化鈦等之顏料、 磷酸锆或沸石等之無機離子交換體、染料、抗氧化劑、耐 光安定劑、難燃劑、帶電防止劑、發泡劑、耐衝擊強化劑、 玻璃纖維、金屬皂等之滑劑、防溼劑、增量劑、賴合劑、 成核劑、流動性改良劑、消臭劑、木粉、防黴劑、防污劑、 防鏽劑、金屬粉、紫外線吸收劑、及紫外線遮蔽劑等。惟 -22- 201138638 爲用於清淨水之抗菌處理,儘量不含此等之添加劑爲佳。 對於本發明之水處理用抗菌處理劑,依照各種樹脂之 特性,可使用所有習知之加工技術或器械。於適當之溫度 或壓力下,加熱及加壓或減壓之同時,藉由混合' 混入或 混練之方法可容易加以調製,此等之具體操作只要根據常 法進行即可。又,其形狀並無限制,球狀 '塊狀、海綿狀、 薄膜狀、板狀、線狀或管狀、或此等之複合體等,可成形 加工爲各種形態,並可因應用途予以適當設計。 本發明中之水處理用抗菌處理劑之成形品的比表面 積’愈大則銀之溶出速度變快,可得到較多之溶出銀濃度, 且無遠離與水接觸表面之深部的抗菌劑無法充分利用之虞 故較佳。另一方面,比表面積小者因較厚且強度高,不必 擔心變形後重疊故較佳。因此,本發明中之水處理用抗菌 處理劑的比表面積,較佳爲3〜110cm2/g、更佳爲5〜 1 00cm2/g。比表面積可使用作爲成形體之處理劑的尺寸算 出。例如爲得到3 c m2 /〜5 0 c m2 / g的表面積,若爲球則半徑 爲0.05cm〜lcm左右、若爲l〇cm見方之板狀則平均厚度自 〇.3mm至6mm左右。又,加大比表面積時,若平面形狀則 因設置面積變大’故可能因通水筒等之形狀而有所干擾。 但可成形爲渦型、或使用即使塡充亦得以不損及通水性之 較佳新式樣的成形體。 本發明之水處理方法,其特徵爲包含使前述之水處理 用抗菌處理劑與水接觸之步驟。 &lt;:ί -23- 201138638 本發明之水處理用抗菌處理劑之使用形態並無特別限 制,亦可直接使用、亦可包裹於網狀織物或不織布等、亦 可塡充於筒狀之容器。藉由將抗菌處理劑浸漬於欲處理之 水、或將欲處理之水通過裝有抗菌處理劑之容器,得藉此 使用抗菌處理劑。不必使抗菌處理劑一直存在於水中,於 空氣中即使暫時變乾,再次放回水中其性能並無大變化。 抗菌處理劑之使用量的標準係根據銀含有量或目的之抗菌 效果適當予以調整即可。將本發明中之水處理用抗菌處理 劑浸漬或通過對象之清淨水時之銀溶出量,較佳爲5ppb以 上200ppb以下、更佳爲lOppb以上lOOppb以下。此範圍之 濃度持續3週以上、倘若可能1年左右較佳。又,ppb爲重 量 ppb 0 例如浸漬使用處理劑時,藉由相對於1 L之水,使用表 面積50cm2〜5 00cm2左右之水處理用抗菌處理劑,可得到此 較佳之銀溶出量。相較於浸漬,通水之接觸時間較少,故 通水使用時,較佳表面積爲浸漬之數倍至1〇倍左右。 本發明之水處理用抗菌劑的用途並無特別限定,可有 效用於微生物污染成爲問題之水的水處理用途。可列舉例 如:淨水器用過爐材、蒸飽水機用水槽、循環水、剪花用 水、通水管內或槽、游泳池或池塘、冰箱中之製冰用水、 加溼器、冷氣排水等。 以下’根據實施例說明本發明,惟本發明非受限於此。 粒子之中値粒徑係使用雷射繞射式粒徑分布並根據體 * 24 - 201138638 積基準加以測定。 抗菌劑或其原料中所含鉻的量係使用強酸將檢體溶解 後,將此液體以感應親合電獎(inductively coupled plasma ; ICP )光學放射光譜儀(optical emission spectrophotometer)加以測定並算出。磷的量係使用強酸將 檢體溶解後,將此液體以ICP光學放射光譜儀加以測定並 算出。鈉的量係使用強酸將檢體溶解後,將此液體以原子 吸收光譜儀(atomic absorption spectrometer)加以測定並 算出。氨的量係使用強酸將檢體溶解後,將此液體以靛酚 法加以測定並算出。鋰離子的量係藉由熱分析測定並算出 160〜190 °C之重量減少量。X射線粉末繞射法(XRD )之繞 射強度,係藉由粉末XRD繞射裝置,以X射線50kV/120mA 之條件’藉由Cu ο:線所測定之χ射線繞射強度。細菌數係 藉由使用普通瓊脂培養基之注入培養法(pour culture)以 3 7 °C、培養2天之方法加以測定。銀溶出濃度係以ICP光 學放射光譜儀加以測定。 〈抗菌劑A :經銀取代之磷酸鉻(a )之配製〉 將草酸二水合物0.1莫耳、含給O.i 7%之氧氯化锆八水 合物0.2莫耳、及氯化銨〇」莫耳溶解於去離子水3〇〇ml 後’攪拌下添加磷酸0.3莫耳。使用20%氫氧化鈉水溶液 將此溶液p Η調整至2 · 6後,於9 8 t下攪拌1 4小時。其後, 將得到之沈澱物以去離子水充分洗淨,並於1 2 〇 〇c下乾燥4 小時藉以合成磷酸鍩化合物。 -25- 201138638 經測定此磷酸錐化合物之各成分量,組成式爲下式。Ag〇.55K〇.lH〇.l(H3〇)0.25Zri.99Hf〇, OI(p〇4)3 ·〇.15H2〇 by mixing the silver-substituted chromium phosphate used in the present invention with a resin An antibacterial resin composition can be easily obtained. The method for producing an antibacterial treatment agent for water treatment according to the present invention is characterized by comprising a step of mixing the antibacterial agent with the above resin. The method of processing the silver-substituted zirconium phosphate to the resin to form the antibacterial resin molded article may be any conventional method, and examples thereof include the following four production methods (1) to (4). (1) A method in which a silver-substituted zirconium phosphate is easily attached to a resin or a dispersing agent for improving dispersibility, and a nine-shaped resin or a powdery resin is directly mixed by a mixer. (2) A method in which the mixture is mixed as described above and pressed into a nine shape by an extrusion molding machine, and the molded product is mixed with a nine-shaped resin. (3) A method in which a silver-substituted zirconium phosphate is formed into a high-concentration nine shape by using a wax, and the nine-shaped molded product is mixed with a non-formed resin. Ι:ϊ -19- 201138638 (4) A paste-like composition in which a silver-substituted zirconium phosphate is dispersed and mixed with a high-viscosity liquid of a polyol or the like, and then the paste is mixed with a nine-shaped resin. The method. In the method, when a hydrophilic substance such as a dispersing agent or a polyhydric alcohol is used, it is preferred that the hydrophilic substance in the resin composition exceeds 〇% by weight to less than 5%, more preferably more than 0% by weight. weight%. In the present invention, it is necessary to use a resin having a predetermined standard moisture percentage, because when other hydrophilic substances are used, it is feared that the hydrophilicity of the resin composition becomes too high, the amount of silver eluted is increased, or the hydrophilic component is first dissolved. And change the physical properties of the treatment agent. In the present invention, the amount of the silver phosphate-substituted phosphoric acid pin to the resin composition is from 1 to 30% by weight based on the total weight of the resin composition. The mixing amount is preferably a high concentration from the viewpoint of controlling the concentration of silver eluted into water and the continuous highness; however, in terms of dispersibility or ease of processing when kneading into a resin, the mixing amount is less. good. The mixing amount is preferably 2 to 25% by weight, more preferably 3 to 20% by weight. The method for forming the antibacterial treatment agent for water treatment of the present invention is not limited, and an existing method or apparatus can be used. For example, injection molding (machine), extrusion molding (machine), blow molding (machine), and hot press forming (machine) are exemplified. In addition, in addition to the shape stability, injection molding (machine) is preferred because of less heat experience. The heat is less than the heat, and the resin is less thermally degraded, so that no decomposition component of the resin is dissolved in the water. The standard of the resin used in the antibacterial treatment agent for water treatment of the present invention is -20-201138638. The percentage of moisture refers to the dry state of the physical test method for fiber products as specified in ns L 0 1 0 5:2006 (will The weight of the test piece placed in a hot air dryer at 1〇5 °C ± 2 °C in a constant state) is compared with the standard state (temperature 20 °C ± 2 °C, relative humidity 65% ± 4%). The weight difference of the constant amount of the test piece is taken as the standard moisture content, and based on the weight of the above-mentioned dry state, and expressed as a percentage, and the specific moisture percentage of the fiber of Table 1 of IS L 1 03 0-2 : 2005 is used. The same definition. The higher the standard moisture percentage of the resin used in the present invention, the more the silver elution amount is, the easier the antibacterial effect is, but if the amount of dissolution is too large, the problem of discoloration is liable to occur. On the other hand, the lower the moisture content, the lower the elution amount, and the antibacterial effect is not easily expressed, but the discoloration is reduced. This effect is also greatly affected by the combined antimicrobial agent. The resin used in the present invention has a water content of 1.0% by weight or more and 10% by weight or less, preferably 2% by weight or more and 9% by weight or less, more preferably 3% by weight or more and 8.5% by weight or less, particularly preferably 4% by weight. % or more and 8% by weight or less. As a standard moisture percentage of a general resin, polypropylene is 〇.〇, polyethylene 0.0, vinyl chloride 0.0, vinylidene 0·0, polyester 〇·3~0.4, urethane 1, acrylate 1.2 to 2.0, poly Acetal 2.0, polyamine 3.5 to 5.0, acetate 6 to 7, and oxime 12 to 14' are in terms of standard moisture percentage. The most preferred resin is polyamine. Polyamines are also commonly referred to as nylons and are available in nylon 6, 66, 46, MDX 6, 61, 9T, 610, 612, 11, 12, etc. These may be used singly or in combination. Among them, in terms of versatility, formability, and controllability of silver dissolution, it is particularly preferable to be nylon 6. It can also be mixed with other types of 201138638 nylon. In this case, the mixing ratio is preferably 50% or more and 100% or less. Further, the lower density of the same resin is preferred because it is easily eluted. The density of the resin is known to have an influence on the hardness of the resin and the like. As a central crucible of the standard resin density, it is known that polypropylene 0.90 to 0.91, polyethylene 0.92 to 0.93, vinyl chloride 1.30 to 1.35, nylon 1.12 to 1.14, urethane 1.20, acrylate 1.17 to 1.2, polyacetal 1.42. In the case of the above-mentioned range, it has been found that silver having a high density in the same resin is not easily eluted; and silver having a low density tends to be easily eluted. Further, a resin having a standard water percentage percentage not in the range of 1.0 to 10 can be used to the extent that the effects of the present invention are not impaired. The degree of the effect of the damage is preferably 40% by weight or less, more preferably 20% or less, and particularly preferably 10% by weight or less based on the total amount of the resin to be used. A dispersing agent such as a metal soap can be used in the antibacterial treating agent for water treatment of the present invention. Preferred dispersing agents are metal soaps, such as zinc stearate, calcium stearate, magnesium stearate, etc., more preferably magnesium stearate. In the resin composition used for the antibacterial treatment agent for water treatment of the present invention, in order to improve the workability or other physical properties of the kneading to the resin, various additives may be mixed as necessary. Specific examples include pigments such as zinc oxide and titanium oxide, inorganic ion exchangers such as zirconium phosphate or zeolite, dyes, antioxidants, light stabilizers, flame retardants, charge inhibitors, foaming agents, and impact enhancers. , glass fiber, metal soap and other slip agents, anti-wetting agents, extenders, chelating agents, nucleating agents, fluidity improvers, deodorants, wood powder, mildew inhibitors, antifouling agents, rust inhibitors, Metal powder, ultraviolet absorber, and ultraviolet shielding agent. However, -22- 201138638 is used for the antibacterial treatment of clean water, and it is better to exclude such additives as much as possible. For the antibacterial treatment agent for water treatment of the present invention, all conventional processing techniques or instruments can be used in accordance with the characteristics of various resins. It can be easily prepared by mixing, 'mixing or kneading, at the appropriate temperature or pressure, while heating and pressurizing or depressurizing. The specific operations can be carried out according to the usual methods. Further, the shape is not limited, and a spherical shape of a block, a sponge, a film, a plate, a wire, a tube, or a composite thereof can be formed into various forms and can be appropriately designed according to the use. . In the molded article of the antibacterial treatment agent for water treatment of the present invention, the larger the specific surface area ', the faster the elution rate of silver is, and the more the dissolved silver concentration is obtained, and the antibacterial agent which is not far from the deep surface of the contact surface with water is insufficient. It is better to use it. On the other hand, those having a small specific surface area are thick and have high strength, and it is not necessary to worry about overlapping after deformation. Therefore, the specific surface area of the antibacterial treatment agent for water treatment in the present invention is preferably from 3 to 110 cm 2 /g, more preferably from 5 to 100 cm 2 /g. The specific surface area can be calculated using the size of the treating agent as a shaped body. For example, in order to obtain a surface area of 3 c m2 /~5 0 c m2 / g, if the sphere is a sphere, the radius is about 0.05 cm to about 1 cm, and if it is a plate of l〇cm square, the average thickness is from about 3 mm to about 6 mm. Further, when the specific surface area is increased, if the planar shape is increased, the installation area may become large, which may cause interference due to the shape of the water-passing cylinder or the like. However, it can be formed into a vortex type or a molded body which is preferably a new type which does not impair the water permeability even if it is filled. The water treatment method of the present invention is characterized by comprising the step of bringing the above-mentioned antibacterial treatment agent for water treatment into contact with water. &lt;: ί -23- 201138638 The use form of the antibacterial treatment agent for water treatment of the present invention is not particularly limited, and may be used as it is, or may be wrapped in a mesh fabric or a non-woven fabric, or may be filled in a cylindrical container. . The antibacterial treatment agent can be used by immersing the antibacterial treatment agent in the water to be treated or by passing the water to be treated through a container containing the antibacterial treatment agent. It is not necessary to keep the antibacterial treatment agent in the water all the time, and even if it is temporarily dried in the air, there is no large change in the performance of returning it to the water again. The standard of the amount of the antibacterial treatment agent to be used may be appropriately adjusted depending on the silver content or the antibacterial effect of the purpose. The amount of silver eluted when the antibacterial treatment agent for water treatment of the present invention is immersed or passed through the purified water of the object is preferably 5 ppb or more and 200 ppb or less, more preferably 10 ppb or more and 100 ppb or less. The concentration in this range lasts for more than 3 weeks, and it is better if it is likely to be about 1 year. Further, ppb is a weight ppb 0. For example, when a treatment agent is used for immersion, a preferred amount of silver elution can be obtained by using an antibacterial treatment agent for water treatment having a surface area of about 50 cm 2 to about 500 cm 2 with respect to 1 L of water. Compared with the impregnation, the contact time of the water is small, so when the water is used, the surface area is preferably several times to about 1 times of the impregnation. The use of the antibacterial agent for water treatment of the present invention is not particularly limited, and it can be effectively used for water treatment of water in which microbial contamination is a problem. For example, water purifiers for water purifiers, water tanks for water purifiers, circulating water, water for cutting flowers, water pipes or tanks, swimming pools or ponds, ice making water in refrigerators, humidifiers, and cold air drainage. The invention is described below based on the examples, but the invention is not limited thereto. The particle size of the particles in the particles was measured using a laser diffraction type particle size distribution and based on the volume ratio of the body * 24 - 201138638. The amount of chromium contained in the antibacterial agent or its raw material is determined by dissolving the sample using a strong acid, and the liquid is measured by an inductively coupled plasma (ICP) optical emission spectrophotometer. The amount of phosphorus was measured by dissolving the sample using a strong acid, and the liquid was measured by an ICP optical emission spectrometer. The amount of sodium was dissolved in a sample using a strong acid, and this liquid was measured by an atomic absorption spectrometer and calculated. The amount of ammonia was measured by dissolving the sample using a strong acid, and the liquid was measured by the indophenol method and calculated. The amount of lithium ions was measured by thermal analysis and the weight loss of 160 to 190 °C was calculated. The diffraction intensity of the X-ray powder diffraction method (XRD) is the diffraction intensity of the x-rays measured by the Cu ο: line by X-ray 50 kV/120 mA by a powder XRD diffraction apparatus. The number of bacteria was measured by a pour culture using a common agar medium at 37 ° C for 2 days. The silver dissolution concentration was measured by ICP optical emission spectrometry. <Antimicrobial Agent A: Preparation of Chromium Phosphate (a) Substituted by Silver> 0.1 mol of oxalic acid dihydrate, 0.2 mol of zirconia octahydrate containing 7% of Oi, and ammonium chloride 〇 After the ear was dissolved in 3 〇〇 ml of deionized water, 0.3 mol of phosphoric acid was added under stirring. After the solution p Η was adjusted to 2·6 using a 20% aqueous sodium hydroxide solution, the mixture was stirred at 9 8 t for 14 hours. Thereafter, the obtained precipitate was sufficiently washed with deionized water and dried at 1 2 〇 〇c for 4 hours to synthesize a yttrium phosphate compound. -25- 201138638 The amount of each component of the phosphoric acid cone compound was determined and the composition formula was as follows.

Na〇.6(NH4)〇.4Zri.98Hf〇.〇2(P〇4)3 · O.O9H2O 於所得到之磷酸鉻0.09莫耳中,添加溶解有硝酸銀〇 〇5 莫耳之離子交換水溶液450ml,並藉由於60。(:下攪拌2小 時將銀予以支載。將銀予以支載處理後之漿料加以過爐、 水洗並以去離子水洗淨至濾液的導電度成爲70 yS爲止。 進一步’藉由將使用電爐於6 5 (TC下熱處理12小時後之此 乾燥品予以碎裂而得到經銀取代之磷酸锆(A )。 此經銀取代之磷酸鉻(A )的中値粒徑爲1 · 〇 v m、銀含 有率爲1 0.2重量% ’且藉由測定各成分量所得到之組成式 如下:Na〇.6(NH4)〇.4Zri.98Hf〇.〇2(P〇4)3 · O.O9H2O In the obtained chromium phosphate 0.09 mol, an ion exchange aqueous solution in which 5 mol of silver nitrate was dissolved was added. 450ml, and by 60. (The silver is supported by stirring for 2 hours. The slurry after the silver is supported is subjected to furnace, washed with water and washed with deionized water until the conductivity of the filtrate becomes 70 yS. Further 'by being used The dried product of the electric furnace after being subjected to heat treatment for 12 hours at TC is broken to obtain silver-substituted zirconium phosphate (A). The silver-substituted chromium phosphate (A) has a median diameter of 1 · 〇vm The silver content is 12.2% by weight' and the composition obtained by measuring the amount of each component is as follows:

Ago.sNao.i H〇.4Zri.98Hf〇.〇2(P〇4)3 〈抗菌劑B :經銀取代之磷酸锆(b )之配製〉 將草酸二水合物〇」莫耳、含給〇1 8%之氧氯化锆八水 合物0.19莫耳、及氯化銨〇.10莫耳溶解於去離子水3〇〇ml 後’攪拌下添加磷酸0.3莫耳。使用20%氫氧化鈉水溶液 將此溶液pH調整至2 · 7後,於9 8 t下攪拌1 4小時。其後, 將得到之沈澱物藉由去離子水充分洗淨並於1 20 °C下乾 燥,藉以合成磷酸锆化合物。 經測定此磷酸錶化合物之各成分量,組成式如下: Na〇.5(NH4)〇.8Zi·丨'9 丨 Hf0.0tl5(P〇4)3 · 〇.11Η2〇 於所得到之磷酸锆化合物0.09莫耳中,添加溶解有硝 酸銀0.019莫耳之in硝酸水溶液450 ml,並藉由於60 °C下 -26- 201138638 攪拌2小時將銀予以支載。其後藉由去離子水充分洗淨, 並將經1 20°C乾燥處理者於670°C下高溫加熱處理4小時。 將高溫加熱處理後之粉末輕輕予以碎裂後,於溼度5 〇 %、 溫度1 1 0 °C之氛圍中靜置6小時並予以吸溼處理,藉此得到 經銀取代之磷酸鉻(B )。 此經銀取代之磷酸锆(B )的中値粒徑爲〇. 8 m、銀含 有率爲4.2重量%,且藉由測定各成分量所得到之組成式 如下:Ago.sNao.i H〇.4Zri.98Hf〇.〇2(P〇4)3 <Antibacterial agent B: Preparation of silver-substituted zirconium phosphate (b)> Oxalic acid dihydrate 〇", containing 〇1 8% of zirconium oxychloride octahydrate 0.19 moles, and ammonium chloride 〇.10 moles dissolved in deionized water 3 〇〇 ml, and then add 0.3 mol of phosphoric acid under stirring. After adjusting the pH of the solution to 2·7 using a 20% aqueous sodium hydroxide solution, the mixture was stirred at 9 8 t for 14 hours. Thereafter, the obtained precipitate was sufficiently washed with deionized water and dried at 1,200 ° C to synthesize a zirconium phosphate compound. The amount of each component of the phosphoric acid table compound was determined as follows: Na〇.5(NH4)〇.8Zi·丨'9 丨Hf0.0tl5(P〇4)3 · 〇.11Η2〇 obtained zirconium phosphate In the compound 0.09 mol, 450 ml of an aqueous solution of nitric acid in which 0.019 mol of silver nitrate was dissolved was added, and the silver was supported by stirring at -26-201138638 at 60 °C for 2 hours. Thereafter, it was sufficiently washed with deionized water, and subjected to a drying treatment at 1200 ° C for 4 hours at a high temperature of 670 ° C. After the high-temperature heat-treated powder was gently broken, it was allowed to stand in an atmosphere of a humidity of 5 〇% and a temperature of 110 ° C for 6 hours and subjected to moisture absorption treatment, thereby obtaining a silver-substituted chromium phosphate (B). ). The silver-substituted zirconium phosphate (B) has a median diameter of 〇. 8 m and a silver content of 4.2% by weight, and the composition formula obtained by measuring the amounts of the respective components is as follows:

Ag〇.I9Na〇.37 H〇.21(H3〇)0.43Zl.l.9lHf〇.015(P〇4)3 · 0.1 9 Η 2 Ο 〈抗菌劑C :經銀取代之磷酸锆(c )之配製〉 將含給0.18 %之氧氯化銷八水合物0.195莫耳及氯化銨 0.12莫耳溶解於去離子水300ml後,攪拌下添加磷酸〇 3 莫耳。使用20%氫氧化鈉水溶液將此溶液pH調整至2.7 後’於1 40°C飽和蒸氣壓下攪拌4小時。其後,將得到之沈 澱物藉由去離子水充分洗淨並於12〇°c下乾燥,藉以合成磷 酸鉻化合物。 經測定此磷酸銷化合物之各成分量,組成式如下: Na〇.35(NH4)〇.85Zn.93Hf〇.〇2(P〇4)3 · 0.09Η2〇 於所得到之磷酸锆0.09莫耳中,添加溶解有硝酸銀 0-014莫耳之離子交換水45 0ml,並藉由於60t下攪拌2小 時將銀予以支載。其後藉由去離子水充分洗淨,並將經1 20 °C乾燥處理者於700°C下高溫加熱處理4小時,藉此得到經 銀取代之磷酸锆(C )。 -27- 201138638 此經銀取代之磷酸锆(C )的中値粒徑爲〇. 8 # m、銀含 有率爲3 ·丨重量%,且藉由測定各成分量所得到之組成式 如下:Ag〇.I9Na〇.37 H〇.21(H3〇)0.43Zl.l.9lHf〇.015(P〇4)3 · 0.1 9 Η 2 Ο <Antibacterial agent C: Zirconium phosphate substituted by silver (c) Preparation> After dissolving 0.18 mol of 0.15 mol of oxychlorinated pin octahydrate and 0.12 mol of ammonium chloride in deionized water, 300 g of deuterated phosphate was added thereto with stirring. The pH of the solution was adjusted to 2.7 using a 20% aqueous sodium hydroxide solution and stirred at a saturated vapor pressure of 1 40 ° C for 4 hours. Thereafter, the obtained precipitate was sufficiently washed with deionized water and dried at 12 ° C to synthesize a chromium phosphate compound. The amount of each component of the phosphoric acid pin compound was determined as follows: Na〇.35(NH4)〇.85Zn.93Hf〇.〇2(P〇4)3 · 0.09Η2〇 The obtained zirconium phosphate 0.09 mole In the middle, 45 ml of ion-exchanged water in which 0-014 mol of silver nitrate was dissolved was added, and silver was supported by stirring at 60 t for 2 hours. Thereafter, it was sufficiently washed with deionized water, and heat-treated at 1,200 ° C for 4 hours at 700 ° C to obtain silver-substituted zirconium phosphate (C ). -27- 201138638 The silver-substituted zirconium phosphate (C) has a median particle size of 〇. 8 # m, a silver content of 3 · 丨 by weight, and the composition of each component is determined as follows:

Ag〇.l4Na〇.24 H〇.46Zr2.03Hf〇.02(P〇4)3 〈抗菌劑D :經銀取代之磷酸鉻(D )之配製〉 將含給0.18 %之氧氯化鉻八水合物0.195莫耳及氯化銨 0.12莫耳溶解於去離子水3〇〇ml後,攪拌下添加磷酸ο.〗 旲耳。使用2 0 %氫氧化鈉水溶液將此溶液ρ η調整至2.7 後’於1 40X:飽和蒸氣壓下攪拌4小時。其後’將得到之沈 澱物藉由去離子水充分洗淨並於12(rc下乾燥,藉以合成磷 酸鍩.化合物。 經測定此磷酸銷化合物之各成分量,組成式如下:Ag〇.l4Na〇.24 H〇.46Zr2.03Hf〇.02(P〇4)3 <Antibacterial agent D: Preparation of chromium phosphate (D) substituted by silver> 0.18 % of chromium oxychloride is added After hydrate 0.15 mol and ammonium chloride 0.12 mol dissolved in deionized water 3 〇〇 ml, add phosphoric acid under stirring ο. 旲 ear. This solution ρ η was adjusted to 2.7 using a 20% aqueous sodium hydroxide solution and stirred at 1 40X: saturated vapor pressure for 4 hours. Thereafter, the precipitate obtained was sufficiently washed with deionized water and dried at 12 (r) to synthesize a bismuth phosphite compound. The components of the phosphoric acid compound were determined to have the following composition:

NaZr 1 9 8 5 Hf〇.〇i 5(P〇4)3 . O.09H2O 於所得到之磷酸锆〇 〇9莫耳中,添加溶解有硝酸銀〇.〇8 莫耳之離子交換水450ml,並藉由於6〇t下攪拌2小時將 銀予以支載。其後藉由去離子水充分洗淨,並將經丨2〇。〇乾 燥處理者於700 C下高溫加熱處理4小時,藉此得到經銀取 代之磷酸锆(D )。 經測定此經銀取代之磷酸鉻(D )的各成分量,組成式 如下:NaZr 1 9 8 5 Hf〇.〇i 5(P〇4)3 . O.09H2O Into the obtained zirconium phosphate 〇〇9 molar, 450 ml of ion-exchanged water in which silver nitrate 〇.〇8 mol was dissolved was added. The silver was supported by stirring for 2 hours at 6 〇t. It is then thoroughly washed with deionized water and passed through a crucible. The dry-drying treatment was heat-treated at 700 C for 4 hours, thereby obtaining silver-substituted zirconium phosphate (D). The amount of each component of the silver-substituted chromium phosphate (D) was determined as follows:

Ag〇.79Na〇.u H〇.28Zn 98sHf〇 〇)5(p〇4)3 並且此經銀取代之磷酸鉻(D )的中値粒徑爲1. 〇 &quot; m、 銀含有率爲15.3重量%。 •28- 201138638 〈抗菌劑E :沸石系銀系無機抗菌劑(e)之配製〉 5、市售之A 沸石2〇g中,添加溶解有】钾硝酸銀之 離子交換水溶液1〇〇m卜並藉由於6〇t:下攪拌2小時將銀 予以支載。水洗後,1201乾燥後所得之沸石系銀系無機抗 菌劑(E)經碎裂後,中値粒徑爲4 ^ m、銀含有率爲4 2 重量%。 〈抗囷劑F:沸石系銀系無機抗菌劑(F)之配製〉 於市售之A型沸石20g中,添加溶解有3 6g硝酸銀之 離子交換水溶液100ml,並藉由於6〇t下攪拌2小時將銀 予以支載。水洗後’ 1 2〇。(:乾燥後所得之沸石系銀系無機抗 菌劑(F)經碎裂後,中値粒徑爲m、銀含有率爲1〇 2 重量%。 〈抗囷劑G :銀玻璃系抗菌劑(g )之配製〉 調合玻璃原料使之成爲Ag2〇(2重量%) 、K2〇(7重 量% ) 、B2〇3(45 重量 %) 、Si〇2(46 重量 %)並於 1200 C下加熱熔融。熔融後’使用金屬製之冷卻成形輥予以冷 卻’並將得到之玻璃經簡單敲碎者進一步於球磨機予以乾 式壓碎後,得到中値粒徑9 V m、銀含有率爲1.9重量%之 銀玻璃系抗菌劑(G ) 。 ^ 〈實施例1〜9及比較例1〜9〉 將根據前述方法所得到之各種銀系無機抗菌劑A〜G ®合於如表1之各種樹脂,並予以成形製作爲實施例1〜9 及比較例1〜9之抗菌處理劑。其係使用標準水分百分率4.4 -29- 201138638 重量%之耐綸 6 ( UBE INDVSTRIES,LTD.製;商品名 1011FB)、標準水分百分率3.9重量%之耐綸 66(UBE INDVSTRIES,LTD.製;商品名2020B)、標準水分百分率 1.8重量%之聚縮醛樹脂(p〇iypiastics Co.,Ltd.製;商品名 Duraeon )、標準水分百分率 1.4重量%之丙烯酸酯樹脂 (MITSUBISHI RAYON CO.,LTD·製:商品名 Acrypet)、標 準水分百分率0.0重量%之聚丙嫌樹脂(Prime Porypro公 司製;商品名J105G)、標準水分百分率0.3重量%之聚酯 樹脂(UNITKA,LTD.製;商品名NEH-2030 )作爲樹脂,並 將抗菌劑粉末直接混合於各種樹脂九後,予以成形。處理 劑平板成形時,使用射出成形機做成10cm見方之板狀時, 厚1mm之平板,比表面積(依尺寸之計算値)約14cm2/g ; 厚4mm之平板,比表面積約3cm2/g;厚0.15mm時,比表 面積約110cm2/g。處理劑九係使用熱切壓出成形機成形爲 直徑4mm、高1mm之圓錐形。又,樹脂種類與抗菌劑之組 合、抗菌齊!|之混合率、處理劑形狀及處理劑之比表面積係 記述於表1。惟,比較例8及9發生顯著發泡及變色,成形 本身無法完成,故未測定比表面積,且亦未進行其後使用 處理劑之試驗。 -30- 201138638 表1 樹脂之種類 樹脂之標準 水分百分率 (重量%) 抗菌劑 之種類 抗菌劑之混 合率 (重量%) 處理劑 之形狀 處理劑之 比表面積 (cm2/g) 實施例1 耐輪6 4.4 A 10 板狀 14 實施例2 耐綸6 4.4 A 10 臓 3 實施例3 耐綸6 4.4 A 10 板狀 110 實施例4 耐綸6 4.4 A 10 九狀 9 實施例5 耐綸6 4.4 B 10 九狀 9 實施例6 耐輪6 4.4 C 10 九狀 9 實施例7 耐綸66 3.9 A 10 尬 9 實施例8 聚縮醛樹脂 1.8 A 10 九狀 9 實施例9 丙烯酸酯樹脂 1.4 A 10 九狀 9 比較例1 聚丙烯樹脂 0.0 A 10 九狀 9 比較例2 聚酯樹脂 0.3 A 10 九狀 9 比較例3 耐綸6 4.4 A 0.8 ΛΜ 9 比較例4 耐綸6 4.4 D 0.5 九狀 9 比較例5 聚丙烯樹脂 0.0 E 33 9 比較例6 聚丙烯樹脂 0.0 F 10 九狀 9 比較例7 耐輪6 4.4 G 10 九狀 9 比較例8 耐綸6 4.4 E 33 尬 比較例9 耐綸6 4.4 F 10 九狀 _ (表中,一表示未測定) -31 - 201138638 〈使用飲用用天然水之抗菌處理評價〉 測定將實施例1〜9及比較例1〜7所得到之水處理用 抗菌處理劑各30g,浸漬於添加有市售之飲用用天然水(以 下,稱作天然水)及硝酸鈉並將天然水中之鈉濃度調整爲 5 00ppm的1L水中,並於水溫約15°C下保存1天後測定水 中的銀濃度。又,對於天然水,測定直接保存21天後,以 及每天僅重新更換水並同樣保存2 1天後之水中的銀濃 度。藉由ICP光學放射光譜儀測定之溶出銀濃度之結果示 於表2。 表2 保存1天後之銀濃度 (雷量ppb) 保存21天後之銀濃度. (重量ppb) 檢體之水質 天然水 天然水+Na 500ppm 天然水 天然水 換水 Μ ίκ Μ /\ w 有(每天) 實施例1 25 899 25 27 實施例2 7 390 22 10 實施例3 128 3093 198 98 實施例4 44 912 54 32 實施例5 11 569 20 33 實施例6 6 239 14 9 實施例7 18 701 28 18 實施例8 11 333 20 11 實施例9 6 471 19 5 比較例1 3 155 32 .1 比較例2 4 87 45 1 比較例3 2 62 21 4 比較例4 12 56 21 1 比較例5 12 59 28 3 比較例6 19 64 19 2 比較例7 562 540 6192 122 -32- 201138638 實施例1〜9顯示:1天後之銀濃度皆爲5ppb以上,且 與有無換水無關,即使2 1天後亦無大幅度銀濃度之增減, 銀溶出安定發生。又,使Na濃度爲500ppm之高濃度的溶 出試驗的意義係基於以下想法:即,因Na離子與銀離子之 離子交換迅速發生,若使可自試驗片溶出之銀離子溶出並 測定其濃度,則可反映出其得以溶出之銀的量。而於此試 驗中可得到高銀濃度之試驗片,由於其得以溶出之銀的量 多,故足以判斷其於一般使用條件下爲持續性高者。 另一方面,比較例1〜3 : 1天後之溶出量少,達到可 得到抗菌效果之銀濃度需要時間。又,比較例1、2及4則 顯示:由於換水導致銀濃度降低,於交換水之條件下,一 直無法達到可得到抗菌效果之充分銀濃度。 比較例3〜6 :由於即使N a濃度爲5 0 0 p p m之條件下的 銀濃度低,故得以溶出之銀的量少而無法期待持續性。 比較例7 :因未換水之21天後的銀濃度較所需濃度 高,故觀察到因銀離子濃度過高所導致之變色,而無法溶 出無過與不及之一定濃度的銀離子。 〈長期間壽命之評價〉 又,爲調查長期間壽命’於實施例3與4之2種類中’ 將每日換水之試驗延長進行至90天。於是,第90天之水 中銀離子濃度,實施例3爲13PPb、實施例4爲24ppb’與 第1天、第21天相反’實施例4較實施例3高。此結果顯 示:相較於實施例3,實施例4初期之銀溶出量雖較少’ -33- 201138638 但濃度變動較少並得以長期間溶出而較優異。 〈使用工業用水之通水處理評價〉 將實施例3、4及比較例1、3、7之試驗片各100g分 別塡充於淨水器筒,並使一般細菌數平均約1 00個/m卜水 溫約15°C之工業用水以0.1升/分通過。根據使用一般瓊脂 培養基之注入培養法,測定通水1 0分鐘後及1天後之工業 用水lml中之一般細菌數的結果、以及藉由ICP光學放射 光譜儀測定此時之溶出銀濃度的結果示於表3。 表3 一般細菌數(cfu/ml ) 銀濃度(質量ppb ) 通水時間 1 0分鐘後 1天後 1 0分鐘後 1天後 實施例3 少於1 少於1 42 3 1 實施例4 少於1 少於1 12 18 比較例1 47 94 2 0 比較例3 29 73 9 3 比較例7 18 98 7 1 無抗菌劑 98 1 10 — —— (表中’ 一表不未測定) 實施例3及4,10分鐘後及1天後均確認抗菌效果, 並確認銀溶出濃度安定。另一方面’比較例1、3及7,相 較於10分鐘後,1天後之抗菌效果及銀溶出濃度明顯降 低。由於比較例7所使用之成形體,係顯示銀持續溶出而 與離子交換無關者,故於表2所示之換水方式的評價中, -34- 201138638 得確認即使達到高濃度’銀還是持續溶出之結果。另一方 面’通水處理評價之表3的試驗結果中得知:由於對於通 水,銀之溶出速度不高,故得知i 〇分鐘後之銀濃度並不怎 麼高,1天後溶出速度則進一步降低。 產業上利用之可能性 本發明之水處理用抗菌處理劑,係得以維持一定之銀 濃度,且具有長期之持續性。因此,對於飲用水或循環水 等之清淨水,即使因通水或消費等而有水之更換,亦得以 調整爲必要量之水中的一定之銀濃度,且長期維持抗菌效 果。 【圖式簡單說明】 Μ 。 ^\\\ 【主要元件符號說明】 無。 -35-Ag〇.79Na〇.u H〇.28Zn 98sHf〇〇)5(p〇4)3 and the silver-substituted chromium phosphate (D) has a median particle size of 1. 〇&quot; m, silver content 15.3 wt%. •28- 201138638 <Antibacterial agent E: Preparation of zeolite-based silver-based inorganic antibacterial agent (e)> 5. A commercially available A zeolite 2〇g is added with an ion exchange aqueous solution in which potassium potassium nitrate is dissolved. The silver was supported by stirring at 6 〇t: for 2 hours. After washing with water, the zeolite-based silver-based inorganic antibacterial agent (E) obtained after drying at 1201 was crushed, and had a medium ruthenium size of 4 μm and a silver content of 42% by weight. <Anti-caries agent F: Preparation of zeolite-based silver-based inorganic antibacterial agent (F)> 100 g of an ion-exchanged aqueous solution in which 36 g of silver nitrate was dissolved was added to 20 g of a commercially available type A zeolite, and stirred by 6 〇t. Silver is supported for hours. After washing, '1 2 〇. (: After the zeolite-based silver-based inorganic antibacterial agent (F) obtained after drying is crushed, the median particle size is m and the silver content is 1〇2% by weight. <Anti-caries agent G: silver glass-based antibacterial agent ( g) Preparation> Mix the glass materials to make Ag2〇 (2% by weight), K2〇 (7% by weight), B2〇3 (45% by weight), Si〇2 (46% by weight) and heat at 1200 C. Melting. After melting, 'cooling is performed using a metal cooling forming roll' and the obtained glass is further crushed by a ball mill to obtain a medium-sized particle size of 9 V m and a silver content of 1.9% by weight. Silver glass-based antibacterial agent (G). <Examples 1 to 9 and Comparative Examples 1 to 9> Various silver-based inorganic antibacterial agents A to G® obtained by the above method were combined in various resins as shown in Table 1. The antibacterial treatment agents of Examples 1 to 9 and Comparative Examples 1 to 9 were formed by using Nylon 6 (manufactured by UBE INDVSTRIES, LTD.; trade name 1011FB) having a standard moisture percentage of 4.4 -29 to 201138638% by weight. , a standard moisture percentage of 3.9 wt% of nylon 66 (manufactured by UBE INDVSTRIES, LTD.; trade name 2020B), Polyacetal resin (manufactured by P〇iypiastics Co., Ltd.; trade name Duraeon) having a water content of 1.8% by weight, and an acrylic resin having a standard moisture content of 1.4% by weight (manufactured by MITSUBISHI RAYON CO., LTD.: trade name Acrypet a polyacrylic resin (manufactured by Prime Porypro Co., Ltd.; trade name J105G) having a standard moisture percentage of 0.0% by weight, a polyester resin (manufactured by UNITKA, LTD.; trade name: NEH-2030) having a standard moisture percentage of 0.3% by weight as a resin, and The antibacterial agent powder is directly mixed into various resins and then molded. When the treatment agent is formed into a flat plate, when the injection molding machine is used to form a plate having a thickness of 1 cm, the specific surface area (calculated by size) is about 14 cm 2 . / g ; a plate having a thickness of 4 mm, a specific surface area of about 3 cm 2 / g; and a specific surface area of about 110 cm 2 / g when the thickness is 0.15 mm. The treatment agent is formed into a conical shape having a diameter of 4 mm and a height of 1 mm by using a hot-cut extrusion molding machine. The combination of the resin type and the antibacterial agent, the antibacterial ratio, the mixing ratio of the treating agent, and the specific surface area of the treating agent are described in Table 1. However, Comparative Examples 8 and 9 caused significant foaming and discoloration. The specific surface area was not measured, and the treatment agent was not used. -30- 201138638 Table 1 Resin type Resin standard moisture percentage (% by weight) Antibacterial agent type Antibacterial agent mixing ratio ( % by weight) specific surface area (cm2/g) of the shape treating agent of the treating agent Example 1 Wheel resistant 6 4.4 A 10 Plate shape 14 Example 2 Nylon 6 4.4 A 10 臓 3 Example 3 Nylon 6 4.4 A 10 plate Example 110 Example 4 Nylon 6 4.4 A 10 Nine-shaped 9 Example 5 Nylon 6 4.4 B 10 Nine-shaped 9 Example 6 Wheel-resistant 6 4.4 C 10 Nine-shaped 9 Example 7 Nylon 66 3.9 A 10 尬9 Implementation Example 8 Polyacetal resin 1.8 A 10 Nine form 9 Example 9 Acrylate resin 1.4 A 10 Nine form 9 Comparative Example 1 Polypropylene resin 0.0 A 10 Nine form 9 Comparative Example 2 Polyester resin 0.3 A 10 Nine form 9 Comparative Example 3 Nylon 6 4.4 A 0.8 ΛΜ 9 Comparative Example 4 Nylon 6 4.4 D 0.5 Nine 9 Comparative Example 5 Polypropylene resin 0.0 E 33 9 Comparative Example 6 Polypropylene resin 0.0 F 10 Nine shape 9 Comparative Example 7 Resistance wheel 6 4.4 G 10 Nine 9 Comparative Example 8 Nylon 6 4.4 E 33 尬Comparative Example 9 Nylon 6 4.4 F 10 Nine-shaped _ (in the table, one is not measured) -31 - 201138638 <Evaluation of antibacterial treatment using natural water for drinking> Each of the antibacterial treatment agents for water treatment obtained in Examples 1 to 9 and Comparative Examples 1 to 7 was measured. 30 g, immersed in 1 L of water supplemented with commercially available drinking natural water (hereinafter referred to as natural water) and sodium nitrate and adjusted to a sodium concentration of 500 ppm in natural water, and stored at a water temperature of about 15 ° C. The silver concentration in the water was measured after the day. Further, for the natural water, the silver concentration in the water after 21 days of direct storage and only the water was changed again every day and stored for 21 days. The results of the dissolved silver concentration measured by ICP optical emission spectrometry are shown in Table 2. Table 2 Silver concentration after 1 day of storage (Ray ppb) Silver concentration after 21 days of storage. (Weight ppb) Water quality of the sample Natural water Natural water + Na 500ppm Natural water Natural water exchange Μ κκ Μ /\ w Yes ( Daily) Example 1 25 899 25 27 Example 2 7 390 22 10 Example 3 128 3093 198 98 Example 4 44 912 54 32 Example 5 11 569 20 33 Example 6 6 239 14 9 Example 7 18 701 28 18 Example 8 11 333 20 11 Example 9 6 471 19 5 Comparative Example 1 3 155 32 .1 Comparative Example 2 4 87 45 1 Comparative Example 3 2 62 21 4 Comparative Example 4 12 56 21 1 Comparative Example 5 12 59 28 3 Comparative Example 6 19 64 19 2 Comparative Example 7 562 540 6192 122 -32- 201138638 Examples 1 to 9 show that the silver concentration after 1 day is 5 ppb or more, and has nothing to do with whether or not there is water change, even after 2 1 days. When the concentration of silver is increased or decreased, the dissolution of silver occurs. Further, the meaning of the dissolution test at a high concentration of Na concentration of 500 ppm is based on the idea that ion exchange between Na ions and silver ions occurs rapidly, and silver ions eluted from the test piece are eluted and the concentration thereof is measured. It can reflect the amount of silver that it is dissolved. In this test, a test piece having a high silver concentration can be obtained, and since it is capable of dissolving a large amount of silver, it is sufficient to judge that it is highly sustained under normal use conditions. On the other hand, in Comparative Examples 1 to 3, the amount of elution after one day was small, and it took time to reach the silver concentration at which the antibacterial effect was obtained. Further, in Comparative Examples 1, 2 and 4, it was revealed that the silver concentration was lowered due to water exchange, and under the condition of exchange of water, the sufficient silver concentration at which the antibacterial effect was obtained could not be achieved. Comparative Examples 3 to 6: Since the silver concentration under the condition of a Na concentration of 50,000 p p m is low, the amount of silver eluted is small, and sustainability cannot be expected. Comparative Example 7: Since the concentration of silver after 21 days without water change was higher than the desired concentration, discoloration due to an excessively high concentration of silver ions was observed, and a certain concentration of silver ions could not be eluted. <Evaluation of long-term life> In addition, in order to investigate the long-term life' in the two types of Examples 3 and 4', the daily water exchange test was extended to 90 days. Thus, the silver ion concentration in the water on the 90th day was 13 PPb in Example 3, and 24 ppb' in Example 4 was opposite to the first day and the 21st day. Example 4 was higher than Example 3. This result shows that, compared with Example 3, the amount of silver eluted in the initial stage of Example 4 was less than -33-201138638, but the concentration variation was small and it was excellent in dissolution over a long period of time. <Evaluation of water treatment using industrial water> 100 g of each of the test pieces of Examples 3 and 4 and Comparative Examples 1, 3 and 7 were respectively placed in a water purifier, and the average number of bacteria was about 100 pieces/m. Industrial water having a water temperature of about 15 ° C was passed at 0.1 liter/min. According to the injection culture method using a general agar medium, the results of measuring the total number of bacteria in 1 ml of industrial water after 10 minutes and one day after passing water, and the results of measuring the concentration of dissolved silver at this time by ICP optical emission spectrometry In Table 3. Table 3 General bacteria number (cfu/ml) Silver concentration (mass ppb) Water time 1 minute after 1 day 1 minute after 1 minute 1 Example 3 Less than 1 Less than 1 42 3 1 Example 4 Less than 1 less than 1 12 18 Comparative Example 1 47 94 2 0 Comparative Example 3 29 73 9 3 Comparative Example 7 18 98 7 1 No antibacterial agent 98 1 10 — —— (The table is not measured) Example 3 and After 4, 10 minutes and 1 day, the antibacterial effect was confirmed, and the silver dissolution concentration was confirmed. On the other hand, in Comparative Examples 1, 3 and 7, the antibacterial effect and the silver elution concentration were significantly lowered after one day after 10 minutes. Since the molded article used in Comparative Example 7 showed that silver was continuously eluted and was not related to ion exchange, in the evaluation of the water exchange method shown in Table 2, it was confirmed that -34-201138638 even if the high concentration 'silver was reached, the dissolution continued. The result. On the other hand, in the test results of Table 3 of the water treatment evaluation, it was found that since the dissolution rate of silver was not high for water passage, it was found that the silver concentration after i 〇 minutes was not so high, and the dissolution rate after one day was not high. Then further decrease. Industrial Applicability The antibacterial treatment agent for water treatment of the present invention maintains a constant silver concentration and has long-term sustainability. Therefore, for clean water such as drinking water or circulating water, even if water is replaced by water or consumption, it can be adjusted to a certain amount of silver in the necessary amount of water, and the antibacterial effect is maintained for a long period of time. [Simple description of the diagram] Μ . ^\\\ [Main component symbol description] None. -35-

Claims (1)

201138638 七、申請專利範圍: 1. 一種水處理用抗菌處理劑,其特徵爲由含有:JISL 0105: 2006規定之標準水分百分率爲1〜10重量%之樹 脂、及1〜3 0重量%之作爲抗菌劑並以式〔1〕表示之經 銀取代之磷酸鉻的樹脂組成物而成, AgaMbZrcHfd(P〇4)3 · nHaO 〔 1〕 式〔1〕中,Μ爲至少一種選自於鹼金屬離子、鹼土金屬 離子、銨離子、氫離子及經離子所構成之群組的離子;a、 b及c分別爲獨立之整數;d爲0或整數;η爲0或2以 下之整數;a、b、c、及d係滿足於式〔Α〕之關係;Μ 爲1價時,係滿足於式〔Β〕; Μ爲2價時,係滿足於式 〔C〕, 1.75 &lt; c + d &lt; 2.25 〔 A〕 a+b+4(c+d)=9 〔B〕 a+2b+4(c+d) = 9 〔C〕。 2·如申請專利範圍第1項之水處理用抗菌處理劑,其中前 述經銀取代之磷酸锆的銀含有率爲4〜13重量%。 3. 如申請專利範圍第1項之水處理用抗菌處理劑,其中前 述處理劑之比表面積爲5〜100cm2/g。 4. 如申請專利範圍第1項之水處理用抗菌處理劑,其中構 成前述樹脂組成物之樹脂的50〜100重量%爲聚醯胺樹 脂。 5. 如申請專利範圍第4項之水處理用抗菌處理劑,其中前 -36- 201138638 述聚醯胺樹脂爲耐綸6。 6. —種如申請專利範圍第1至5項中任一項之水處理用抗 菌處理劑之製造方法,其係包含將前述抗菌劑與前述樹 脂予以混合之步驟。 7·—種水處理方法,其係包含使如申請專利範圍第1至5 項中任一項之水處理用抗菌處理劑與水接觸之步驟。 -37- 201138638 四、指定代表圖: (一) 本案指定代表圖為:無。 (二) 本代表圖之元件符號簡單說明: 4^: 〇 五、本案若有化學式時,請揭示最能顯示發明特徵的化學式:201138638 VII. Patent application scope: 1. An antibacterial treatment agent for water treatment, characterized by comprising: a resin having a standard moisture percentage of 1 to 10% by weight as specified in JISL 0105:2006, and 1 to 30% by weight The antibacterial agent is a resin composition of the silver-substituted chromium phosphate represented by the formula [1], and AgaMbZrcHfd(P〇4)3 · nHaO [1] wherein, in the formula [1], at least one selected from the group consisting of alkali metals An ion, an alkaline earth metal ion, an ammonium ion, a hydrogen ion, and a group of ions formed by ions; a, b, and c are independent integers; d is 0 or an integer; η is an integer of 0 or less; a, b, c, and d are satisfied with the relationship of the formula [Α]; Μ is 1 valence, satisfying the formula [Β]; Μ is 2 valence, satisfying the formula [C], 1.75 &lt; c + d &lt; 2.25 [ A] a + b + 4 (c + d) = 9 [B] a + 2b + 4 (c + d) = 9 [C]. 2. The antibacterial treatment agent for water treatment according to the first aspect of the invention, wherein the silver content of the silver-substituted zirconium phosphate is 4 to 13% by weight. 3. The antibacterial treatment agent for water treatment according to the first aspect of the invention, wherein the treatment agent has a specific surface area of 5 to 100 cm 2 /g. 4. The antibacterial treatment agent for water treatment according to claim 1, wherein 50 to 100% by weight of the resin constituting the resin composition is a polyamide resin. 5. For the antibacterial treatment agent for water treatment according to item 4 of the patent application, the poly-amide resin described in the former -36-201138638 is nylon 6. The method for producing an antibacterial treatment agent for water treatment according to any one of claims 1 to 5, which comprises the step of mixing the antibacterial agent with the aforementioned resin. A water treatment method comprising the step of bringing the antibacterial treatment agent for water treatment according to any one of claims 1 to 5 into contact with water. -37- 201138638 IV. Designated representative map: (1) The representative representative of the case is: None. (2) A brief description of the symbol of the representative figure: 4^: 〇 5. If there is a chemical formula in this case, please disclose the chemical formula that best shows the characteristics of the invention:
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Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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JP4893184B2 (en) * 2006-09-22 2012-03-07 東亞合成株式会社 Silver inorganic antibacterial agent
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CN101596603A (en) * 2009-07-06 2009-12-09 魏珊珊 A kind of preparation method and its usage of reducing nano-silver by phosphate

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