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JP6444083B2 - Water purifier cartridge and water purifier - Google Patents
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JP6444083B2 - Water purifier cartridge and water purifier - Google Patents

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JP6444083B2
JP6444083B2 JP2014149627A JP2014149627A JP6444083B2 JP 6444083 B2 JP6444083 B2 JP 6444083B2 JP 2014149627 A JP2014149627 A JP 2014149627A JP 2014149627 A JP2014149627 A JP 2014149627A JP 6444083 B2 JP6444083 B2 JP 6444083B2
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治雄 横田
治雄 横田
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Organo Corp
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Description

本発明は、浄水器用カートリッジおよび浄水器に関する。   The present invention relates to a water purifier cartridge and a water purifier.

軟水の効能として、(a)お茶やコーヒーの味をまろやかにする、(b)調理器具等のスケール発生を防止する、(c)石鹸の泡立ちが良くなる、(d)グラス等容器へのウォーターマーク発生を抑制する、等がある。このため、従来から、軟化機能を有した浄水器が広く利用されている。このような浄水器としては、例えば、容器内にカチオン交換樹脂を充填した浄水器が利用されている。   As soft water effects, (a) mellow the taste of tea and coffee, (b) prevent scales from cooking utensils, etc. (c) improve the foaming of soap, (d) water into containers such as glasses For example, the generation of marks is suppressed. For this reason, conventionally, water purifiers having a softening function have been widely used. As such a water purifier, for example, a water purifier filled with a cation exchange resin in a container is used.

特許文献1(特開2014−100633号公報)には、筒状の容器内に低架橋度のNa型強酸性カチオン交換樹脂(アンバージェット(登録商標)1220)を充填した浄水器が開示されている(段落[0057])。   Patent Document 1 (Japanese Patent Laid-Open No. 2014-100635) discloses a water purifier in which a cylindrical container is filled with a Na-type strongly acidic cation exchange resin (Amberjet (registered trademark) 1220) having a low crosslinking degree. (Paragraph [0057]).

特開2014−100633号公報JP 2014-100653 A

強酸性カチオン交換樹脂は水と接触することにより、少なからず不純物等に由来する成分の溶出が起こる。この溶出は強酸性カチオン交換樹脂と水との接触時間が長くなるほど増加する。特に、浄水器においては、水道水質基準項目として規定されているような人間の健康や生活環境に悪影響を与える物質の溶出は極力、防止する必要がある。   When a strongly acidic cation exchange resin comes into contact with water, elution of components derived from impurities and the like occurs. This elution increases as the contact time between the strongly acidic cation exchange resin and water increases. In particular, in water purifiers, it is necessary to prevent as much as possible the elution of substances that adversely affect human health and the living environment as specified in the tap water quality standard items.

浄水器に供給される水は基本的に水道水となるため、本発明者らは、水道水と強酸性カチオン交換樹脂が接触することによる強酸性カチオン交換樹脂からの溶出物について調査した。その結果、水道水中の残留塩素の有無にかかわらず、水道水と強酸性カチオン交換樹脂とが接触することにより、強酸性カチオン交換樹脂からホルムアルデヒドが溶出することを見出した。従って、ホルムアルデヒドの溶出は、残留塩素等による強酸性カチオン交換樹脂の酸化分解が原因ではないものと考えられる。   Since the water supplied to the water purifier is basically tap water, the present inventors investigated the eluate from the strong acid cation exchange resin due to contact between the tap water and the strong acid cation exchange resin. As a result, it was found that formaldehyde is eluted from the strongly acidic cation exchange resin by contacting the tap water with the strongly acidic cation exchange resin regardless of the presence or absence of residual chlorine in the tap water. Therefore, it is considered that the elution of formaldehyde is not caused by oxidative decomposition of the strongly acidic cation exchange resin due to residual chlorine or the like.

また、一般的に、浄水器の使用方法は連続的ではなく、間欠使用となる。例えば、家庭での浄水器の使用では、深夜の睡眠時間帯は未使用状態となる。この未使用時間が長くなるほど、翌朝の開始直後の浄水器出口水の溶出物濃度は高くなり、ホルムアルデヒド濃度は高くなった。従って、一定時間、使用を停止した後の浄水器において、使用開始時の強酸性カチオン交換樹脂からのホルムアルデヒドの溶出を抑制する必要があった。   Moreover, generally the usage method of a water purifier is not continuous but becomes intermittent use. For example, when the water purifier is used at home, the sleeping hours at midnight are unused. The longer this unused time, the higher the eluate concentration of the water purifier outlet water immediately after the start of the next morning, and the higher the formaldehyde concentration. Therefore, in the water purifier after being stopped for a certain period of time, it was necessary to suppress the elution of formaldehyde from the strongly acidic cation exchange resin at the start of use.

本発明は、上記課題に鑑みてなされたものである。すなわち、本発明は、一定時間、使用を停止した後に使用を開始した場合であっても、処理水(浄水器に通水後の水)へのホルムアルデヒドの溶出を抑制する浄水器用カートリッジ及び浄水器を提供することを目的とする。   The present invention has been made in view of the above problems. That is, the present invention relates to a water purifier cartridge and a water purifier that suppresses the elution of formaldehyde into treated water (water after passing through the water purifier) even when the use is stopped after being stopped for a certain period of time. The purpose is to provide.

一実施形態は、
架橋度が16〜24%の強酸性カチオン交換樹脂を単独で充填した浄水器用カートリッジであって、原水を通水した際の処理水中のホルムアルデヒド濃度が0.013mg/L以下に抑制されることを特徴とする浄水器用カートリッジおよび浄水器に関する。
また他の実施形態は、架橋度が16〜24%の強酸性カチオン交換樹脂を単独で充填した浄水器用カートリッジに原水を通水し、ホルムアルデヒド濃度が0.013mg/L以下に抑制された処理水を製造することを特徴とする処理水の製造方法に関する。
One embodiment is:
It is a cartridge for a water purifier filled with a strong acid cation exchange resin having a crosslinking degree of 16 to 24% alone, and the concentration of formaldehyde in the treated water when raw water is passed is suppressed to 0.013 mg / L or less. The present invention relates to a water purifier cartridge and a water purifier.
In another embodiment, raw water is passed through a cartridge for water purifier alone filled with a strong acid cation exchange resin having a crosslinking degree of 16 to 24%, and the treated water in which the formaldehyde concentration is suppressed to 0.013 mg / L or less. It is related with the manufacturing method of the treated water characterized by manufacturing.

一定時間、使用を停止した後に使用を開始した場合であっても、処理水へのホルムアルデヒドの溶出を抑制する浄水器用カートリッジおよび浄水器を提供することができる。   Even if it is a case where use is started after stopping use for a fixed time, the cartridge for water purifiers and water purifier which suppress elution of formaldehyde to treated water can be provided.

一実施形態は、架橋度が16〜24%の強酸性カチオン交換樹脂を充填した浄水器用カートリッジに関するものである。他の実施形態は、通水方向において、活性炭と、強酸性カチオン交換樹脂とをこの順に配置した浄水器用カートリッジと、浄水器用カートリッジを収容するハウジングと、を備えた浄水器に関するものである。ホルムアルデヒドは強酸性カチオン交換樹脂の構造の一部が脱離、分解等により遊離、または反応することで処理水中に溶出するものと考えられる。そこで、強酸性カチオン交換樹脂の架橋度を16〜24%にすることで樹脂の構造の一部が脱離、分解、反応等を起こすことを抑制できる。この結果、ホルムアルデヒドが処理水(浄水器に通水後の水)中に溶出することを効果的に抑制できる。架橋度が16%未満では、強酸性カチオン交換樹脂の構造強度が不十分となり、ホルムアルデヒドの溶出が起こりやすくなる。一方、架橋度が24%を超えると、イオン交換速度が遅くなったり、強酸性カチオン交換樹脂の再生速度が遅くなったりする。   One embodiment relates to a water purifier cartridge filled with a strongly acidic cation exchange resin having a crosslinking degree of 16 to 24%. Other embodiment is related with the water purifier provided with the cartridge for water purifiers which arrange | positioned activated carbon and strong acid cation exchange resin in this order in the water flow direction, and the housing which accommodates the cartridge for water purifiers. Formaldehyde is considered to elute into the treated water when a part of the structure of the strongly acidic cation exchange resin is released or reacted by desorption or decomposition. Thus, by setting the degree of cross-linking of the strongly acidic cation exchange resin to 16 to 24%, it is possible to suppress part of the resin structure from desorbing, decomposing, reacting, and the like. As a result, it can suppress effectively that formaldehyde elutes in treated water (water after passing through a water purifier). If the degree of cross-linking is less than 16%, the structural strength of the strongly acidic cation exchange resin becomes insufficient, and elution of formaldehyde tends to occur. On the other hand, when the degree of cross-linking exceeds 24%, the ion exchange rate becomes slow, or the regeneration rate of the strongly acidic cation exchange resin becomes slow.

強酸性カチオン交換樹脂の架橋度は、強酸性カチオン交換樹脂用の原料中の架橋剤の含量によって決定される。例えば、メタクリル系、アクリル系、またはスチレン系の強酸性カチオン交換樹脂の場合には、原料中の架橋剤であるジビニルベンゼンの含量によって架橋度が決定される。   The degree of crosslinking of the strongly acidic cation exchange resin is determined by the content of the crosslinking agent in the raw material for the strongly acidic cation exchange resin. For example, in the case of a methacrylic, acrylic or styrene strongly acidic cation exchange resin, the degree of crosslinking is determined by the content of divinylbenzene as a crosslinking agent in the raw material.

強酸性カチオン交換樹脂は、ゲル型構造、マクロポーラス型構造、およびポーラス型構造のうち、何れの構造を有することもできる。好ましくは、強酸性カチオン交換樹脂は、マクロポーラス型構造、またはポーラス型構造の構造を有するのが良い。   The strongly acidic cation exchange resin can have any structure among a gel type structure, a macroporous type structure, and a porous type structure. Preferably, the strongly acidic cation exchange resin may have a macroporous structure or a porous structure.

なお、ゲル型構造と、マクロポーラス型構造およびポーラス型構造とは、下記の方法によって判別することができる。   The gel type structure, the macroporous type structure and the porous type structure can be distinguished by the following method.

強酸性カチオン交換樹脂は塩形であってもH形であっても良い。塩形の強酸性カチオン交換樹脂の種類は特に限定されないが、例えば、Na形の酸性カチオン交換樹脂、K形の強酸性カチオン交換樹脂を挙げることができる。なお、強酸性カチオン交換樹脂に対応する溶液を通液することによって所望のH形、または塩形とすることができる(例えば、H形ではHCl水溶液、Na形ではNaOH水溶液、K形ではKOH水溶液を通液することができる)。 The strongly acidic cation exchange resin may be in a salt form or an H form. Type strongly acidic cation exchange resin of the salt form is not particularly limited, for example, a Na type strong acidic cation exchange resin, K-type strongly acidic cation exchange resin. A desired H form or salt form can be obtained by passing a solution corresponding to the strongly acidic cation exchange resin (for example, HCl aqueous solution in H form, NaOH aqueous solution in Na form, KOH aqueous solution in K form). Can be passed through).

強酸性カチオン交換樹脂の母体構造は特に限定されないが例えば、メタクリル系、アクリル系、またはスチレン系の強酸性カチオン交換樹脂とすることができる。   The matrix structure of the strongly acidic cation exchange resin is not particularly limited, and for example, it can be a methacrylic, acrylic or styrene strong acid cation exchange resin.

強酸性カチオン交換樹脂は、架橋度が16〜24%のものであれば市販のものを使用することができる。ゲル型構造の強酸性カチオン交換樹脂としては、アンバージェット 1060,1600(Amberjet;登録商標)、ダイヤイオン SK116(Diaion;登録商標)、ピュロライト C100X16MBH(Purolite;登録商標)を挙げることができる。マクロポーラス型構造の強酸性カチオン交換樹脂としては、アンバーライト 200C、200CT(AMBERLITE;登録商標)、アンバーレックス 210(AMBEREX;登録商標)を挙げることができる。   As the strongly acidic cation exchange resin, a commercially available one can be used as long as the degree of crosslinking is 16 to 24%. Examples of the strongly acidic cation exchange resin having a gel type structure include Amberjet 1060, 1600 (Amberjet; registered trademark), Diaion SK116 (Diaion; registered trademark), and Purolite C100X16MBH (Purolite; registered trademark). Examples of the strongly acidic cation exchange resin having a macroporous structure include Amberlite 200C, 200CT (AMBERLITE; registered trademark), and Amberlex 210 (AMBEREX; registered trademark).

強酸性カチオン交換樹脂の前段(通水方向に対して上流側)に、活性炭を設け、活性炭と強酸性カチオン交換樹脂をこの順に配置した浄水器用カートリッジ、及びこれを備えた浄水器としても良い。この活性炭により、水中のカチオン成分以外の有機物、溶存酸素、残留塩素等を除去して、水の純度を更に向上させることができる。   It is good also as a water purifier cartridge which provided activated carbon in the front | former stage (upstream side with respect to a water flow direction) of strong acid cation exchange resin, and has arrange | positioned activated carbon and strong acid cation exchange resin in this order, and this. This activated carbon can remove organic substances other than the cation component in water, dissolved oxygen, residual chlorine, and the like, thereby further improving the purity of water.

浄水器の形態は特に限定されないが例えば、ハウジングと、ハウジングの上部に設けられた原水入口と、ハウジングの下部に設けられた浄水出口とを有し、ハウジング内に浄水器用カートリッジが配置され、浄水器用カートリッジは原水入口と浄水出口に連通するものを挙げることができる。浄水器の種類としては特に限定されないが、例えば、ポット型、蛇口直結型、据え置き型、またはアンダーシンク型の浄水器を使用することができる。   The form of the water purifier is not particularly limited. For example, the water purifier has a housing, a raw water inlet provided in the upper part of the housing, and a water outlet provided in the lower part of the housing, and a water purifier cartridge is disposed in the housing. The cartridge for equipment can be one that communicates with the raw water inlet and the purified water outlet. Although it does not specifically limit as a kind of water purifier, For example, a pot type, a faucet direct connection type, a stationary type, or an undersink type water purifier can be used.

以下、実施例を参照して本発明をさらに詳細に説明するが、本発明はこれらの実施例によって限定されるものではない。   EXAMPLES Hereinafter, although this invention is demonstrated further in detail with reference to an Example, this invention is not limited by these Examples.

[実施例1]
内径4.6cm、高さ100cmのアクリルカラム内に、架橋度が20%でマクロポーラス型構造を有するNa形の強酸性カチオン交換樹脂(商品名;アンバーライト(登録商標) 200CT(ダウ・ケミカル社製))を900ml、充填し、そのカートリッジ内に水温23℃の相模原市水をSV60BV/時間で15分間、通水を行った。その後、24時間、放置(23℃に調製した室内にて水浸漬状態)し、再び23℃の水道水をSV60BV/時間で1分間、通水し、その流出水(処理水)を採取し、ホルムアルデヒド濃度を分析した。なお、ホルムアルデヒド濃度は、JIS S 3200−7:2004 附属書9に従い、ホルムアルデヒドの溶媒抽出−ホルムアルデヒドの誘導体化−ガスクロマトグラフ質量分析を用いた方法により行った。
[Example 1]
Na type strongly acidic cation exchange resin (trade name; Amberlite (registered trademark) 200CT (Dow Chemical Co., Ltd.) in an acrylic column having an inner diameter of 4.6 cm and a height of 100 cm and having a macroporous structure with a crosslinking degree of 20%. The product was filled with 900 ml of Sagamihara-shi water having a water temperature of 23 ° C. at SV60 BV / hour for 15 minutes. Then, it is left for 24 hours (in a room immersed in a room adjusted to 23 ° C.), and again the tap water at 23 ° C. is passed for 1 minute at SV60 BV / hour, and the effluent water (treated water) is collected. The formaldehyde concentration was analyzed. The formaldehyde concentration was determined by a method using solvent extraction of formaldehyde, derivatization of formaldehyde, and gas chromatography mass spectrometry according to JIS S 3200-7: 2004 Annex 9.

[実施例2]
実施例1において、Na形強酸性カチオン交換樹脂を、架橋度16%でゲル型構造を有する強酸性カチオン交換樹脂(商品名;アンバージェット(登録商標) 1060(ダウ・ケミカル社製))に変更した。これ以外は実施例1と同様にして、通水を行いホルムアルデヒド濃度を測定した。
[Example 2]
In Example 1, the Na-type strongly acidic cation exchange resin was changed to a strongly acidic cation exchange resin (trade name; Amberjet (registered trademark) 1060 (manufactured by Dow Chemical Company)) having a gel-type structure with a crosslinking degree of 16%. did. Except for this, water was passed through in the same manner as in Example 1 to measure the formaldehyde concentration.

[実施例3]
浄水器への供給水を、残留塩素および溶存酸素を除去した相模原市水に変更した以外は実施例1と同様にして、通水を行いホルムアルデヒド濃度を測定した。なお、残留塩素については活性炭、溶存酸素については脱気膜で除去した。
[Example 3]
Water was passed in the same manner as in Example 1 except that the water supplied to the water purifier was changed to Sagamihara City water from which residual chlorine and dissolved oxygen were removed, and the formaldehyde concentration was measured. Residual chlorine was removed with activated carbon, and dissolved oxygen was removed with a degassing membrane.

[実施例4]
浄水器への供給水を、残留塩素および溶存酸素を除去した相模原市水に変更した以外は実施例2と同様にして、通水を行いホルムアルデヒド濃度を測定した。なお、残留塩素および溶存酸素の除去は実施例3と同様に行った。
[Example 4]
Water was passed in the same manner as in Example 2 except that the water supplied to the water purifier was changed to Sagamihara City water from which residual chlorine and dissolved oxygen were removed, and the formaldehyde concentration was measured. The residual chlorine and dissolved oxygen were removed in the same manner as in Example 3.

[比較例1]
実施例1において、使用するNa形の強酸性カチオン交換樹脂を、架橋度が8%でゲル型構造を有する強酸性カチオン交換樹脂(アンバージェット(登録商標) 1220;ダウ・ケミカル社製)に変更した。これ以外は実施例1と同様にして、通水を行いホルムアルデヒド濃度を測定した。
[Comparative Example 1]
In Example 1, the Na-type strongly acidic cation exchange resin used was changed to a strongly acidic cation exchange resin (Amberjet (registered trademark) 1220; manufactured by Dow Chemical Co., Ltd.) having a gel-type structure with a crosslinking degree of 8%. did. Except for this, water was passed through in the same manner as in Example 1 to measure the formaldehyde concentration.

[比較例2]
実施例3において、使用するNa形の強酸性カチオン交換樹脂を、架橋度が8%でゲル型構造を有する強酸性カチオン交換樹脂(アンバージェット(登録商標) 1220;ダウ・ケミカル社製)に変更した。これ以外は実施例3と同様にして、通水を行いホルムアルデヒド濃度を測定した。
[Comparative Example 2]
In Example 3, the Na-type strongly acidic cation exchange resin used was changed to a strongly acidic cation exchange resin (Amberjet (registered trademark) 1220; manufactured by Dow Chemical Co., Ltd.) having a crosslinking degree of 8% and a gel-type structure. did. Except for this, water was passed through in the same manner as in Example 3 to measure the formaldehyde concentration.

[比較例3]
実施例1において、使用するNa形の強酸性カチオン交換樹脂を、架橋度が12%でゲル型構造を有する強酸性カチオン交換樹脂(アンバージェット(登録商標) 1024;ダウ・ケミカル社製)に変更した。これ以外は実施例1と同様にして、通水を行いホルムアルデヒド濃度を測定した。
[Comparative Example 3]
In Example 1, the Na-type strongly acidic cation exchange resin used was changed to a strongly acidic cation exchange resin (Amberjet (registered trademark) 1024; manufactured by Dow Chemical Co., Ltd.) having a gel degree structure with a crosslinking degree of 12%. did. Except for this, water was passed through in the same manner as in Example 1 to measure the formaldehyde concentration.

(結果)
実施例1〜4および比較例1〜3における、使用した強酸性カチオン交換樹脂の種類を表1、浄水器に通水後の処理水中のホルムアルデヒド濃度を表2に示す。なお、浄水器に通水前の供給水中のホルムアルデヒド濃度は、相模原市水、ならびに残留塩素および溶存酸素を除去した相模原市水とも、0.005mg/L未満であった。
(result)
Table 1 shows the types of strong acidic cation exchange resins used in Examples 1 to 4 and Comparative Examples 1 to 3, and Table 2 shows the formaldehyde concentration in the treated water after passing through the water purifier. The formaldehyde concentration in the feed water before passing through the water purifier was less than 0.005 mg / L for both Sagamihara city water and Sagamihara city water from which residual chlorine and dissolved oxygen were removed.

Figure 0006444083
Figure 0006444083

Figure 0006444083
Figure 0006444083

表2の結果より、何れの実施例および比較例でも、供給水(相模原市水、ならびに残留塩素および溶存酸素を除去した相模原市水)と比較して、処理水中のホルムアルデヒド濃度は増加することが分かる。しかしながら、何れの実施例も処理水中のホルムアルデヒド濃度は、比較例における処理水中のホルムアルデヒド濃度よりも低い値を示した。発明者の事前の調査から、強酸性カチオン交換樹脂の水中への浸漬時間が増加するにつれて処理水中のホルムアルデヒド濃度は増加したことから、上記のように実施例における処理水中のホルムアルデヒド濃度が低減されたのは、強酸性カチオン交換樹脂から処理水中へのホルムアルデヒドの溶出が抑制されたためと考えられる。また、実施例3および4、ならびに比較例2では、供給水として残留塩素および溶存酸素を除去した相模原市水を使用したにもかかわらず、処理水中にはホルムアルデヒドが溶出していることから、ホルムアルデヒドは、塩素や溶存酸素等による強酸性カチオン交換樹脂の酸化劣化とは異なるメカニズムにより処理水中に溶出しているものと考えられる。   From the results of Table 2, in any of the examples and comparative examples, the concentration of formaldehyde in the treated water may increase as compared with the feed water (Sagamihara city water and Sagamihara city water from which residual chlorine and dissolved oxygen have been removed). I understand. However, in all Examples, the formaldehyde concentration in the treated water was lower than the formaldehyde concentration in the treated water in the comparative example. From the inventor's previous investigation, the formaldehyde concentration in the treated water increased as the immersion time of the strongly acidic cation exchange resin in water increased, so the formaldehyde concentration in the treated water in the examples was reduced as described above. This is probably because elution of formaldehyde from the strongly acidic cation exchange resin into the treated water was suppressed. In Examples 3 and 4 and Comparative Example 2, formaldehyde was eluted in the treated water despite the use of Sagamihara city water from which residual chlorine and dissolved oxygen were removed as the feed water. Is considered to be eluted in the treated water by a mechanism different from the oxidative degradation of the strongly acidic cation exchange resin due to chlorine, dissolved oxygen, or the like.

Claims (5)

架橋度が16〜24%の強酸性カチオン交換樹脂を単独で充填した浄水器用カートリッジであって、原水を通水した際の処理水中のホルムアルデヒド濃度が0.013mg/L以下に抑制されることを特徴とする浄水器用カートリッジ。   It is a cartridge for a water purifier filled with a strong acid cation exchange resin having a crosslinking degree of 16 to 24% alone, and the concentration of formaldehyde in the treated water when raw water is passed is suppressed to 0.013 mg / L or less. Features a water purifier cartridge. 通水方向において、活性炭と、強酸性カチオン交換樹脂とをこの順に配置した浄水器用カートリッジであって、該強酸性カチオン交換樹脂として架橋度が16〜24%の強酸性カチオン交換樹脂を単独で充填しており、原水を通水した際の処理水中のホルムアルデヒド濃度が0.013mg/L以下に抑制されることを特徴とする浄水器用カートリッジ。 A water purifier cartridge in which activated carbon and a strong acid cation exchange resin are arranged in this order in the direction of water flow, and the strong acid cation exchange resin is filled with a strong acid cation exchange resin having a crosslinking degree of 16 to 24% as the strong acid cation exchange resin. And the formaldehyde concentration in the treated water when raw water is passed is suppressed to 0.013 mg / L or less . 前記強酸性カチオン交換樹脂は、ポーラス型構造またはマクロポーラス型構造を有することを特徴とする請求項1又は2に記載の浄水器用カートリッジ。 The cartridge for water purifier according to claim 1 or 2, wherein the strongly acidic cation exchange resin has a porous structure or a macroporous structure . 請求項1〜3の何れか1項に記載の浄水器用カートリッジと、
前記浄水器用カートリッジを収容するハウジングと、
を備えたことを特徴とする浄水器。
The water purifier cartridge according to any one of claims 1 to 3,
A housing for housing the water purifier cartridge;
A water purifier characterized by comprising
架橋度が16〜24%の強酸性カチオン交換樹脂を単独で充填した浄水器用カートリッジに原水を通水し、ホルムアルデヒド濃度が0.013mg/L以下に抑制された処理水を製造することを特徴とする処理水の製造方法。   The raw water is passed through a cartridge for a water purifier alone filled with a strongly acidic cation exchange resin having a crosslinking degree of 16 to 24% to produce treated water in which the formaldehyde concentration is suppressed to 0.013 mg / L or less. To produce treated water.
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