JPH0822307B2 - Method for cleaning and sterilizing equipment used for desalting sugar-tight liquid - Google Patents

Method for cleaning and sterilizing equipment used for desalting sugar-tight liquid

Info

Publication number
JPH0822307B2
JPH0822307B2 JP61263941A JP26394186A JPH0822307B2 JP H0822307 B2 JPH0822307 B2 JP H0822307B2 JP 61263941 A JP61263941 A JP 61263941A JP 26394186 A JP26394186 A JP 26394186A JP H0822307 B2 JPH0822307 B2 JP H0822307B2
Authority
JP
Japan
Prior art keywords
hydrochloric acid
cleaning
desalting
molasses
temperature
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP61263941A
Other languages
Japanese (ja)
Other versions
JPS63186655A (en
Inventor
利勝 浜野
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsui Sugar Co Ltd
AGC Inc
Original Assignee
Asahi Glass Co Ltd
Mitsui Sugar Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Asahi Glass Co Ltd, Mitsui Sugar Co Ltd filed Critical Asahi Glass Co Ltd
Priority to JP61263941A priority Critical patent/JPH0822307B2/en
Publication of JPS63186655A publication Critical patent/JPS63186655A/en
Publication of JPH0822307B2 publication Critical patent/JPH0822307B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は糖蜜液の脱塩に用いる機器の洗浄、殺菌方
法、特にイオン交換膜のような隔膜を用いた糖蜜液の脱
塩装置の洗浄、殺菌方法に係わる。
DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention relates to a method for cleaning and sterilizing equipment used for desalting molasses liquid, and particularly for cleaning a molasses liquid desalting device using a diaphragm such as an ion exchange membrane. , Sterilization method.

[従来の技術] 従来より、糖蜜の濾過、脱塩装置は、微生物の増殖作
用によって生産される水不溶性粘着物質等により装置の
汚染や目詰まりによる液流れの不良等が発生し、これを
有機物系の殺菌剤を用いたり、或は加熱等によって殺菌
することや、又は電気透析槽を解体し多数のイオン交換
膜や室枠を人手により1枚ずつスポンジ状器具等によっ
て洗浄し、再度組立てる方法が行われている。
[Prior Art] Conventionally, molasses filtration and desalination devices have been contaminated or clogged due to water-insoluble adhesive substances produced by the growth action of microorganisms, resulting in poor liquid flow. Method of sterilizing by using a system sterilizer, heating, etc., or disassembling the electrodialysis tank and manually washing a large number of ion exchange membranes and chamber frames one by one with a sponge-like instrument, and then reassembling Is being done.

[発明の解決しようとする問題点] しかし、濾過器や、特にイオン交換樹脂或はイオン交
換膜等の隔膜を用いた脱塩装置に対しては、耐熱性等の
点から十分な加熱殺菌を行うことは不可能である。ま
た、有機物系の殺菌剤を用いることも考えられるが、食
品として糖蜜を扱う場合には、使用が禁止されているも
のが多い(例えばホルマリン等)。また、たまたま使用
が許可されていても、イオン交換樹脂やイオン交換膜に
対し、非可逆的な吸着を起こすため、使用が不可能であ
る等の欠点を有していた。また、人手による電気透析槽
の解体、洗浄はイオン交換膜の損傷や多大の時間、労力
を要すると共に主工程を停止することになり、糖分の損
失を招くことになる。
[Problems to be Solved by the Invention] However, sufficient heat sterilization is required from the viewpoint of heat resistance, etc., for a desalting device using a filter or a diaphragm such as an ion exchange resin or an ion exchange membrane. It is impossible to do. Although it is possible to use an organic fungicide, it is often prohibited to use molasses as food (eg, formalin). Further, even if it happens to be permitted to be used, it has a drawback that it cannot be used because it causes irreversible adsorption to an ion exchange resin or an ion exchange membrane. Further, manually dismantling and cleaning the electrodialysis tank requires damage to the ion exchange membrane, requires a large amount of time and labor, and stops the main process, resulting in sugar loss.

[問題点を解決するための手段] 本発明者はこれら従来法の欠点を排除し、特に隔膜を
用いた糖蜜の脱塩装置に対し、好適に作用する洗浄、殺
菌手段を見出すことを目的として種々研究、検討した結
果、食品関係に使用可能な無機薬品を選び、しかもこれ
を特定条件下に用いることにより前記目的を達成し得る
ことを見出した。かくして本発明は、糖蜜液の脱塩に用
いる機器を温度40℃以上の塩酸と接触せしめることを特
徴とする糖蜜液の脱塩に用いる機器の洗浄、殺菌方法で
ある。
[Means for Solving Problems] The present inventors have aimed to eliminate the drawbacks of these conventional methods and to find a washing and sterilizing means that works suitably for a molasses desalting apparatus using a diaphragm. As a result of various studies and studies, it was found that the above-mentioned object can be achieved by selecting an inorganic drug that can be used in foods and using it under specific conditions. Thus, the present invention is a method for cleaning and sterilizing a device used for desalting molasses liquid, characterized in that the device used for desalting molasses liquid is contacted with hydrochloric acid at a temperature of 40 ° C or higher.

本発明において用いられる塩酸は特に食品添加用のも
のが好ましく、塩酸の濃度は15〜30%程度を採用するの
が適当である。温度が前記範囲に満たない場合には殺菌
力が弱く、逆に前記範囲を超える場合には、塩酸の蒸発
が著しく、作業上危険であると共に、それ以上の効果を
期待し得ないのでいずれも好ましくない。
The hydrochloric acid used in the present invention is particularly preferably used for food additives, and the concentration of hydrochloric acid is suitably about 15 to 30%. If the temperature is lower than the above range, the bactericidal power is weak. On the contrary, if the temperature is higher than the above range, hydrochloric acid is significantly evaporated, which is dangerous in operation, and further effects cannot be expected. Not preferable.

また、使用温度は40℃以上であることが必要である。
温度がこれより低いと殺菌力が実質的にない。そして温
度の上限としては殺菌効果及び作業上の安全性を考慮す
ると80℃程度が適当である。これらの温度範囲の内55〜
65℃を採用する場合には実質的に完全な殺菌作用を有す
ると共に、装置に付着した菌類の洗浄をも行い得るし、
また作業上の安全性も高いので特に好ましい。本発明方
法が適用される糖蜜の脱塩に用いる機器として、糖蜜の
濾過器、脱塩装置本体はじめその前後の処理装置や付属
機器類を含むものである。具体的な洗浄、殺菌手段とし
ては、用いられる塩酸中にこれら機器を浸漬せしめてお
く方法や、この塩酸や機器に振動等を与え、塩酸と機器
の接触を十分ならしめる手段や、或は塩酸をこれら機器
類に流し通す等適宜な手段を採用し得る。
In addition, the operating temperature must be 40 ° C or higher.
At temperatures below this, there is virtually no germicidal activity. Considering the sterilization effect and work safety, the upper limit of temperature is about 80 ° C. 55 ~ within these temperature ranges
When 65 ° C is adopted, it has a substantially complete bactericidal action, and can also clean the fungi attached to the device,
Further, it is particularly preferable because it has high safety in work. The equipment used for desalting molasses to which the method of the present invention is applied includes a molasses filter, a desalting apparatus main body, a processing apparatus before and after the desalting apparatus, and auxiliary equipment. As a concrete cleaning and sterilizing means, a method of immersing these devices in hydrochloric acid to be used, a means of applying vibration or the like to the hydrochloric acid or the device to sufficiently bring the hydrochloric acid into contact with the device, or hydrochloric acid Appropriate means can be adopted such as flowing the above through these devices.

[作用] 本発明における作用は塩酸の微生物の産成せる水不溶
性粘着物質の加水分解作用と必ずしも明確でないが、15
〜30%、40〜80℃の塩酸は、微生物に対する酸としての
細胞に働きかける加水分解作用と高濃度であるが故の浸
透作用により微生物の細胞を容易に破壊し、殺菌と同時
に洗浄が可能になるものと思われる。
[Action] The action in the present invention is not always clear as the action of hydrochloric acid on the hydrolysis of the water-insoluble adhesive substance produced by the microorganisms.
Hydrochloric acid of ~ 30%, 40 ~ 80 ° C easily destroys the cells of microorganisms due to the hydrolysis action that acts on the cells as an acid against the microorganisms and the permeation action due to its high concentration, enabling sterilization and washing at the same time. It seems to be.

本発明者等は甘蔗原料糖工場の電気透析装置内、及び
圧力計の圧力検出部、附属配管内などの菌叢発生箇所か
ら生菌を採取し、水不溶性粘着物質を多量に生産する菌
10株を純粋分離し、これらの菌と菌が生産する水不溶性
粘着物質の基本的性質の解明を行った。その結果、これ
らの菌は全てバチルス(Bacillus)属の桿菌であること
が明らかとなり、水不溶性粘着物質は温塩酸、好ましく
は温度40〜60℃、濃度15〜30%の塩酸に容易に溶解する
ことを見出した。
The present inventors collect viable bacteria in the electrodialysis device of the sugar cane raw sugar factory, the pressure detection part of the pressure gauge, and the bacterial flora generation site such as the attached pipe, and produce a large amount of the water-insoluble adhesive substance.
The 10 strains were purely isolated, and the basic properties of these fungi and the water-insoluble adhesive substances produced by the fungi were clarified. As a result, it was revealed that all of these bacteria were Bacillus bacilli, and the water-insoluble adhesive substance was easily dissolved in warm hydrochloric acid, preferably at a temperature of 40 to 60 ° C and a concentration of 15 to 30% hydrochloric acid. I found that.

次に水不溶性粘着物質の溶解性に関する試験の結果を
示す。
Next, the result of the test concerning the solubility of the water-insoluble sticky substance will be shown.

[供試材料]沖縄の3段煎糖方式甘蔗原料糖工場のII番
蜜を固形分濃度18%に稀釈し、これを倍地として水不溶
性粘着物質を生産する分離菌株を72時間、55℃で振盪培
養した後、生産された水不溶性粘着物質を遠心分取して
供試した。
[Sample material] No.2 honey from Okinawa's three-stage decoction type sugar cane raw sugar factory was diluted to a solid concentration of 18%, and the isolated strain that produces a water-insoluble sticky substance was used for 72 hours at 55 ° C. After culturing with shaking at, the produced water-insoluble sticky substance was centrifuged and tested.

[試験方法]水不溶性粘着物質を含む培養表面の菌塊
(ペリクル)の小片を試験管内の所定濃度の塩酸、硫酸
又は水酸化ナトリウム溶液に投入し、所定温度で約1分
間振盪して溶解性を観察した。
[Test method] A small piece of a bacterial mass (pellicle) on the culture surface containing a water-insoluble adhesive substance is put into a hydrochloric acid, sulfuric acid or sodium hydroxide solution having a predetermined concentration in a test tube, and the mixture is shaken at a predetermined temperature for about 1 minute to be soluble. Was observed.

[結果] 試験結果は−、+、±、++、で表示し、その意味は
次の通りである。
[result] The test results are indicated by-, +, ±, ++, and their meanings are as follows.

−溶解しない。-Does not dissolve.

±僅かに溶解する。± Slightly soluble.

+溶解するが不完全。+ Dissolved but incomplete.

++完全に溶解する。++ Completely dissolve.

塩酸、硫酸、水酸化ナトリウム以外にも酢酸、クエン
酸について試験した結果、全く溶解しなかった。
As a result of testing acetic acid and citric acid in addition to hydrochloric acid, sulfuric acid and sodium hydroxide, they were not dissolved at all.

この試験においてはイオン交換膜、特にアニオン交換
膜の耐熱温度は60℃であり、塩酸の実用最高濃度は30%
である故、この温度と濃度が上限となる。試験の結果、
洗浄に使用する塩酸の温度40℃以下、濃度15%以下では
急激に効果が低下することが明らかとなった。また、水
不溶性粘着物質の化学的分析によってグルコース、ガラ
クトースなどの重合物が主成分であることも明らかにな
った。
In this test, the heat-resistant temperature of the ion-exchange membrane, especially the anion-exchange membrane, is 60 ℃, and the practical maximum concentration of hydrochloric acid is 30%.
Therefore, this temperature and concentration are the upper limits. Test results,
It was clarified that when the temperature of hydrochloric acid used for cleaning was 40 ° C or less and the concentration was 15% or less, the effect was drastically reduced. In addition, it was revealed by chemical analysis of the water-insoluble adhesive substance that polymers such as glucose and galactose are the main components.

なお、本発明は、その他ホエイ、醤油等の食品関係の
脱塩、濾過、装置の殺菌、洗浄にも用い得る。
The present invention can also be used for desalting, filtration, sterilization and cleaning of devices such as whey and soy sauce.

[実施例1] 濾過器を備え、陽イオン交換膜(旭硝子社製CMV)900
枚および陰イオン交換膜(旭硝子社製AMV)900枚を膜間
隔0.75mmで交互に配置された電気透析槽からなる脱塩装
置を用い、糖蜜の脱塩を24時間連続して行ったところ、
濾過器入口の圧力が0.2kg/cm2から0.7kg/cm2に、透析槽
入口の圧力が0.4kg/cm2から1.5kg/cm2に、夫々上昇し
た。糖蜜の脱塩を中止し、40℃に保持された18%の食添
用塩酸を20m3/時の割合で濾過器及び透析槽に対し、糖
蜜に代えて30分間流通せしめた後、通常の運転に復した
ところ、圧力が濾過器で0.3kg/cm2に、透析槽では0.7kg
/cm2に低下した。この装置を解体して調べたところ、所
々に菌類の付着が認められ、この菌類は適正な環境下で
は増殖するおそれがあった。そこで引続き塩酸の温度を
55℃に上げ、同様の操作を行ったところ、入口圧力が濾
過器では0.2kg/cm2に、透析槽では0.4kg/cm2に夫々低下
し、解体の結果、菌類の残留は認められなかった。その
後は、2日に1度の割で前記40℃と55℃の洗浄を繰返す
ことにより濾過器及び透析槽の殺菌、洗浄を行い、安定
した操業が確保されている。
[Example 1] A cation exchange membrane (CMV manufactured by Asahi Glass Co., Ltd.) 900 equipped with a filter
And anion-exchange membrane (AMV manufactured by Asahi Glass Co., Ltd.) 900 sheets were used for desalination of molasses continuously for 24 hours using a desalting device consisting of electrodialysis tanks alternately arranged with a membrane interval of 0.75 mm.
The pressure at the inlet of the filter increased from 0.2 kg / cm 2 to 0.7 kg / cm 2 , and the pressure at the inlet of the dialysis tank increased from 0.4 kg / cm 2 to 1.5 kg / cm 2 . After desalting molasses was stopped, 18% hydrochloric acid for food addition kept at 40 ° C was passed through the filter and dialysis tank at a rate of 20 m 3 / hour for 30 minutes instead of molasses, and then normal After returning to operation, the pressure was 0.3 kg / cm 2 in the filter and 0.7 kg in the dialysis tank.
It fell to / cm 2 . When this device was disassembled and examined, adhesion of fungi was found in some places, and this fungus was likely to grow in an appropriate environment. Therefore, the temperature of hydrochloric acid
Raised to 55 ° C., it was subjected to the same operation, to 0.2 kg / cm 2 at the inlet pressure filter, the dialysis cell respectively reduced to 0.4 kg / cm 2, a result of dismantling the remaining fungi observed It was After that, the filter and the dialysis tank are sterilized and washed by repeating the washing at 40 ° C. and 55 ° C. every two days to ensure stable operation.

[実施例2] カチオン膜と耐汚染アニオン膜を組み合わせた膜有効
面積0.23m2の電気透析装置((旭硝子社製DU−ob型)を
バッチ方式により7サイクル/日、3時間/サイクルの
運転を30日間行った。
[Example 2] An electrodialyzer (a DU-ob type manufactured by Asahi Glass Co., Ltd.) having a membrane effective area of 0.23 m 2 in which a cation membrane and an antifouling anion membrane are combined is operated in a batch system for 7 cycles / day for 3 hours / cycle. For 30 days.

沖縄の3段煎糖方式甘蔗料糖工場のII番糖蜜を約2倍
に水で稀釈した後、珪藻土をプレコートした濾過機で濾
過した糖蜜を原料として、糖蜜濃度35%、温度40℃、膜
面流速LV=10cm/sec、膜間電圧0.2〜0.4V/対で電気透析
を行った。電気透析を開始してから3日後に電気透析槽
への原液の流量が減少し、4日目に電気透析槽を組み込
んだまま、水でポンプ循環洗浄した後に、50℃、15%の
塩酸でポンプ循環洗浄し、再び水でポンプ循環洗浄し
た。
After diluting the No. 2 molasses from the three-stage decoction type sugar cane sugar factory in Okinawa with water about twice, the molasses filtered with a filter precoated with diatomaceous earth was used as the raw material, molasses concentration 35%, temperature 40 ° C, membrane Electrodialysis was performed at a surface flow rate of LV = 10 cm / sec and a transmembrane voltage of 0.2 to 0.4 V / pair. After 3 days from the start of electrodialysis, the flow rate of the stock solution into the electrodialysis tank decreased, and on the 4th day, with the electrodialysis tank installed, after washing with pump circulation with water, 50 ° C, 15% hydrochloric acid was used. The pump was circulated and washed again with water.

この洗浄操作によって、原液の膜面流速は完全に回復
した。このようにして、2〜3日に1回、温塩酸で電気
透析槽内を洗浄することにより、電気透析槽を解体せず
に30日間運転を継続した後に、電気透析槽を解体して内
部を観察したところ、水不溶性粘着物質の付着は全く認
められなかった。
By this washing operation, the membrane surface flow velocity of the stock solution was completely recovered. In this way, by washing the inside of the electrodialysis tank with warm hydrochloric acid once every 2 to 3 days, the electrodialysis tank is disassembled after the operation is continued for 30 days without disassembling the electrodialysis tank. As a result, the adhesion of the water-insoluble adhesive substance was not observed at all.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】糖蜜液の脱塩に用いる機器を温度40℃以上
の塩酸と接触せしめることを特徴とする糖蜜液の脱塩に
用いる機器の洗浄、殺菌方法。
1. A method for cleaning and sterilizing a device used for desalting molasses liquid, which comprises bringing the device used for desalting molasses liquid into contact with hydrochloric acid at a temperature of 40 ° C. or higher.
【請求項2】温度は40〜80℃である請求の範囲1の洗
浄、殺菌方法。
2. The cleaning and sterilizing method according to claim 1, wherein the temperature is 40 to 80 ° C.
【請求項3】塩酸の濃度は15〜30%である請求の範囲1
の洗浄、殺菌方法。
3. The concentration of hydrochloric acid is 15 to 30%.
How to clean and sterilize.
JP61263941A 1986-11-07 1986-11-07 Method for cleaning and sterilizing equipment used for desalting sugar-tight liquid Expired - Lifetime JPH0822307B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61263941A JPH0822307B2 (en) 1986-11-07 1986-11-07 Method for cleaning and sterilizing equipment used for desalting sugar-tight liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61263941A JPH0822307B2 (en) 1986-11-07 1986-11-07 Method for cleaning and sterilizing equipment used for desalting sugar-tight liquid

Publications (2)

Publication Number Publication Date
JPS63186655A JPS63186655A (en) 1988-08-02
JPH0822307B2 true JPH0822307B2 (en) 1996-03-06

Family

ID=17396385

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61263941A Expired - Lifetime JPH0822307B2 (en) 1986-11-07 1986-11-07 Method for cleaning and sterilizing equipment used for desalting sugar-tight liquid

Country Status (1)

Country Link
JP (1) JPH0822307B2 (en)

Also Published As

Publication number Publication date
JPS63186655A (en) 1988-08-02

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