JP6639812B2 - CIP cleaning method - Google Patents

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JP6639812B2
JP6639812B2 JP2015120426A JP2015120426A JP6639812B2 JP 6639812 B2 JP6639812 B2 JP 6639812B2 JP 2015120426 A JP2015120426 A JP 2015120426A JP 2015120426 A JP2015120426 A JP 2015120426A JP 6639812 B2 JP6639812 B2 JP 6639812B2
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吉央 島村
吉央 島村
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Adeka Corp
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本発明は、CIP洗浄用組成物を用いたCIP洗浄方法に関し、更に詳細には、飲食料品工場の製造ラインのCIP洗浄方法に関する。   The present invention relates to a CIP cleaning method using a CIP cleaning composition, and more particularly, to a CIP cleaning method for a production line of a food and beverage factory.

ビール、ジュース、乳飲料等の飲料、乳製品、冷凍食品、レトルト食品、調味料、マヨネーズ等の食品を製造する飲食料品製造工場では、その製造設備や製造機器類のためにCIP洗浄によって洗浄を行っている。CIP洗浄とは“Cleaning in place”の頭文字をとったもので、製造設備や製造機器類を分解することなく、そのままの状態で洗浄液を流通させてその内部を満たして循環させたり、さらには洗浄液をスプレーしたりして、残留汚れを洗浄・除去する洗浄方法であり、定置洗浄又は定置循環洗浄とも呼ばれている。   In food and beverage manufacturing plants that manufacture foods such as beer, juice, dairy beverages, dairy products, frozen foods, retort foods, seasonings, mayonnaise, etc., they are cleaned by CIP cleaning for their manufacturing facilities and equipment. It is carried out. CIP cleaning is an acronym for “Cleaning in place”, which allows a cleaning liquid to flow as it is without disassembling manufacturing equipment and manufacturing equipment, and to fill and circulate the cleaning liquid. This is a cleaning method of spraying a cleaning liquid to wash and remove residual stains, and is also called stationary cleaning or stationary circulation cleaning.

従来、CIP洗浄では、アルカリ洗浄や、アルカリ洗浄に酸洗浄を組み合わせた洗浄が行われている。なかでも飲食料品製造工場では製品由来の有機物汚れと無機物汚れが発生することから、高い清浄度を保つために、アルカリ洗浄工程で金属イオン封鎖剤を併用したり、アルカリ洗浄工程と酸洗浄工程とを組み合わせたり、アルカリ洗浄、酸洗浄工程に更に、除菌剤による除菌工程を組み合わせたCIP洗浄も行われている。   Conventionally, in CIP cleaning, alkali cleaning or cleaning combining acid cleaning with alkali cleaning is performed. Among them, food and beverage manufacturing plants produce organic and inorganic stains derived from products.To maintain high cleanliness, use a sequestering agent in the alkaline washing step, or use an alkaline washing step and an acid washing step. CIP cleaning is also performed in which an alkali cleaning and an acid cleaning steps are combined with a disinfection step using a disinfectant.

従来、CIP洗浄に用いられる洗浄剤組成物や洗浄方法が種々提案されており、例えば水酸化ナトリウム及びグルタミン酸塩類等を含有する洗浄剤組成物を用いる方法(特許文献1)、水酸化アルカリ金属塩、アルキルポリグルコシド、ポリオキシアルキレンエーテル及び/又はポリオキシアルキレンアルキルフェニルエーテル、金属イオン封鎖剤、高分子ポリマーを含有する組成物(特許文献2)が提案されている。また除菌機能を有するものとしては、次亜塩素酸塩とイソシアヌル酸又はその塩を含むもの(特許文献3)、水酸化アルカリ金属塩、塩素系酸化剤、ケイ酸塩、ホスホン酸塩、両性界面活性剤を含むもの(特許文献4)等が知られている。   Conventionally, various cleaning compositions and cleaning methods used for CIP cleaning have been proposed. For example, a method using a cleaning composition containing sodium hydroxide and glutamates (Patent Document 1), an alkali metal hydroxide salt , A composition containing an alkyl polyglucoside, a polyoxyalkylene ether and / or a polyoxyalkylene alkyl phenyl ether, a sequestering agent, and a high-molecular polymer (Patent Document 2). Further, those having a disinfecting function include those containing hypochlorite and isocyanuric acid or a salt thereof (Patent Document 3), alkali metal hydroxide salts, chlorinated oxidizing agents, silicates, phosphonates, amphoteric One containing a surfactant (Patent Document 4) is known.

特許第4114820号Patent No. 4114820 特開2006−265469号JP 2006-265469 A 特許第5007203号Patent No. 5007203 特開2010−215780号JP 2010-215780 A

しかしながら特許文献1、特許文献2に開示されているCIP洗浄方法は、水酸化ナトリウム等のアルカリと金属イオン封鎖剤とを組み合わせたアルカリ洗浄の技術であり、飲食料品製造工場におけるCIP洗浄に適用した場合、十分な汚れ除去が困難であり、アルカリ洗浄工程の前後に更に酸洗浄工程を組み合わせる必要がある。しかしながらアルカリ洗浄工程と酸洗浄工程とを組み合わせてCIP洗浄を行う場合、アルカリ洗浄工程と酸洗浄工程との間ですすぎ工程が必要であり、洗浄のサイクルが長くなるという問題がある。特に近年、生産効率向上による生産量の増加や顧客の嗜好の多様化により飲食料品の品種が増加し、生産品の切り替えのためのCIP洗浄の頻度が増えており、CIP洗浄に長時間を要することは生産効率の著しい低下原因となっている。また特許文献3、4記載のCIP洗浄方法も、次亜塩素酸等の塩素系除菌剤を用いるため、酸洗浄工程を組み合わせる場合、有毒な塩素ガス発生を防止するためにすすぎ工程において十分なすすぎが必要であり、更に洗浄サイクルが長くなるという問題があった。しかも飲食料品製造工場では、多糖類やバイオフィルム等の汚れが発生し易いが、従来のCIP洗浄剤方法では、多糖類やバイオフィルムの汚れは除去が難しく、特に塩素系除菌剤を用いた除菌工程を組み合わせて行う場合、塩素失活の少ない低い温度で洗浄すると、洗浄性、除菌性が低下するという問題があった。   However, the CIP cleaning methods disclosed in Patent Literature 1 and Patent Literature 2 are techniques of alkaline cleaning using a combination of an alkali such as sodium hydroxide and a sequestering agent, and are applied to CIP cleaning in a food and beverage manufacturing plant. In this case, it is difficult to sufficiently remove dirt, and it is necessary to further combine an acid cleaning step before and after the alkali cleaning step. However, when performing the CIP cleaning by combining the alkali cleaning step and the acid cleaning step, a rinsing step is required between the alkali cleaning step and the acid cleaning step, and there is a problem that the cleaning cycle becomes long. In particular, in recent years, the variety of foods and beverages has increased due to an increase in production volume due to improvement in production efficiency and diversification of customer preferences, and the frequency of CIP cleaning for switching products has increased. The necessity causes a significant decrease in production efficiency. Also, in the CIP cleaning methods described in Patent Documents 3 and 4, since a chlorine-based disinfectant such as hypochlorous acid is used, when the acid cleaning step is combined, sufficient rinsing step is required to prevent generation of toxic chlorine gas. There is a problem that rinsing is required and the washing cycle is further lengthened. Moreover, in a food and beverage manufacturing plant, dirt such as polysaccharides and biofilms is easily generated. However, it is difficult to remove dirt from polysaccharides and biofilms by the conventional CIP cleaning method. When performing the combined sterilization steps, there is a problem that washing at a low temperature with little chlorine inactivation degrades the washing property and the sterilization property.

本発明は上記従来の課題を解決すべくなされたもので、酸洗浄工程を行わなくても飲食料品工場における有機物汚れ、無機物汚れの効率的除去と除菌とを同時に行うことができ、しかも低温で洗浄しても短時間で効率良く汚れ除去、除菌を行うことができるCIP洗浄方法を提供することを目的とする。   The present invention has been made to solve the above-mentioned conventional problems, and it is possible to simultaneously perform efficient removal of bacteria and inorganic bacteria and sterilization without performing an acid washing step, and furthermore, It is an object of the present invention to provide a CIP cleaning method capable of efficiently removing dirt and removing bacteria in a short time even if the cleaning is performed at a low temperature.

上記課題を解決するために、本発明者等は鋭意検討した結果、(A)アルカリ金属水酸化物及び/又はアルカリ土類金属水酸化物、(B)メチルグリシン二酢酸又はその塩、を含有し、(A)成分と(B)成分の質量比が、(A)/(B)=0.16〜190であるCIP用洗浄剤組成物を水で希釈した希釈洗浄液に対して、(C)成分として塩素系除菌剤を含有するCIP用添加剤を添加して有効塩素量0.005〜0.2質量%、(B)成分を0.001〜0.6質量%含有するCIP除菌洗浄液により、CIP除菌洗浄液の温度を10〜60℃として飲食料品製造ラインをCIP洗浄する方法が、従来のCIP洗浄方法が有していた問題を解決できることを見出し、本発明を完成するに至った。   In order to solve the above-mentioned problems, the present inventors have conducted intensive studies and as a result, have found that (A) an alkali metal hydroxide and / or an alkaline earth metal hydroxide, and (B) methylglycine diacetate or a salt thereof. Then, the mass ratio of the component (A) to the component (B) is (A) / (B) = 0.16 to 190. ) Addition of a CIP additive containing a chlorine-based disinfectant as a component to remove CIP containing 0.005 to 0.2% by mass of effective chlorine and 0.001 to 0.6% by mass of component (B). The present inventors have found that a method of CIP-cleaning a food and beverage production line by setting the temperature of a CIP sanitizing cleaning liquid to 10 to 60 ° C. using a bacterial cleaning liquid can solve the problems of the conventional CIP cleaning method, and complete the present invention. Reached.

即ち本発明は、
(1)(A)成分としてアルカリ金属水酸化物、(B)成分としてメチルグリシン二酢酸又はその塩を含有し、(A)成分と(B)成分の質量比が、(A)/(B)=0.16〜190であるCIP用洗浄剤組成物を水で希釈した希釈洗浄液に対して、(C)成分として塩素系除菌剤を含有するCIP用添加剤を添加して調製した、有効塩素量0.005〜0.2質量%、(B)成分を0.001〜0.6質量%含有する10〜60℃のCIP除菌洗浄液により飲食料品製造ラインのCIP洗浄及び除菌洗浄を同時に行うことを特徴とするCIP洗浄方法、
(2)(A)成分が水酸化ナトリウム、水酸化カリウムより選ばれた少なくとも一種以上を含有する上記(1)のCIP洗浄方法、
(3)(C)成分は、塩素系除菌剤として次亜塩素酸アルカリ金属塩及び/又は次亜塩素酸アルカリ土類金属塩、塩素化イソシアヌル酸塩から選ばれた少なくとも一種以上を含有する上記(1)又は(2)のCIP洗浄方法、
(4)さらに、(A)成分、(B)成分を含む前記CIP用洗浄剤組成物に、(D)成分として高分子ポリマーを、(B)成分と(D)成分の質量比が、(D)/(B)=0.05〜10になるように含有する上記(1)〜(3)のいずれかのCIP洗浄方法、
を要旨とする。
That is, the present invention
(1) (A) an alkali metal hydroxide compound as a component, contains methylglycine diacetic acid or a salt thereof, (A) component (B) weight ratio of the component (B), (A) / (B ) = 0.16 to 190, prepared by adding a CIP additive containing a chlorine-based disinfectant as a component (C) to a diluted washing solution obtained by diluting a CIP detergent composition with water. CIP cleaning and disinfection of food and beverage production line with a CIP disinfecting cleaning solution at 10 to 60 ° C containing 0.005 to 0.2% by mass of effective chlorine and 0.001 to 0.6% by mass of component (B) A CIP cleaning method, wherein the cleaning is performed simultaneously;
(2) The CIP cleaning method of the above (1), wherein the component (A) contains at least one selected from sodium hydroxide and potassium hydroxide,
(3) The component (C) contains at least one or more selected from alkali metal hypochlorite and / or alkaline earth metal hypochlorite and chlorinated isocyanurate as a chlorine-based disinfectant. (1) or (2) the CIP cleaning method,
(4) Further, in the CIP cleaning composition containing the components (A) and (B), a polymer is used as the component (D), and the mass ratio of the components (B) and (D) is ( D) / (B) = the CIP cleaning method according to any one of the above (1) to (3), which is contained so as to be 0.05 to 10.
Is the gist.

本発明のCIP洗浄方法は、酸洗浄を行わなくても飲食料品製造ラインで発生する有機汚れや無機汚れを確実かつ同時に洗浄除去することができるとともに、除菌も一工程で行うことができ、アルカリ洗浄、酸洗浄、除菌の三工程を組み合わせた洗浄が不要であるとともに、各工程間のすすぎ工程も不要となるため、洗浄サイクルが短く、生産品の切り替え時の洗浄時間を短縮でき、飲食料品の生産品種が多い場合であっても生産効率よく生産を行うことができる。また10〜60℃の洗浄液により洗浄するため塩素失活による除菌性が低下する虞がなく、低い温度で洗浄した際に除去することが困難であった多糖類やバイオフィルム等の汚れも効率よく洗浄除去することができる。   ADVANTAGE OF THE INVENTION The CIP washing | cleaning method of this invention can wash | clean and remove the organic dirt and inorganic dirt which generate | occur | produce in a food-and-drinks production line simultaneously without performing acid washing, and can also remove bacteria in one process. Cleaning is not required by combining the three steps of alkali cleaning, acid cleaning, and bacteria elimination, and the rinsing step between each step is also unnecessary.This shortens the cleaning cycle and reduces the cleaning time when switching between products. In addition, even when there are many types of food and beverage products, production can be performed with high production efficiency. In addition, since it is washed with a washing liquid at 10 to 60 ° C., there is no possibility that the disinfecting property due to chlorine inactivation may be reduced, and dirt such as polysaccharides and biofilms which are difficult to remove when washed at a low temperature can be efficiently treated. Can be washed and removed well.

本発明のCIP洗浄方法において用いる(A)成分としては、水酸化ナトリウム、水酸化カリウム等のアルカリ金属水酸化物、水酸化カルシウム、水酸化マグネシウム等のアルカリ土類金属水酸化物等が挙げられる。アルカリ金属水酸化物、アルカリ土類金属水酸化物は、1種又は2種以上を併用することができる。(A)成分としては、水酸化ナトリウム、水酸化カリウムが好ましい。(A)成分のアルカリ金属水酸化物及び/又はアルカリ土類金属水酸化物は、CIP洗浄剤組成物中に1〜40質量%含有することが好ましいが、3〜36質量%含有することがより好ましく、5〜32質量%含有することが最も好ましい。(A)成分が1質量%未満では洗浄性が低下する場合があり、40質量%を超えると貯蔵安定性が低下する場合がある。   The component (A) used in the CIP cleaning method of the present invention includes alkali metal hydroxides such as sodium hydroxide and potassium hydroxide, and alkaline earth metal hydroxides such as calcium hydroxide and magnesium hydroxide. . The alkali metal hydroxide and the alkaline earth metal hydroxide can be used alone or in combination of two or more. As the component (A), sodium hydroxide and potassium hydroxide are preferable. The alkali metal hydroxide and / or alkaline earth metal hydroxide of the component (A) is preferably contained in the CIP detergent composition in an amount of 1 to 40% by mass, but is preferably contained in an amount of 3 to 36% by mass. More preferably, the content is most preferably 5 to 32% by mass. If the amount of the component (A) is less than 1% by mass, the detergency may decrease, and if it exceeds 40% by mass, the storage stability may decrease.

(B)成分としては、メチルグリシン二酢酸、メチルグリシン二酢酸ナトリウム塩、メチルグリシン二酢酸カリウム塩等が用いられるが、メチルグリシン二酢酸ナトリウム塩、メチルグリシン二酢酸カリウム塩が好ましい。(B)成分のメチルグリシン二酢酸又はその塩は、CIP洗浄剤組成物中に0.001〜40質量%含有することが好ましいが、0.05〜10.1質量%含有することがより好ましく、0.1〜1質量%含有することが最も好ましい。メチルグリシン二酢酸又はその塩が0.001質量%未満では洗浄性が低下する場合があり、40質量%を超えると貯蔵安定性が低下する場合がある。本発明において用いるCIP洗浄剤組成物は、取り扱いやすい点から、(A)成分、(B)成分とともに水を含む水溶液の形態であることが好ましく、水溶液に使用する水としては、水道水、地下水、工業用水、イオン交換水、蒸留水等が挙げられるが、貯蔵安定性の点からイオン交換水や蒸留水が好ましい。   As the component (B), methyl glycine diacetate, methyl glycine diacetate sodium salt, methyl glycine diacetate potassium salt and the like are used, and methyl glycine diacetate sodium salt and methyl glycine diacetate potassium salt are preferred. Component (B) methylglycine diacetate or a salt thereof is preferably contained in the CIP detergent composition at 0.001 to 40% by mass, more preferably 0.05 to 10.1% by mass. , 0.1 to 1% by mass. If the amount of methyl glycine diacetic acid or a salt thereof is less than 0.001% by mass, detergency may decrease, and if it exceeds 40% by mass, storage stability may decrease. The CIP detergent composition used in the present invention is preferably in the form of an aqueous solution containing water together with the components (A) and (B) from the viewpoint of easy handling. Examples of the water used in the aqueous solution include tap water and groundwater. , Industrial water, ion-exchanged water, distilled water and the like, and ion-exchanged water and distilled water are preferred from the viewpoint of storage stability.

(C)成分の塩素系除菌剤を含有するCIP用添加剤は、次亜塩素酸カリウム、次亜塩素酸ナトリウム等の次亜塩素酸塩、亜塩素酸カリウム、亜塩素酸ナトリウム等の亜塩素酸塩、塩素酸カリウム、塩素酸ナトリウム等の塩素酸塩、過塩素酸カリウム、過塩素酸ナトリウム等の過塩素酸塩、ジクロロイソシアヌル酸ナトリウム、ジクロロイソシアヌル酸カリウム等のジクロロイソシアヌル酸塩等の塩素系除菌剤を含むものが挙げられる。CIP用添加剤は、これら塩素系除菌剤を1種又は2種以上含んでいても良い。塩素系除菌剤としては、次亜塩素酸アルカリ金属塩、次亜塩素酸アルカリ土類金属塩、ジクロロイソシアヌル酸塩が好ましく、これらを1種又は2種以上を組み合わせて用いることが好ましい。(C)成分のCIP用添加剤は、上記塩素系除菌剤のみからなるものであっても、塩素系除菌剤の水溶液であっても良い。また上記塩素系除菌剤や塩素系除菌剤の水溶液に、更に水酸化ナトリウム等のアルカリ、高分子ポリマー、ケイ酸塩等の1種以上を配合したCIP用添加剤も(C)成分として使用することができる。(C)成分のCIP用添加剤は粉体、液体、水で希釈した溶液のどの形態でも使用することができるが、取り扱いやすい点から液体や溶液が好ましい。溶液に使用される水としては、イオン交換水、蒸留水、純水、軟水、水道水等が挙げられるが、貯蔵安定性の点からイオン交換水、蒸留水、純水等が好ましい。   (C) Additives for CIP containing the chlorine-based disinfectant of the component include hypochlorites such as potassium hypochlorite and sodium hypochlorite, and hypochlorites such as potassium chlorite and sodium chlorite. Chlorates, potassium chlorates, chlorates such as sodium chlorate, potassium perchlorates, perchlorates such as sodium perchlorate, dichloroisocyanurates such as sodium dichloroisocyanurate, potassium dichloroisocyanurate, etc. Those containing a chlorine-based disinfectant may be mentioned. The additive for CIP may contain one or more of these chlorine-based disinfectants. As the chlorine-based disinfectant, alkali metal hypochlorite, alkaline earth metal hypochlorite, and dichloroisocyanurate are preferable, and it is preferable to use one or a combination of two or more thereof. The additive for CIP of the component (C) may be composed of only the chlorine-based disinfectant or may be an aqueous solution of the chlorine-based disinfectant. In addition, an additive for CIP in which at least one kind of an alkali such as sodium hydroxide, a polymer, or a silicate is further added to the aqueous solution of the chlorine-based disinfectant or the chlorine-based disinfectant is also used as the component (C). Can be used. The additive for CIP as the component (C) can be used in any form of powder, liquid, or solution diluted with water, but liquid or solution is preferred from the viewpoint of easy handling. Examples of the water used for the solution include ion-exchanged water, distilled water, pure water, soft water, and tap water. From the viewpoint of storage stability, ion-exchanged water, distilled water, pure water, and the like are preferable.

本発明のCIP洗浄方法は、上記(A)成分と(B)成分の質量比が、(A)/(B)=0.16〜190であるCIP用洗浄剤組成物を水で希釈した希釈洗浄液に対し、(C)成分として塩素系除菌剤を含有するCIP用添加剤を添加して調製した、有効塩素量0.005〜0.2質量%、(B)成分を0.001〜0.6質量%含有する10〜60℃のCIP除菌洗浄液により飲食料品製造ラインの洗浄を行う。CIP洗浄剤組成物を希釈するための水としては、水道水、地下水、工業用水、イオン交換水、蒸留水等が挙げられるが、経済性の点から水道水、地下水が好ましい。CIP用洗浄剤組成物の(A)成分と(B)成分の質量比(A)/(B)が0.16未満であると、有効塩素安定性が低下する場合があり、190を超えると無機物汚れや多糖類汚れの洗浄性が低下する場合がある。(A)成分と(B)成分の質量比は、(A)/(B)=1〜100であることが好ましく、5〜80であることがより好ましい。また、CIP除菌洗浄液は、有効塩素量が0.005〜0.2質量%含有するが、好ましくは0.01〜0.15質量%であり、より好ましくは0.02〜0.12質量%である。0.005質量%未満であると、除菌性が低下する場合があり、0.2質量%を超えると金属腐食防止性が低下する場合がある。CIP除菌洗浄液中の(B)成分の割合は、0.001〜0.6質量%含有するが、より好ましくは0.01〜0.55質量%であり、さらに好ましくは0.1〜0.5質量%である。(B)成分の割合が0.001質量%未満であると、CIP除菌洗浄液が有機物の洗浄性に劣るものとなり、0.6質量%を超えて使用すると有効塩素安定性が低下し、また、CIP除菌洗浄液の洗浄性としては飽和し、経済性に劣る。尚、CIP除菌洗浄液の有効塩素量は、CIP除菌洗浄液を調製した直後における量である。尚、有効塩素量はJIS K 0101の残留塩素−よう素滴定法に基づき、測定をおこなった。   In the CIP cleaning method of the present invention, the CIP cleaning composition having a mass ratio of the component (A) to the component (B) of (A) / (B) = 0.16 to 190 is diluted with water. The cleaning solution was prepared by adding a CIP additive containing a chlorine-based disinfectant as a component (C). The food / beverage product manufacturing line is washed with a CIP sterilization washing solution containing 10% by mass of 10 to 60 ° C. Examples of water for diluting the CIP cleaning composition include tap water, ground water, industrial water, ion-exchanged water, distilled water, and the like, and tap water and ground water are preferred from the viewpoint of economy. When the mass ratio (A) / (B) of the component (A) and the component (B) of the cleaning composition for CIP is less than 0.16, the effective chlorine stability may decrease. In some cases, the cleaning properties of inorganic soils and polysaccharide stains are reduced. The mass ratio of the component (A) to the component (B) is preferably (A) / (B) = 1 to 100, and more preferably 5 to 80. Further, the CIP disinfecting and washing solution contains 0.005 to 0.2% by mass of effective chlorine, preferably 0.01 to 0.15% by mass, and more preferably 0.02 to 0.12% by mass. %. If the amount is less than 0.005% by mass, the bactericidal property may decrease. If the amount exceeds 0.2% by mass, the metal corrosion inhibiting property may decrease. The proportion of the component (B) in the CIP sanitizing and washing solution is 0.001 to 0.6% by mass, more preferably 0.01 to 0.55% by mass, and even more preferably 0.1 to 0% by mass. 0.5% by mass. When the proportion of the component (B) is less than 0.001% by mass, the CIP sanitizing cleaning solution is inferior in the detergency of organic substances, and when it exceeds 0.6% by mass, the effective chlorine stability decreases, and However, the detergency of the CIP disinfecting cleaning solution is saturated, resulting in poor economy. Note that the effective chlorine amount of the CIP disinfecting washing solution is the amount immediately after preparing the CIP disinfecting washing solution. In addition, the effective chlorine amount was measured based on the residual chlorine-iodine titration method of JIS K0101.

本発明のCIP洗浄方法に用いるCIP除菌洗浄液は、(A)成分、(B)成分、(C)成分とともに更に(D)成分として高分子ポリマーを含んでいると、洗浄中のスケール付着抑制の効果がある。(D)成分は、(A)成分、(B)成分とともにCIP用洗浄剤組成物中に、(B)と(D)成分の質量比が、(D)/(B)=0.01〜10となるように配合することが好ましく、(D)/(B)=0.05〜2となるように配合することがより好ましい。   If the CIP disinfecting cleaning solution used in the CIP cleaning method of the present invention further contains a high molecular polymer as the component (D) in addition to the component (A), the component (B), and the component (C), scale adhesion during cleaning is suppressed. Has the effect. The component (D), together with the component (A) and the component (B), in the detergent composition for CIP, the mass ratio of the component (B) to the component (D) is (D) / (B) = 0.01 to It is preferable to mix it so that it may be set to 10, and it is more preferable to mix | blend so that it may become (D) / (B) = 0.05-2.

(D)成分の高分子ポリマーとしては、ポリアクリル酸、ポリメタクリル酸、ポリマレイン酸、ポリイタコン酸、アクリル酸−メタクリル酸共重合体、アクリル酸−マレイン酸共重合体、オレフィン−マレイン酸共重合体、アクリル酸−スルホン酸共重合体、無水マレイン酸−スチレン共重合体、無水マレイン酸−エチレン共重合体、無水マレイン酸−酢酸ビニル共重合体、無水マレイン酸−アクリル酸エステル共重合体等や、これらの塩が挙げられるが、ポリアクリル酸又はその塩、ポリマレイン酸又はその塩、アクリル酸−メタクリル酸共重合体、アクリル酸−マレイン酸共重合体、オレフィン−マレイン酸共重合体、アクリル酸−スルホン酸共重合体が好ましい。これらのポリカルボン酸型ポリマー又はその塩は、単独で用いても2種類以上組み合わせて用いても良い。アクリル酸型共重合体、マレイン酸型共重合体、メタクリル酸型共重合体等の共重合体としては、アミド結合を含まないものが好ましい。ポリアクリル酸の重量平均分子量は500〜20,000が好ましく、特に好ましくは1,500〜15,000である。   Examples of the high molecular weight polymer as the component (D) include polyacrylic acid, polymethacrylic acid, polymaleic acid, polyitaconic acid, acrylic acid-methacrylic acid copolymer, acrylic acid-maleic acid copolymer, and olefin-maleic acid copolymer. , Acrylic acid-sulfonic acid copolymer, maleic anhydride-styrene copolymer, maleic anhydride-ethylene copolymer, maleic anhydride-vinyl acetate copolymer, maleic anhydride-acrylic acid ester copolymer, etc. These salts include polyacrylic acid or a salt thereof, polymaleic acid or a salt thereof, acrylic acid-methacrylic acid copolymer, acrylic acid-maleic acid copolymer, olefin-maleic acid copolymer, acrylic acid -Sulfonic acid copolymers are preferred. These polycarboxylic acid type polymers or salts thereof may be used alone or in combination of two or more. As a copolymer such as an acrylic acid type copolymer, a maleic acid type copolymer, and a methacrylic acid type copolymer, those containing no amide bond are preferable. The weight average molecular weight of the polyacrylic acid is preferably from 500 to 20,000, particularly preferably from 1,500 to 15,000.

CIP用洗浄剤組成物を希釈する水としては微生物学的、化学的に清浄で健康に有害な菌や化合物を含まない水であれば問題はなく、通常は水道水、地下水、工業用水などが用いられる。希釈に使用する水の清浄化処理方法としては、エアレーション、逆浸透膜ろ過、限外ろ過、珪藻土ろ過、イオン交換、蒸留等が挙げられ、これらは1種又は2種以上組み合わせて清浄化処理が行われる。洗浄液はその都度調製することが好ましいが、一度洗浄に使用した洗浄液やすすぎ水であっても、汚れの混入が少なければ回収して保存しておき、使用時に再度(A)〜(D)成分の1種または2種以上を添加してリユース洗浄ができる。CIP用洗浄剤組成物の希釈のための水は、10〜60℃に冷却または加温して用いることができる。本発明のCIP洗浄方法は、CIP除菌洗浄液を温度10〜60℃で使用するが、13〜40℃で使用することが好ましく、15〜30℃で使用することがより好ましい。   As the water for diluting the detergent composition for CIP, there is no problem as long as the water is microbiologically and chemically clean and does not contain any harmful bacteria or compounds. Usually, tap water, groundwater, industrial water and the like are used. Used. Examples of the method of cleaning water used for dilution include aeration, reverse osmosis membrane filtration, ultrafiltration, diatomaceous earth filtration, ion exchange, and distillation. These may be used alone or in combination of two or more. Done. It is preferable to prepare the washing solution each time, but even if the washing solution or the rinsing water used once for washing is collected with little contamination, it is stored and stored again, and the components (A) to (D) are re-used at the time of use. Reuse cleaning can be performed by adding one or more of the above. The water for diluting the cleaning composition for CIP can be used after cooling or heating to 10 to 60 ° C. In the CIP cleaning method of the present invention, the CIP sanitizing cleaning solution is used at a temperature of 10 to 60 ° C, preferably at 13 to 40 ° C, more preferably at 15 to 30 ° C.

本発明方法において、CIP除菌洗浄液には、更に必要に応じて(B)成分以外のキレート剤、界面活性剤、有機塩類、分散剤、可溶化剤、染料、防腐剤、(C)成分以外の除菌剤、消泡剤、腐食抑制剤、天然抽出物等を本発明の効果を損なわない範囲で配合することができる。   In the method of the present invention, the CIP disinfecting washing solution may further contain, if necessary, a chelating agent other than the component (B), a surfactant, an organic salt, a dispersant, a solubilizer, a dye, a preservative, and a component other than the component (C). , A disinfectant, a defoamer, a corrosion inhibitor, a natural extract and the like can be blended within a range that does not impair the effects of the present invention.

本発明のCIP洗浄方法では、飲食品製造ライン内の、タンク内においては噴射ノズルやローラーボール、シャワーボール等から回転を伴う動きによって洗浄液が噴射され、満遍なく洗浄液が内部と接触するように洗浄を行う。また、配管内においては、流速にして0.5〜4.0m/secにて、好ましくは1.0〜3.0m/secの高速の流れによって洗浄を行う。   In the CIP cleaning method of the present invention, the cleaning liquid is sprayed by a rotating motion from a spray nozzle, a roller ball, a shower ball, or the like in the tank in the food and beverage production line, and the cleaning is performed so that the cleaning liquid uniformly contacts the inside. Do. In the piping, the cleaning is performed at a flow rate of 0.5 to 4.0 m / sec, preferably at a high speed of 1.0 to 3.0 m / sec.

従来のCIP洗浄においては、1.水洗浄、2.アルカリ洗浄、3.水すすぎ、4.酸洗浄、5.水すすぎ、6.除菌、7.水すすぎ、という工程を、CIP洗浄液の配合成分、汚れの種類や状態に応じて、一部の工程が省略されたり、順序が変更されたり、あるいは同じ工程が繰り返し実施されるものであったが、本発明方法では、1.水洗浄、2.CIP洗浄液による洗浄、3.水すすぎ、の三工程で従来のCIP洗浄における上記1〜7の工程を行ったと同等の効果を得ることができる。従来のCIP洗浄におけるそれぞれの工程は、5分から60分で実施され、本発明のCIP洗浄方法においても、それぞれの工程を5分から60分で行うことができるが、10分から40分で行うことが好ましい。   In the conventional CIP cleaning, 1. water washing; 2. alkali washing; 3. water rinse; 4. acid washing; 5. water rinse, 6. eradication; In the process of rinsing with water, some processes are omitted, the order is changed, or the same process is repeatedly performed, depending on the components of the CIP cleaning solution, the type and condition of dirt. In the method of the present invention, 1. water washing; 2. cleaning with a CIP cleaning solution; In the three steps of water rinsing, the same effect as in the above steps 1 to 7 in the conventional CIP cleaning can be obtained. Each step in the conventional CIP cleaning is performed in 5 to 60 minutes, and in the CIP cleaning method of the present invention, each step can be performed in 5 to 60 minutes, but can be performed in 10 to 40 minutes. preferable.

従来のCIP洗浄における温度は、1.水洗浄、2.アルカリ洗浄、3.水すすぎ、4.酸洗浄、5.水すすぎ、6.除菌、7.水すすぎの工程のうち、1.水洗浄、7.水すすぎ工程においては、使用する水を加温せずに10℃〜60℃で使用される場合があるが、2.アルカリ洗浄、3.水すすぎ、4.酸洗浄、5.水すすぎ、6.除菌工程においては加温し60℃〜140℃で使用される場合が多く、熱エネルギーを必要とされるため効率が悪かった。本発明方法においては、1.水洗浄、2.CIP洗浄液による洗浄、3.水すすぎ、の各工程を通して10〜60℃にて行うことが出来るが、2.CIP洗浄液による洗浄の工程は、CIP除菌洗浄液温度13〜40℃にて行うことが好ましく、CIP除菌洗浄液温度15〜30℃にて行うことがより好ましい。CIP除菌洗浄液温度が10℃未満では、有機物の洗浄性が劣り、60℃を超えると(C)成分の添加後に塩素の安定性が悪くなる。本発明の方法では希釈する水が10〜60℃であれば、加温に必要な熱エネルギーを削減することができる。   The temperature in the conventional CIP cleaning is as follows. 1. water washing; 2. alkali washing; 3. water rinse; 4. acid washing; 5. water rinse, 6. eradication; Among the water rinsing steps, 6. water washing; In the water rinsing step, the water to be used may be used at a temperature of 10 ° C to 60 ° C without heating. 2. alkali washing; 3. water rinse; 4. acid washing; 5. water rinse, In the disinfection process, heating is often performed at 60 ° C. to 140 ° C., and thermal energy is required, resulting in poor efficiency. In the method of the present invention, 1. water washing; 2. cleaning with a CIP cleaning solution; Water rinsing can be carried out at 10 to 60 ° C. through each step. The step of cleaning with the CIP cleaning liquid is preferably performed at a CIP sterilization cleaning liquid temperature of 13 to 40 ° C, and more preferably at a CIP sterilization cleaning liquid temperature of 15 to 30 ° C. When the temperature of the CIP disinfecting cleaning solution is lower than 10 ° C., the cleaning properties of organic substances are inferior. When the temperature exceeds 60 ° C., the stability of chlorine is deteriorated after the addition of the component (C). In the method of the present invention, if the water to be diluted is 10 to 60 ° C., the heat energy required for heating can be reduced.

以下、本発明を実施例と比較例により具体的に説明するが、本発明はこれらにより限定されるものではない。実施例、比較例において配合に用いた各成分を下記に示す。尚、表中における実施例および比較例の配合の数値は純分の質量%を表す。   Hereinafter, the present invention will be described specifically with reference to Examples and Comparative Examples, but the present invention is not limited thereto. The components used in the Examples and Comparative Examples are shown below. In addition, the numerical value of the combination of the example and the comparative example in the table represents mass% of the pure content.

(A)成分
A−1:水酸化ナトリウム
A−2:水酸化カリウム
(A) Component A-1: sodium hydroxide A-2: potassium hydroxide

(B)成分
B−1:メチルグリシン二酢酸三ナトリウム(商品名:トリロンM パウダー、BASFジャパン社製、有効成分量 98%)
(B′)成分:B成分の比較成分
B′−1:エチレンジアミン四酢酸四ナトリウム(商品名:ディゾルビンNA、アクゾノーベル社製)
B′−2:グルタミン酸二酢酸三ナトリウム(商品名:GLDA、アクゾノーベル社製)
B′−3:ニトリロ三酢酸三ナトリウム(商品名:トリロンA92R、BASFジャパン社製)
B′−4:トリポリ燐酸ナトリウム(商品名:トリポリ燐酸ソーダ、下関三井化学社製)
(B) Component B-1: trisodium methylglycine diacetate (trade name: Trilon M powder, manufactured by BASF Japan, 98% active ingredient)
Component (B '): Comparative component of component B B-1: tetrasodium ethylenediaminetetraacetate (trade name: Disorbin NA, manufactured by Akzo Nobel)
B'-2: Trisodium glutamate diacetate (trade name: GLDA, manufactured by Akzo Nobel)
B'-3: Trisodium nitrilotriacetate (trade name: Trilon A92R, manufactured by BASF Japan)
B'-4: sodium tripolyphosphate (trade name: sodium tripolyphosphate, manufactured by Shimonoseki Mitsui Chemicals, Inc.)

(C)成分
C−1:次亜塩素酸ナトリウム(商品名:次亜塩素酸ソーダ、旭硝子社製、有効塩素量12%)
C−2:ジクロロイソシアヌル酸ナトリウム(商品名:ハイライト60G、日産化学工業社製、有効塩素量60%)
C−3:次亜塩素酸ナトリウム7.8%、水酸化ナトリウム2%、ポリアクリル酸ナトリウム(重量平均分子量4,000)1.5%、ケイ酸ナトリウム(NaO・3SiO)3.5%の水溶液
(C) Component C-1: sodium hypochlorite (trade name: sodium hypochlorite, manufactured by Asahi Glass Co., available chlorine amount: 12%)
C-2: sodium dichloroisocyanurate (trade name: Highlight 60G, manufactured by Nissan Chemical Industries, available chlorine 60%)
C-3: 7.8% sodium hypochlorite, 2% sodium hydroxide, 1.5% sodium polyacrylate (weight average molecular weight 4,000) 1.5%, sodium silicate (Na 2 O · 3SiO 2 ) 5% aqueous solution

(D)成分
D−1:ポリアクリル酸ナトリウム(商品名:ソカランPA30CL グラニュール、BASFジャパン社製、有効成分量 45%、平均分子量8,000)
D−2:アクリル酸マレイン酸共重合体ナトリウム(商品名:アキュゾール505N グラニュール、ロームアンドハース社製、有効成分量 35%、平均分子量40,000)
(D) Component D-1: sodium polyacrylate (trade name: Sokalan PA30CL Granule, manufactured by BASF Japan, active ingredient amount 45%, average molecular weight 8,000)
D-2: Sodium acrylic acid / maleic acid copolymer (trade name: Acusol 505N Granule, manufactured by Rohm and Haas Co., Ltd., active ingredient content 35%, average molecular weight 40,000)

実施例1〜35、比較例1〜14
表1〜6に示す(A)成分と(B)成分とを含むCIP用洗浄剤組成物の水溶液を、炭酸カルシウム換算で75mg/L[ドイツ硬度4.2°DH]の人工硬水で、表に示す希釈倍率となるように希釈したCIP希釈洗浄液に、表に示す(C)成分(CIP用添加剤)を添加してCIP除菌洗浄液を調製した。CIP用洗浄剤組成物の(A)成分と(B)成分の質量比を表1〜6に示す。このCIP除菌洗浄液を用い、洗浄性試験並びに塩素安定性試験、除菌性試験を行ない評価した。結果を表1〜6に示す。尚、表中の各成分の割合は質量%であり、(C)成分の添加量は、CIP用洗浄剤組成物を希釈した希釈洗浄液100g当たりに対する量(g)で、括弧内の値は、塩素系除菌剤としての有効塩素量(質量%)を示した。
Examples 1 to 35, Comparative Examples 1 to 14
An aqueous solution of the cleaning composition for CIP containing the components (A) and (B) shown in Tables 1 to 6 was prepared using artificial hard water having a concentration of 75 mg / L [German hardness 4.2 ° DH] in terms of calcium carbonate. The components (C) (additives for CIP) shown in the table were added to the CIP diluted washing solution diluted so as to have the dilution ratio shown in Table 1 to prepare a CIP sanitizing washing solution. Tables 1 to 6 show the mass ratio of the component (A) to the component (B) of the cleaning composition for CIP. Using this CIP disinfecting cleaning solution, a detergency test, a chlorine stability test and a disinfecting test were performed and evaluated. The results are shown in Tables 1 to 6. The ratio of each component in the table is% by mass, and the addition amount of the component (C) is an amount (g) per 100 g of the diluted cleaning solution obtained by diluting the cleaning composition for CIP. The effective chlorine content (% by mass) as a chlorine-based disinfectant was shown.

※1:有機物汚れ洗浄性試験
試験方法:
ステンレス片(6cm×7cmの長方形、厚さ1mmのSUS316片)の質量を測定し、これに有機物汚れとしてコーラ濃縮物を乾燥重量が50mgとなるように塗布し、110℃で30分加熱して汚れを付着させたものを試験片として質量を測定した。この試験片をCIP除菌洗浄液300mLに浸漬し、表に示す温度で20分間放置した後、イオン交換水ですすぎ、105℃で30分間乾燥した後、質量を測定した。洗浄前の試験片と、汚れ付着前のステンレス片との質量差を汚れ付着量とし、洗浄前後の試験片の質量変化から下記式により洗浄率を算出し、以下の基準で洗浄性を評価した。
洗浄率(%)={(洗浄前試験片重量−洗浄後試験片重量)/(汚れ付着量)}×100
有機物汚れ洗浄性評価基準:
○:洗浄率80%以上(洗浄性に優れる)
△:洗浄率70%以上、80%未満(洗浄性良好)
×:洗浄率70%未満(洗浄性が悪い)
とし、評価基準が△、○を実用性のあるものと判定した。
* 1: Organic stain cleaning test method:
The mass of a stainless steel piece (6 cm × 7 cm rectangle, SUS316 piece with a thickness of 1 mm) was measured, and a cola concentrate as an organic stain was applied so as to have a dry weight of 50 mg, and heated at 110 ° C. for 30 minutes. The mass to which the stain was attached was measured as a test piece. The test piece was immersed in 300 mL of the CIP sanitizing and washing solution, allowed to stand at the temperature shown in the table for 20 minutes, rinsed with ion-exchanged water, dried at 105 ° C. for 30 minutes, and weighed. The test piece before washing, and the difference in mass between the stainless steel piece before the stain adhered and the amount of stain, the washing rate was calculated from the change in the mass of the test piece before and after washing by the following formula, and the cleanability was evaluated based on the following criteria. .
Washing rate (%) = {(test specimen weight before washing−test specimen weight after washing) / (dirt adhesion amount)} × 100
Evaluation criteria for cleaning of organic stains:
:: 80% or more of cleaning rate (excellent in cleaning)
△: 70% or more and less than 80% of cleaning rate (good cleaning property)
×: less than 70% of cleaning rate (poor cleaning)
The evaluation criteria of Δ and ○ were judged to be practical.

※2:無機物汚れ洗浄性試験
試験方法:
ステンレス片(6cm×7cmの長方形、厚さ1mmのSUS316ステンレス片)の質量を測定し、これに無機物汚れとして炭酸カルシウムを乾燥重量が50mgとなるように塗布し、110℃で30分加熱して汚れを付着させたものを試験片として質量を測定した。この試験片をCIP除菌洗浄液300mLに浸漬し、表に示す温度で20分間放置した後、イオン交換水ですすぎ、105℃で30分間乾燥した後、試験片の質量を測定した。洗浄前の試験片と、汚れ付着前のステンレス片との質量差を汚れ付着量とし、洗浄前後の試験片の質量変化から以下の式により洗浄率を算出し、以下の基準で洗浄性を評価した。
洗浄率(%)={(洗浄前試験片重量−洗浄後試験片重量)/(汚れ付着量)}×100
無機物汚れ洗浄性評価基準:
○:洗浄率80%以上(洗浄性に優れる)
△:洗浄率70%以上、80%未満(洗浄性良好)
×:洗浄率70%未満(洗浄性が悪い)
とし、評価基準が△、○を実用性のあるものと判定した。
* 2: Inorganic soil cleaning test method:
The mass of a stainless steel piece (a SUS316 stainless steel piece having a rectangular shape of 6 cm × 7 cm and a thickness of 1 mm) was measured, and calcium carbonate was applied thereto as an inorganic soil so as to have a dry weight of 50 mg, and heated at 110 ° C. for 30 minutes. The mass to which the stain was attached was measured as a test piece. The test piece was immersed in 300 mL of the CIP sanitizing and washing solution, left at the temperature shown in the table for 20 minutes, rinsed with ion-exchanged water, dried at 105 ° C. for 30 minutes, and the mass of the test piece was measured. The difference in mass between the test piece before washing and the stainless steel piece before soiling is regarded as the amount of soiling, and the washing rate is calculated from the change in the mass of the test piece before and after washing according to the following formula, and the cleaning performance is evaluated based on the following criteria. did.
Washing rate (%) = {(test specimen weight before washing−test specimen weight after washing) / (dirt adhesion amount)} × 100
Evaluation criteria for inorganic soil cleaning:
:: 80% or more of cleaning rate (excellent in cleaning)
△: 70% or more and less than 80% of cleaning rate (good cleaning property)
×: less than 70% of cleaning rate (poor cleaning)
The evaluation criteria of Δ and ○ were judged to be practical.

※3:多糖類汚れ洗浄性試験
試験方法:
モルト84g、ホップ1.0g、グラニュー糖35g、ドライイースト0.1g、蒸留水900gを混合し、醗酵液とした。上記醗酵液にステンレス片(6cm×7cmの長方形、厚さ1mmのSUS316ステンレス片)を25℃で48時間半浸漬し醗酵させ、多糖類汚れをステンレス片に付着させた後、105℃で30分乾燥したものを試験片とした。この試験片をCIP除菌洗浄液300mLに浸漬し、表に示す温度で20分間放置した後、イオン交換水ですすぎ、105℃で30分間乾燥した後、質量を測定した。洗浄前の試験片と、汚れ付着前のステンレス片との質量差を汚れ付着量とし、洗浄前後の試験片の質量変化から以下の式により洗浄率を算出し、以下の基準で洗浄性を評価した。
洗浄率(%)={(洗浄前試験片重量−洗浄後試験片重量)/(汚れ付着量)}×100
多糖類汚れ洗浄性評価基準:
○:洗浄率80%以上(洗浄性に優れる)
△:洗浄率70%以上、80%未満(洗浄性良好)
×:洗浄率70%未満(洗浄性が悪い)
とし、評価基準が△、○を実用性のあるものと判定した。
* 3: Polysaccharide stain cleaning test method:
A fermentation solution was prepared by mixing 84 g of malt, 1.0 g of hops, 35 g of granulated sugar, 0.1 g of dry yeast, and 900 g of distilled water. A piece of stainless steel (a SUS316 stainless steel piece having a rectangular shape of 6 cm × 7 cm and a thickness of 1 mm) was immersed in the above fermentation solution for 48 and a half hours at 25 ° C. for fermentation. The dried one was used as a test piece. The test piece was immersed in 300 mL of the CIP sterilization cleaning solution, left at the temperature shown in the table for 20 minutes, rinsed with ion-exchanged water, dried at 105 ° C. for 30 minutes, and then weighed. The mass difference between the test piece before washing and the stainless steel piece before soiling is defined as the amount of soiling, and the washing rate is calculated from the mass change of the test piece before and after washing according to the following formula, and the cleaning performance is evaluated based on the following criteria. did.
Washing rate (%) = {(test specimen weight before washing−test specimen weight after washing) / (dirt amount)} × 100
Evaluation criteria for polysaccharide stain cleanability:
:: 80% or more of cleaning rate (excellent in cleaning)
Δ: 70% or more and less than 80% of cleaning rate (good cleaning property)
×: less than 70% of cleaning rate (poor cleaning performance)
The evaluation criteria of Δ and ○ were judged to be practical.

※4:有効塩素安定性試験
試験方法:
CIP除菌洗浄液200mLを表に示す洗浄温度で30分経過後、有効塩素残存率を以下の基準で評価した。尚、有効塩素残存率はJIS K 0101の残留塩素−よう素滴定法に基づき、以下に示す式により求めた。
有効塩素残存率(%)=(加温後の洗浄液中の有効塩素濃度)/(加温前の洗浄液中の有効塩素濃度)×100
有効塩素安定性の評価:
○:有効塩素残存率が70%以上
△:有効塩素残存率が50%以上、70%未満
×:有効塩素残存率が50%未満
−:測定不能
とし、△、○を実用性のあるものとして判定した。
* 4: Effective chlorine stability test Test method:
After a lapse of 30 minutes using 200 mL of the CIP sanitizing washing solution at the washing temperature shown in the table, the effective chlorine remaining rate was evaluated according to the following criteria. The effective chlorine residual ratio was determined by the following equation based on the residual chlorine-iodine titration method of JIS K0101.
Effective chlorine remaining rate (%) = (effective chlorine concentration in cleaning solution after heating) / (effective chlorine concentration in cleaning solution before heating) × 100
Evaluation of available chlorine stability:
:: Effective chlorine remaining rate is 70% or more △: Effective chlorine remaining rate is 50% or more and less than 70% ×: Effective chlorine remaining rate is less than 50%-: Measurement is impossible, and △ and ○ are regarded as practical. Judged.

※5:一般細菌に対する除菌性試験
供試菌株(一般細菌):
財団法人発酵研究所の黄色ブドウ球菌:Staphylococcus aureus NBRC13276(10CFU/mLレベル)、緑膿菌:Pseudomonas aeruginosa NBRC13736(10CFU/mLレベル)を用いた。
試験方法:
CIP除菌洗浄液10mLに、供試菌株をSCDブイヨン培地で培養した菌液0.1mLを添加し、表に示す洗浄温度で15分間接触させたものを試験液とした。この試験液1mLを、チオ硫酸ナトリウム0.1質量%含有したSCD寒天培地にて混釈培養後、37℃で24時間培養した。培養終了後、生菌数を測定し、下記基準で評価を行った。
評価基準:
○:供試菌のlog reductionが3以上の菌数減少
△:供試菌のlog reductionが2以上、3未満の菌数減少
×:供試菌のlog reductionが2未満の菌数減少
とし、△、○を実用性のあるものとして判定した。
* 5: Escherichia coli test strain for general bacteria (General bacteria):
Institute for Fermentation of Staphylococcus aureus: Staphylococcus aureus NBRC13276 (10 8 CFU / mL level), Pseudomonas aeruginosa were used: Pseudomonas aeruginosa NBRC13736 (10 8 CFU / mL level).
Test method:
A test solution was prepared by adding 0.1 mL of a bacterial solution obtained by culturing the test strain in an SCD broth medium to 10 mL of the CIP disinfecting and washing solution and contacting the solution for 15 minutes at the washing temperature shown in the table. 1 mL of this test solution was pour-cultured on an SCD agar medium containing 0.1% by mass of sodium thiosulfate, and then cultured at 37 ° C. for 24 hours. After completion of the culture, the number of viable bacteria was measured and evaluated according to the following criteria.
Evaluation criteria:
:: Log reduction of the test bacteria is 3 or more. Δ: Log reduction of the test bacteria is 2 or more and less than 3. ×: Log reduction of the test bacteria is 2 or less. Δ and ○ were judged to be practical.

※6:芽胞菌に対する除菌性試験
(a)供試菌株(芽胞菌):
芽胞菌として、バチルスサブチリス(Bacillus subtilis)(NBRC3134)を用いた。
(b)芽胞懸濁液の作製:
供試菌株をSCD寒天培地(日水製薬品)に塗抹し、30℃で培養し、培養後、顕微鏡観察にて芽胞が十分に形成されていることを確認した。平板培地上に滅菌済み純水を10mL入れ、コロニーを掻き取り懸濁液を収集した。収集した懸濁液に、10000rpmで、4℃、15分間の条件で遠心洗浄を3回実施し、遠心後、滅菌済み純水を適量加え、2.0〜9.0×10CFU/mL程度になるように菌数を調製し、ウォーターバスにて80℃、15分間の加熱処理をして芽胞懸濁液とした。
(c)試験方法:
CIP除菌洗浄液10mLに、終濃度1.5〜5.0×10(CFU/mL)となるように芽胞懸濁液0.1mLを添加し、表に示す洗浄温度で15分間接触させたものを試験液とした。この試験液1mLを、チオ硫酸ナトリウム0.1質量%含有したSCD寒天培地にて混和固化し、30℃で2日間培養した。培養後、生菌数を測定し、初発菌数との差より、以下の基準で評価した。
評価基準:
○:供試菌のlog reductionが3以上の菌数減少
△:供試菌のlog reductionが2以上、3未満の菌数減少
×:供試菌のlog reductionが2未満の菌数減少
とし、△、○を実用性のあるものとして判定した。
* 6: Eradication test for spores (a) Test strain (Spores):
Bacillus subtilis (NBRC3134) was used as the spore bacterium.
(B) Preparation of spore suspension:
The test strain was spread on an SCD agar medium (Nissui Pharmaceutical), cultured at 30 ° C., and after culturing, it was confirmed by microscopic observation that spores had been sufficiently formed. 10 mL of sterilized pure water was put on the plate medium, the colonies were scraped, and the suspension was collected. The collected suspension was subjected to centrifugal washing three times at 10,000 rpm and 4 ° C. for 15 minutes, and after centrifugation, an appropriate amount of sterilized pure water was added, and 2.0 to 9.0 × 10 8 CFU / mL. The number of bacteria was adjusted to about the same, and heat treatment was performed at 80 ° C. for 15 minutes in a water bath to obtain a spore suspension.
(C) Test method:
0.1 mL of the spore suspension was added to 10 mL of the CIP disinfecting washing solution to a final concentration of 1.5 to 5.0 × 10 5 (CFU / mL), and contacted at the washing temperature shown in the table for 15 minutes. These were used as test liquids. 1 mL of this test solution was mixed and solidified in an SCD agar medium containing 0.1% by mass of sodium thiosulfate, and cultured at 30 ° C. for 2 days. After the cultivation, the number of viable bacteria was measured and evaluated based on the following criteria based on the difference from the initial number of bacteria.
Evaluation criteria:
:: A decrease in the number of bacteria with a log reduction of the test bacterium of 3 or more Δ: A decrease in the number of bacteria with a log reduction of the bacterium of 2 or more and less than 3 ×: A decrease in the number of germs with a log reduction of the test bacterium of less than 2 Δ and ○ were judged to be practical.

※7:スケール付着抑制性試験:
200mL容のガラス瓶に、CIP除菌洗浄液100mLを入れ、リン酸カルシウム0.4gを添加して20分間攪拌した。80℃の恒温下で24時間放置し、蒸留水でガラス瓶をすすぎ乾燥後、ガラス瓶のスケール付着の有無を目視にて判断し、以下の基準で評価した。
スケール抑制性の評価基準:
〇:スケール付着なし
△:僅かにスケールが付着しているが、使用上問題ないレベル
×:スケールが付着している
とし、△、○を実用性のあるものとして判定した。
* 7: Scale adhesion inhibition test:
In a 200 mL glass bottle, 100 mL of the CIP sterilization and washing solution was added, and 0.4 g of calcium phosphate was added, followed by stirring for 20 minutes. The glass bottle was left standing at a constant temperature of 80 ° C. for 24 hours, rinsed with distilled water and dried, and then the presence or absence of scale adhesion of the glass bottle was visually determined, and evaluated according to the following criteria.
Evaluation criteria for scale inhibition:
Δ: No scale adhered Δ: Level slightly adhered, but no problem in use ×: Scale adhered, and Δ and ○ were judged to be practical.

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Claims (4)

(A)成分としてアルカリ金属水酸化物、(B)成分としてメチルグリシン二酢酸又はその塩を含有し、(A)成分と(B)成分の質量比が、(A)/(B)=0.16〜190であるCIP用洗浄剤組成物を水で希釈した希釈洗浄液に対して、(C)成分として塩素系除菌剤を含有するCIP用添加剤を添加して調製した、有効塩素量0.005〜0.2質量%、(B)成分を0.001〜0.6質量%含有する10〜60℃のCIP除菌洗浄液により飲食料品製造ラインのCIP洗浄及び除菌洗浄を同時に行うことを特徴とするCIP洗浄方法。 (A) an alkali metal hydroxide compound as component (B) contains a methyl glycine diacetic acid or a salt thereof as an ingredient, the mass ratio of the component (A) and component (B), (A) / (B) = 0 The effective chlorine amount prepared by adding a CIP additive containing a chlorine-based disinfectant as a component (C) to a diluted washing solution obtained by diluting a CIP detergent composition having a pH of 16 to 190 with water. Simultaneous CIP washing and disinfection washing of a food and beverage production line with a CIP disinfection washing solution containing 10 to 60 ° C containing 0.005 to 0.2% by mass and 0.001 to 0.6% by mass of the component (B). A CIP cleaning method characterized by performing. (A)成分が水酸化ナトリウム、水酸化カリウムより選ばれた少なくとも一種以上を含有することを特徴とする請求項1に記載のCIP洗浄方法。   The CIP cleaning method according to claim 1, wherein the component (A) contains at least one selected from sodium hydroxide and potassium hydroxide. (C)成分は、塩素系除菌剤として次亜塩素酸アルカリ金属塩及び/又は次亜塩素酸アルカリ土類金属塩、塩素化イソシアヌル酸塩から選ばれた少なくとも一種以上を含有することを特徴とする請求項1又は2に記載のCIP洗浄方法。   The component (C) contains at least one selected from the group consisting of alkali metal hypochlorites and / or alkaline earth metal hypochlorites and chlorinated isocyanurates as chlorine-based disinfectants. The CIP cleaning method according to claim 1 or 2, wherein さらに、(A)成分、(B)成分を含む前記CIP用洗浄剤組成物に、(D)成分として高分子ポリマーを、(B)成分と(D)成分の質量比が、(D)/(B)=0.05〜10になるように含有する請求項1〜3のいずれかに記載のCIP洗浄方法。 Further, the cleaning composition for CIP containing the components (A) and (B) is added with a high molecular polymer as the component (D), and the mass ratio of the components (B) and (D) is (D) / The CIP cleaning method according to any one of claims 1 to 3, wherein (C) is contained such that (B) = 0.05 to 10.
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