JPS603494B2 - Sterilization method for modules in reverse osmosis equipment - Google Patents
Sterilization method for modules in reverse osmosis equipmentInfo
- Publication number
- JPS603494B2 JPS603494B2 JP57134500A JP13450082A JPS603494B2 JP S603494 B2 JPS603494 B2 JP S603494B2 JP 57134500 A JP57134500 A JP 57134500A JP 13450082 A JP13450082 A JP 13450082A JP S603494 B2 JPS603494 B2 JP S603494B2
- Authority
- JP
- Japan
- Prior art keywords
- module
- reverse osmosis
- temperature
- modules
- juice
- 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
Links
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- Non-Alcoholic Beverages (AREA)
- Apparatus For Disinfection Or Sterilisation (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Description
【発明の詳細な説明】
本発明は逆浸透装置におけるモジュールの殺菌方法、更
に詳しくは野菜及び/又は果実の搾汁液(以下単に搾汁
液と略称する)を逆浸透装置で濃縮する場合において絶
対的に避けられない問題であるモジュールの菌的汚染を
極めて効率的に且つ安全確実に解消し、結局は濃縮効率
をも向上し得る殺菌方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention provides a method for sterilizing modules in a reverse osmosis device, more specifically, an absolute The present invention relates to a sterilization method that can extremely efficiently and safely eliminate bacterial contamination of modules, which is an unavoidable problem, and can ultimately improve concentration efficiency.
近年、搾汁液の濃縮に逆浸透法の利用が注目されている
。In recent years, the use of reverse osmosis to concentrate squeezed juice has attracted attention.
逆浸透法による搾汁液の濃縮は、その濃縮に際して相変
換を伴わないため、搾汁液の本来的品質(色、味、香等
)の維持に優れているからであり、既にかかる観点から
多くの提案がなされている(特関昭50−154494
、特関昭52一25052、特開昭52一105248
等)。ところで、搾汁液を逆浸透装置で連続的に濃縮す
ると、該装置に組み込まれているモジュールの膿面に種
々の物質が付着堆積してその濃縮効率を損なうようにな
る一方、該モジュールが次第に菌的汚染され、この菌的
汚染が急激に増長する結果、その許容限度を超えて、製
品である濃縮物に品質上の重大な悪影響を及ぼすように
なる。すなわち、搾汁液を逆浸透装置で濃縮する実際の
場面においては、或る期間運転した後、一旦これを休止
し、モジュールの膜面に付着堆積してくる物質を除去し
、モジュールの菌的汚染を解消する殺菌を行ってから運
転を再開することが必要である。従来、かかる付着物質
の除去に関しては、一般にスポンジボールによる方法が
行なわれているが、圧力差を利用した半透膜の弾性作用
によって膜面付着物質を剥離し易くした後にフラッシン
グする方法やこれらを併用する方法(特開昭51一79
686)も提案され、いずれにしても所期の洗浄目的が
蓮せられている。This is because concentrating squeezed juice by reverse osmosis does not involve phase transformation during concentration, so it is excellent in maintaining the original quality of the squeezed liquid (color, taste, aroma, etc.). A proposal has been made (Tokukan Sho 50-154494
, Tokukai Sho 52-25052, Tokukai Sho 52-105248
etc). By the way, when squeezed juice is continuously concentrated using a reverse osmosis device, various substances adhere to and accumulate on the pus surface of the module incorporated in the device, impairing its concentration efficiency, while the module gradually becomes infected with bacteria. As a result, this bacterial contamination increases rapidly, exceeding the permissible limit and having a serious adverse effect on the quality of the concentrate product. In other words, in the actual situation where squeezed juice is concentrated using a reverse osmosis device, after operating for a certain period of time, the device is temporarily stopped, and substances that have accumulated on the membrane surface of the module are removed to prevent bacterial contamination of the module. It is necessary to perform sterilization to eliminate this problem before restarting operation. Conventionally, a method using a sponge ball has been generally used to remove such adhered substances, but there are also methods that use the elastic action of a semipermeable membrane that utilizes a pressure difference to make it easier to peel off the adhered substances on the membrane surface, and then flushing. Method of combined use (Japanese Patent Application Laid-Open No. 51-79
686) has also been proposed, and in any case, the intended purpose of cleaning is maintained.
ところが、モジュールの殺菌に関しては、特に新らしい
提案はなく、従来一般に、次亜塩素酸の如き化学的殺菌
剤の水溶液をモジュール内に通過せしめる方法が行なわ
れているにすぎない。However, no new proposals have been made regarding the sterilization of modules, and the conventional method has generally been to pass an aqueous solution of a chemical sterilizer such as hypochlorous acid into the module.
しかし、化学的殺菌剤を使用する従釆一般の方法による
と、セルロースアセテート膜で代表されるような搾汁液
の濃縮に通常使用されるモジュ−ルの半透膜素材に対し
ては、その膜機能を損なわないようにするため、濃い濃
度の化学的殺菌剤を用いることができず、したがって薄
い濃度の化学的殺菌剤を用いざるを得ないのであるが、
これがためモジュールの殺菌に極めて長時間を要し「
しかもその殺菌程度が必ずしも充分でない等〜バラッキ
が大きいという欠点がある。勿論、逆浸透装置に組み込
まれているモジュールをその都度分解して殺菌すること
も考えられるが、これではあまりにも非現実的である。
そこでL搾汁液を逆浸透装置で濃縮する実際の場面では
Lモジュールを効率的且つ安全確実に殺菌する方法の出
現が強く要請されている。However, conventional methods using chemical disinfectants have shown that the semi-permeable membrane materials of modules commonly used for concentrating juice, such as cellulose acetate membranes, cannot be used. In order not to impair functionality, it is not possible to use chemical disinfectants in high concentrations, and therefore chemical disinfectants in dilute concentrations must be used.
As a result, it takes an extremely long time to sterilize the module.
Moreover, there is a drawback that the degree of sterilization is not necessarily sufficient, etc., and there is a large variation. Of course, it is possible to disassemble and sterilize the module incorporated in the reverse osmosis device each time, but this is extremely impractical.
Therefore, in the actual situation where L juice is concentrated using a reverse osmosis device, there is a strong demand for a method to sterilize the L module efficiently and safely.
本発明は、かかる要請に応える」モジュールの改良され
た殺菌方法を提供するものである。The present invention provides an improved method for sterilizing modules that meets such needs.
以下、図面に基づいて本発明の構成を詳細に説明する。
第1図は、濃縮手順及び洗浄手順をも含んで「本発明の
殺菌手順を例示する系統図である。Hereinafter, the configuration of the present invention will be explained in detail based on the drawings.
FIG. 1 is a system diagram illustrating the sterilization procedure of the present invention, including a concentration procedure and a washing procedure.
供給タンクー内の搾汁液が圧力ポンプ2で逆浸透装置3
へ圧送される。図面で例示する逆浸透装置3は内圧式管
状モジュール4が多数連結されている一過式のものであ
る。前記のように圧送された搾汁液は「内圧式管状モジ
ュール4内を高圧下に流遇する間に濃縮され、該モジュ
ールに取り付けられた半透膜を透過した主として水分か
らなる液が受けタンク5へ排出される一方「濃縮物が連
結されている該モジュールの末端出口から製品タンク6
へ回収される。このような濃縮を或る期間連続して行う
と、内圧式管状モジュール4の膜面に種々の物質が付着
堆積し、また該モジュールが次第に菌的汚染され、これ
らが逆浸透装置の実用的運転上又は得られる濃縮物の品
質上許容限度を超えるようになる。そこで、一般的には
搾汁液の供給側に組み込まれているスポンジボール洗浄
装置7,7′によって、スポンジボールを内圧式管状モ
ジュール4内へ通過させ、膜面の付着堆積物質を剥離除
去して洗浄する。The squeezed liquid in the supply tank is sent to the reverse osmosis device 3 by the pressure pump 2.
is pumped to. The reverse osmosis device 3 illustrated in the drawing is a one-time type device in which a large number of internal pressure type tubular modules 4 are connected. The squeezed liquid pumped as described above is concentrated while flowing under high pressure inside the internal pressure type tubular module 4, and the liquid mainly composed of water that has passed through the semipermeable membrane attached to the module is transferred to the receiving tank 5. from the terminal outlet of the module to which the concentrate is connected to the product tank 6.
will be collected. If such concentration is continued for a certain period of time, various substances will adhere to and accumulate on the membrane surface of the internal pressure type tubular module 4, and the module will gradually become contaminated with bacteria, which will impede the practical operation of the reverse osmosis device. or the quality of the resulting concentrate exceeds acceptable limits. Therefore, the sponge balls are passed through the internal pressure type tubular module 4 using sponge ball cleaning devices 7, 7', which are generally installed on the juice supply side, and the deposited substances on the membrane surface are peeled off and removed. Wash.
そして次のように、本発明に係る殺菌方法を行う。但し
ト膜面への物質の付着堆積とモジュールの菌的汚染とが
同時に許容限度を超えるとは限らないので、場合によっ
ては、叙上の如き洗浄を省略して、次の殺菌のみが行な
われることもある。先ず「連結されている内圧式管状モ
ジュWル4を逆浸透装置3に組み込まれている状態で遮
閉室8内に封じる。Then, the sterilization method according to the present invention is performed as follows. However, since it is not always the case that the accumulation of substances on the membrane surface and the bacterial contamination of the module exceed the permissible limit at the same time, in some cases, the cleaning described above may be omitted and only the next sterilization is performed. Sometimes. First, the connected internal pressure type tubular module W module 4 is sealed in the closed chamber 8 while being incorporated into the reverse osmosis device 3.
この遮閉室8は例えば前述の如き濃縮の際の比較的低温
に維持することの望まれる温度管理をし得るように適宜
に組立又は分解乃至開閉可能であるものが好ましく、そ
の素材は特に限定されないが、後述するような加熱温度
保持の観点から「 ポリウレタンフオームの如き断熱材
が好ましい。次に「前記遮閉室8内へ導入されている配
管9から生の水蒸気を吹き込んで該遮閉室8内を加熱す
る。This closed chamber 8 is preferably one that can be assembled or disassembled or opened and closed as appropriate so as to be able to control the temperature, which is desired to be maintained at a relatively low temperature during concentration as described above, and the material thereof is not particularly limited. However, from the viewpoint of maintaining the heating temperature as described later, it is preferable to use a heat insulating material such as polyurethane foam. Heat.
最後に、かかる加熱状態を維持して、前記内圧式管状モ
ジュール4の膜面全域が7000以上の温度となるよう
にt貯水タンク10から温度制御の可能なヒータilを
介し、圧力ポンプ2を利用して温水を該モジュール内に
通過せしめる。Finally, while maintaining this heating state, the pressure pump 2 is used from the water storage tank 10 via the temperature-controllable heater il so that the entire membrane surface of the internal pressure type tubular module 4 has a temperature of 7000 or higher. to allow hot water to pass through the module.
勿論、予め加熱された温水を用いればヒーター1を省略
することもできる。かかる殺菌操作中、遮閉室8内の温
度及び温水の温度は内圧式管状モジュール4に取り付け
られている半透膜の膜機能を損なわない程度に制御する
。Of course, if preheated hot water is used, the heater 1 can be omitted. During this sterilization operation, the temperature in the closed chamber 8 and the temperature of the hot water are controlled to such an extent that the membrane function of the semipermeable membrane attached to the internal pressure type tubular module 4 is not impaired.
例えば、搾汁液の逆浸透装置による濃縮に通常使用され
るセルロースアセテート膜の場合、80〜85o0以上
になるとその膜機能が損なわれるようになるため、この
場合には遮閉室8内の温度及び温水の温度は80q0以
下とする。したがって同様の意味で、遮閉室8内へ吹き
込む水蒸気は、局部的に内圧式管状モジュール4を過熱
することのないように、要すれば別に遮閉板等を介在さ
せて「除々に吹き込むのが好ましい。本発明者らの試験
によれば、トマトやニンジン更にはリンゴその他の野菜
や果実に搾汁液を逆浸透装置で濃縮する場合、組み込ま
れているモジュールに運転中に発生する菌的汚染の原因
を大勢を占める菌種は「温度7000以上において急激
に死滅することが見出された。For example, in the case of a cellulose acetate membrane that is normally used for concentrating squeezed juice using a reverse osmosis device, its membrane function will be impaired if the temperature exceeds 80 to 85 o0. The temperature shall be 80q0 or less. Therefore, in the same sense, it is recommended that the water vapor blown into the closed chamber 8 be blown into the closed chamber 8 gradually by interposing a separate shielding plate or the like, if necessary, so as not to locally overheat the internal pressure type tubular module 4. Preferable.According to the tests conducted by the present inventors, when the juice of tomatoes, carrots, apples, and other vegetables and fruits is concentrated using a reverse osmosis device, the built-in module is free from bacterial contamination that occurs during operation. ``It was discovered that the bacterial species that account for the majority of the causes die rapidly at temperatures above 7,000.
本発明において、モジュールの膿面全域を7000以上
にするのはこのためであり、またモジュールを遮閉室内
に封じて該遮開室内を水蒸気で加熱し「併せて温水をモ
ジュール内へ通過せしめるのは、モジュールへ取り付け
られている半透膜の膜機能を損なわないように、できる
だけ穏やかな条件下で、しかも短時間に前述の70午○
という温度をモジュールの膜面全域で確保するためであ
る。本発明によれば、殺菌工程から濃縮運転再開までの
間に外部からの菌による汚染の機会もなく、特別の薬品
も使用しないので〜再開後の製品の品質が変化するおそ
れがない。第2図は、前記した第1図の系統図にしたが
って次の条件下で温水を通過させた場合における、殺菌
時間(分)と内圧式管状モジュール4の末端から排出さ
れる水の出口温度(℃)との関係を例示するグラフであ
る。条件:外気温度=2000、温水温度=8000、
温水供給量=300夕/時、半透膜=セルロースアセテ
ート膜(ダイセル社製、DRS95)、モジュール律コ
14側め、モジュール全長=200の。This is why, in the present invention, the entire surface area of the module is set to 7,000 or more, and the module is sealed in a closed chamber and the interior of the shielded chamber is heated with steam to allow hot water to pass into the module. In order not to impair the membrane function of the semipermeable membrane attached to the module, the above-mentioned 70 pm test should be carried out under as gentle conditions as possible and for a short period of time.
This is to ensure that temperature throughout the membrane surface of the module. According to the present invention, there is no chance of contamination by bacteria from the outside between the sterilization process and the restart of the concentration operation, and no special chemicals are used, so there is no risk that the quality of the product will change after the restart. FIG. 2 shows the sterilization time (minutes) and the outlet temperature ( 9 is a graph illustrating the relationship between the temperature and temperature (°C). Conditions: outside air temperature = 2000, hot water temperature = 8000,
Hot water supply rate = 300 pm/hour, semipermeable membrane = cellulose acetate membrane (manufactured by Daicel Corporation, DRS95), module length 14 side, module total length = 200 pm.
第2図において、曲線A(図中△印)は内圧式管状モジ
ュール4を遮閉室8内に封じることなくそのまま外気に
露出させた従来一般的状態の場合、曲線Bは内圧式管状
モジュール4をポリウレタンフオーム製の断熱材で形成
された遮閉室8内へ封じて該遮閉室8内を加熱すること
なくそのままにした場合、曲線Cは曲線Bの場合に加え
て更に遮閉室8内を生の水蒸気で70COに加熱した本
発明に係る場合である。そして、機軸の時間はいずれも
、供給した溢水が内圧式管状モジュール4の末端出口か
ら排出開始された時を0分とした。この第2図からも、
入口溢水温度が80ooの場合、曲線Aで示されるよう
に、一般的な装置では所望する7000以上という温度
を確保することが著るしく困難であり、遮閉室を設けた
だけの曲線Bでもある程度の効果は認められるがなお不
充分であって、本発明に係る曲線Cにおいて、わずかに
2び分という短時間で所望する7000以上という温度
が確保され、したがって内圧式管状モジュール4の膜面
全域において充分な殺菌温度になっていることが明らか
である。前述の如く、搾汁液を逆浸透装置で濃縮する場
合、モジュールを菌的汚染する菌種は7000以上にお
いて急激に死滅する。In FIG. 2, curve A (indicated by △ in the figure) represents the conventional common state in which the internal pressure type tubular module 4 is exposed to the outside air without being sealed in the closed chamber 8, and curve B represents the internal pressure type tubular module 4. When the sealed chamber 8 formed of a polyurethane foam heat insulating material is sealed and the sealed chamber 8 is left as it is without being heated, the curve C shows that in addition to the case of the curve B, the inside of the closed chamber 8 is heated. This is the case according to the present invention in which the temperature was heated to 70CO with water vapor. In each case, the axis time was set to 0 minutes when the supplied overflow water started to be discharged from the terminal outlet of the internal pressure type tubular module 4. From this second figure,
When the inlet overflow temperature is 80 oo, as shown by curve A, it is extremely difficult to secure the desired temperature of 7,000 or higher with a general equipment, and even with curve B, which is only provided with a closed room, it is difficult to maintain the desired temperature of 7,000 or higher. Although the effect is recognized, it is still insufficient, and in curve C according to the present invention, the desired temperature of 7000 or more is secured in a short time of only 2 minutes, and therefore the entire membrane surface of the internal pressure type tubular module 4 is It is clear that the temperature is sufficient for sterilization. As mentioned above, when the squeezed juice is concentrated using a reverse osmosis device, the bacterial species that contaminate the module rapidly become extinct when the number of bacteria exceeds 7,000.
しかし、モジュールをほぼ完全殺菌するには〜 700
0以上の温度においても一定の時間が必要である。そし
てこの必要時間は、特にモジュールの鰭的汚染の程度に
よって影響される。本発明者らの試験によると、かかる
場合において例えば、得られる濃縮物の生菌数が1ぴ〜
1び値/タ程度まで菌的汚染されたモジュールは、?ぴ
○×1び分間程度でよい。したがって、叙上の程度に菌
的汚染されたモジュールは、第2図における本発明の場
合を示す曲線Cにおいては殺菌処理時間30分でほぼ完
全に殺菌されるのである。第3図は、前記第1図の系統
図にしたがいトマトの搾汁液を連続濃縮して菌的汚染さ
れた内圧式管状モジュール4を、ほぼ完全に殺菌した場
合(図中曲線D)と不充分に殺菌した場合(図中曲線E
)とで、その後に再びトマトの搾汁液を連続濃縮したと
きの、連続濃縮時間(時)と得られた濃縮物生菌数(個
/夕)との関係を例示するグラフである。However, to almost completely sterilize the module ~700
A certain amount of time is required even at temperatures above 0. This required time is in particular influenced by the degree of fin contamination of the module. According to the tests conducted by the present inventors, in such cases, for example, the number of viable bacteria in the concentrate obtained is 1 to 1.
What about modules that are bacterially contaminated to a level of 1? About 1 minute is enough. Therefore, a module that is bacterially contaminated to the above degree is almost completely sterilized in 30 minutes of sterilization time in curve C showing the case of the present invention in FIG. FIG. 3 shows a case in which the internal pressure type tubular module 4, which has been bacterially contaminated by continuously concentrating tomato juice according to the system diagram in FIG. (Curve E in the figure)
) is a graph illustrating the relationship between the continuous concentration time (hours) and the number of viable bacteria in the obtained concentrate (cells/night) when tomato juice is continuously concentrated again after that.
但し、連続濃縮の条件は次の通りである。条件:半透膜
=セルロースアセテート膜(ダイセル社製、DRS95
)、モジュール径=13肋◇、全膜面積=20め、搾汁
液供給側圧力=50〜60k9/塊、搾汁液糖度=4.
9%(Brix)、搾汁液温度=35℃、搾汁液供給量
=300夕/時、濃縮倍率=3.耳音(礎度換算)、外
気温=21℃。However, the conditions for continuous concentration are as follows. Conditions: Semipermeable membrane = cellulose acetate membrane (manufactured by Daicel, DRS95
), module diameter = 13 ribs ◇, total membrane area = 20mm, juice supply side pressure = 50-60k9/lump, juice sugar content = 4.
9% (Brix), juice temperature = 35°C, juice supply amount = 300 evenings/hour, concentration ratio = 3. Ear sounds (converted to basic temperature), outside temperature = 21℃.
この第3図からも明らかなように、モジュールの菌的汚
染の許容限界が得られる濃縮物の生菌数で仮りに1ぴ個
/夕である場合(通常、これ以上にモジュールが菌的汚
染されると、得られる濃縮物に品質上重大な悪影響を及
ぼす)、前述の如く本発明によってモジュールをほぼ完
全に殺菌しておけばその後再び3斑時間程度の連続濃縮
をすることができるが(曲線D)、モジュールの殺菌が
不充分であるとその後の連続運転は1斑時間程度しかで
きないのである。As is clear from Fig. 3, if the viable cell count of the concentrate is 1 bacteria per night (normally, if the module is contaminated with bacteria beyond this limit) If the module is almost completely sterilized by the present invention as described above, continuous concentration can be performed again for about 3 hours ( Curve D), if the sterilization of the module is insufficient, subsequent continuous operation can only be performed for about one hour.
(曲線E)。以上説明した通りであるから、本発明には
、搾汁液を逆浸透装置で濃縮する場合において絶対的に
避けられない問題であるモジュールの菌的汚染を極めて
効率的に且つ安全確実に解消し、結局は濃縮効率をも向
上することができる効果がある。(Curve E). As explained above, the present invention provides an extremely efficient and safe way to eliminate bacterial contamination of the module, which is an absolutely unavoidable problem when concentrating squeezed juice using a reverse osmosis device. In the end, it has the effect of improving concentration efficiency.
第1図は本発明の殺菌手順を例示する系統図、第2図は
殺菌時間とモジュールの末端から排出される水の出口温
度との関係を例示するグラフ、第3図は連続濃縮時間と
得られた濃縮物生菌数との関係を例示するグラフである
。
亀・・・・・・供給タンク、2・…・・圧力ポンプ、3
……逆浸透装置、4・・・・・・内圧式管状モジュール
、5・・・…受けタンク、6・・・・・・製品タンク、
7・……スポンジボール洗浄装置「 8…・・・遮閉室
ト9・・…・配管、lo…・・・貯水タンク。
第1図
第2図
第3図Figure 1 is a system diagram illustrating the sterilization procedure of the present invention, Figure 2 is a graph illustrating the relationship between sterilization time and outlet temperature of the water discharged from the end of the module, and Figure 3 is a graph illustrating the relationship between continuous concentration time and yield. 2 is a graph illustrating the relationship between the number of viable bacteria in the concentrate and Tortoise... Supply tank, 2... Pressure pump, 3
... Reverse osmosis device, 4 ... Internal pressure type tubular module, 5 ... Receiving tank, 6 ... Product tank,
7. Sponge ball cleaning device 8... Closed room 9... Piping, lo... Water storage tank. Figure 1 Figure 2 Figure 3
Claims (1)
を使用し、使用後のモジユールを再使用のために殺菌す
る方法であって、前記逆浸透装置に組込まれているモジ
ユールを取囲んで遮閉室を形成し、該遮閉室内に蒸気を
導入するとともに、前記モジユール内に温水を導入し、
該モジユールの逆浸透膜面全域を70℃以上に保持する
ことを特徴とする逆浸透装置におけるモジユールの殺菌
方法。1 A method in which a reverse osmosis device is used to concentrate the juice of vegetables and/or fruits, and the module is sterilized for reuse after use, and the module incorporated in the reverse osmosis device is surrounded. forming a closed chamber, introducing steam into the closed chamber and introducing hot water into the module,
A method for sterilizing a module in a reverse osmosis device, the method comprising maintaining the entire reverse osmosis membrane surface of the module at 70°C or higher.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57134500A JPS603494B2 (en) | 1982-07-31 | 1982-07-31 | Sterilization method for modules in reverse osmosis equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57134500A JPS603494B2 (en) | 1982-07-31 | 1982-07-31 | Sterilization method for modules in reverse osmosis equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5925750A JPS5925750A (en) | 1984-02-09 |
| JPS603494B2 true JPS603494B2 (en) | 1985-01-29 |
Family
ID=15129770
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57134500A Expired JPS603494B2 (en) | 1982-07-31 | 1982-07-31 | Sterilization method for modules in reverse osmosis equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS603494B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4949658B2 (en) * | 2005-06-22 | 2012-06-13 | ダイセン・メンブレン・システムズ株式会社 | Dialysis water production apparatus and sterilization method thereof |
| JP6015654B2 (en) * | 2012-03-16 | 2016-10-26 | 東レ株式会社 | Separation method for separation membrane module, method for producing chemicals by continuous fermentation, and membrane separation type continuous fermentation apparatus |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5272996U (en) * | 1975-11-27 | 1977-05-31 |
-
1982
- 1982-07-31 JP JP57134500A patent/JPS603494B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5925750A (en) | 1984-02-09 |
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