JPH02116375A - Disinfecting method for fermentation raw materials - Google Patents
Disinfecting method for fermentation raw materialsInfo
- Publication number
- JPH02116375A JPH02116375A JP63270321A JP27032188A JPH02116375A JP H02116375 A JPH02116375 A JP H02116375A JP 63270321 A JP63270321 A JP 63270321A JP 27032188 A JP27032188 A JP 27032188A JP H02116375 A JPH02116375 A JP H02116375A
- Authority
- JP
- Japan
- Prior art keywords
- tube
- porous tube
- steam
- raw materials
- fermentation raw
- 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.)
- Granted
Links
Landscapes
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Alcoholic Beverages (AREA)
- Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
- Apparatus For Disinfection Or Sterilisation (AREA)
Abstract
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、醗酵原料の蒸煮殺菌方法に関する。[Detailed description of the invention] [Industrial application field] The present invention relates to a method for sterilizing fermentation raw materials by steaming.
更に詳しくは、蒸煮殺菌時における蒸煮管や配管等の内
部に泥や沈積物等のスラッジの発生・付着を防止する醗
酵原料の殺菌方法に関するものである。More specifically, the present invention relates to a method for sterilizing fermentation raw materials that prevents the generation and adhesion of sludge such as mud and deposits inside steaming pipes and piping during sterilization by steaming.
醗酵法によって有用物質を生産する。場合、醗酵原料中
の雑菌を除く為に、通常、蒸気により加熱殺菌する工程
が採用されている。醗酵原料としては廃糖蜜が最も安価
な原料の一つとして使用されている。Useful substances are produced by fermentation. In this case, a process of heating and sterilizing with steam is usually used to remove bacteria from the fermented raw materials. Blackstrap molasses is used as one of the cheapest raw materials for fermentation.
廃糖蜜等を醗酵原料として用いる場合、加熱蒸煮時に多
量のスラッジが発生し、配管、蒸煮管、槽内等に付着蓄
積することが大きな問題である。When molasses or the like is used as a fermentation raw material, a large amount of sludge is generated during heating and steaming, and it is a big problem that it accumulates in piping, steaming pipes, tanks, etc.
発生したスラッジは通常遠心分離や沈降法によって除去
されるが、高温に加熱される蒸煮管や配管等の内部にス
ラッジが付着、沈積し、これは殺菌汚染等の原因となる
ため、定期的な分解洗浄を余儀なくされる。Generated sludge is usually removed by centrifugation or sedimentation, but sludge adheres to and accumulates inside steaming pipes and piping that are heated to high temperatures, and this can cause sterilization contamination, so it must be removed periodically. Forced to disassemble and clean.
(問題点を解決するための手段〕
本発明者らは、かかる実情に鑑み、スラッジの付着、沈
積を防ぎ、醗酵原料の効果的な蒸煮殺菌方法について、
蒸気を多孔管の細孔を通して醗酵原料に接触させ殺菌す
れば、多孔管の細孔を通して醗酵原料液に接触した蒸気
が管の内面上に凝縮して水の膜を形成するか、多孔管の
内面上に蒸気の薄い層を形成し、その結果、スラッジの
沈着が防止されるのではないかとの考えに基づいて鋭意
研究の結果、所期の目的が達成されることを見出し、本
発明を完成した。(Means for Solving the Problems) In view of the above circumstances, the present inventors have proposed an effective steam sterilization method for fermentation raw materials that prevents the adhesion and deposition of sludge.
If steam is brought into contact with the fermentation raw material through the pores of the porous tube and sterilized, the steam that comes into contact with the fermentation raw material liquid through the pores of the porous tube will condense on the inner surface of the tube and form a water film, or Based on the idea that a thin layer of steam could be formed on the inner surface, and as a result, sludge deposition could be prevented, after extensive research, it was discovered that the desired objective could be achieved, and the present invention was developed. completed.
即ち、本発明は孔径0.5〜5fiの多孔管内部に醗酵
原料を流し、管の外部から水蒸気を供給することを特徴
とする醗酵原料の蒸煮殺菌方法を内容とする。That is, the present invention is directed to a method for sterilizing fermentation raw materials by steaming, which is characterized by flowing the fermentation raw materials inside a porous tube with a pore diameter of 0.5 to 5 fi, and supplying steam from the outside of the tube.
本発明に用いられる装置の一例を第1図に示す。An example of the apparatus used in the present invention is shown in FIG.
同図において蒸煮装置は多孔管(1)と該多孔管(1)
を取り囲む外筒管(2)とからなり、前記多孔管(1)
と外筒管(2)との間に蒸気室(3)が設けられている
。(4)は蒸気入口、(5)は蒸気出口、(6)は圧力
調節弁で温度コントローラー(7)と電気的に接続され
ている。In the figure, the steaming device includes a perforated pipe (1) and a perforated pipe (1).
an outer cylindrical tube (2) surrounding the porous tube (1);
A steam chamber (3) is provided between the outer cylinder pipe (2) and the outer cylinder pipe (2). (4) is a steam inlet, (5) is a steam outlet, and (6) is a pressure regulating valve that is electrically connected to a temperature controller (7).
(8)はドレイントラップである。(8) is a drain trap.
本発明に用いられる多孔管(1)の材質や孔径、形状等
については特に限定されないが、通常孔径0.5〜5日
、好ましくは1〜3fiの円筒状の耐食性のもの、例え
ばステンレス製のものを用いるのが便利である。上記装
置を用いて蒸煮殺菌する方法について説明すると、多孔
管(1)の一方から、醗酵原料、例えば水で希釈した糖
蜜(例えば30〜35%I!濃度)を送液し、低圧蒸気
を蒸気室(3)内に送る。この際、多孔管(1)内の醗
酵原料の圧力(Pl)に対し、蒸気室(3)内の蒸気圧
力(P2)を高めに設定される。多孔管(1)は一定の
滞留時間をもたせるに必要な長さに設定される。多孔管
(1)は蒸煮装2の一部、或いは全部に用いることがで
きる。The material, pore diameter, shape, etc. of the porous tube (1) used in the present invention are not particularly limited, but it is usually a cylindrical corrosion-resistant tube with a pore diameter of 0.5 to 5 days, preferably 1 to 3 fi, such as stainless steel. It is convenient to use something. To explain the method of steam sterilization using the above device, a fermentation raw material such as molasses diluted with water (e.g. 30-35% I! concentration) is sent from one side of the perforated pipe (1), and low pressure steam is steamed. Send it into room (3). At this time, the steam pressure (P2) in the steam chamber (3) is set higher than the pressure (Pl) of the fermentation raw material in the porous pipe (1). The perforated tube (1) is set to a length necessary to provide a constant residence time. The perforated pipe (1) can be used for part or all of the steamer 2.
以下、実施例によって本発明を更に詳細に説明するが、
本発明はこれらにより限定されるものではない。Hereinafter, the present invention will be explained in more detail with reference to Examples.
The present invention is not limited to these.
実施例1
孔径3Wmの多孔管(ステンレス製)エレメント(内径
40m、長さ1,00011)を内管としてもち、第1
図に示した形状の蒸煮装置を作製した。Example 1 A porous pipe (stainless steel) element (inner diameter 40 m, length 1,00011) with a pore diameter of 3 Wm was used as the inner pipe, and the first
A steaming apparatus with the shape shown in the figure was manufactured.
甘蔗糖蜜を水で希釈し糖蜜濃度約35%に設定し、遠心
分M機によりスラッジ成分を除去前処理した液を多孔管
内″に流速0.8 rd /Hrの割合で供給した。こ
の糖蜜液の圧力(Pl)に対し、多孔管外部より供給す
る蒸気の圧力(P2)を、八P=P2−PL・−0,5
〜1.0kg/cdGに設定して、殺菌(約120℃)
を行うた。120℃蒸煮48時間、10回累計時間48
0時間使用後の多孔管内のスケール(沈積物)を測定し
たところ、出口部分での0.1fi以下(軟着層形成)
程度のスケールの沈積が認められたのみで、多孔管内部
には糖蜜原料からくる色素の着色以外にスケールの沈積
は殆ど認められなかった。Cane molasses was diluted with water to set the molasses concentration to approximately 35%, and the liquid, which had been pretreated to remove sludge components using a centrifugal M machine, was supplied into the porous tube at a flow rate of 0.8 rd/Hr.This molasses liquid The pressure (P2) of the steam supplied from the outside of the porous pipe is calculated as follows: 8P=P2-PL・-0,5
Sterilize at ~1.0kg/cdG (approximately 120℃)
I wanted to do it. 120℃ steaming for 48 hours, 10 times cumulative time 48
When measuring the scale (deposits) inside the porous pipe after 0 hours of use, it was found to be less than 0.1fi at the outlet (soft layer formation).
Only some scale deposits were observed, and almost no scale deposits were observed inside the porous tube other than the coloring of the pigment coming from the molasses raw material.
対照として、多孔管の代わりに通常のステンレス製気液
混合ミキサーを用い同様の条件で試験を行ったところ、
168時間の使用で管内に5〜711のスケールの沈積
が認められた。As a control, we conducted a test under similar conditions using a regular stainless steel gas-liquid mixer instead of the perforated tube.
After 168 hours of use, scale deposits of 5 to 711 were observed inside the tube.
実施例2
フィリピン産廃糖蜜(I!濃濃度5弼
屯を蒸煮槽に送りこれを408BXに希釈後、第1図に
示す多孔管加熱装置を通じて蒸煮槽に循環させ、槽内糖
蜜温度を30℃から951℃迄2時間かけて昇温した.
この時の多孔管の孔径はl鰭、多孔管による加熱部の温
度は120℃であった。Example 2 Philippine blackstrap molasses (I! Concentration: 5 tons) was sent to a steaming tank, diluted to 408BX, and circulated to the steaming tank through the perforated tube heating device shown in Figure 1, and the molasses temperature in the tank was raised from 30°C. The temperature was raised to 951°C over 2 hours.
At this time, the pore diameter of the porous tube was 1 fin, and the temperature of the heating section by the porous tube was 120°C.
その後、糖蜜は槽内で95℃で4時間滞留せしめられた
後、遠心分離機によりスラッジ成分を除去後、培養工程
に供給された。Thereafter, the molasses was allowed to remain in the tank at 95°C for 4 hours, and after removing sludge components using a centrifuge, it was supplied to the culture process.
この実験を60回約1ケ月にわたり実施した後、多孔管
内部を分解点検した所、スケールの生成は殆ど認められ
なかった。After carrying out this experiment 60 times over a period of approximately one month, the inside of the porous tube was disassembled and inspected, and almost no scale formation was observed.
一方、対照としてステンレス二重管にて加熱を行い、約
1ケ月60回の繰り返し実験後、加熱部を点検した所、
管内壁面に約3111/Iw程度のスケールの付着が観
察された。On the other hand, as a control, heating was performed in a stainless steel double tube, and after repeating the experiment 60 times for about one month, the heating part was inspected.
Scale adhesion of approximately 3111/Iw was observed on the inner wall surface of the tube.
叙上の通り、本発明によれば、廃糖蜜など醗酵原料を用
いる場合、蒸煮殺菌時のスラッジの付着がなく、従って
長時間の連続運転が可能であり、またスラッジの付着沈
積がない為、雑菌汚染等の異常が少ない。As mentioned above, according to the present invention, when fermentation raw materials such as blackstrap molasses are used, there is no sludge adhesion during steam sterilization, so long-term continuous operation is possible, and since there is no sludge adhesion and sedimentation, There are few abnormalities such as bacterial contamination.
更に、本発明の大きな特徴として、殺菌時の騒音が極め
て小さいことが挙げられる.従来のスパージャ−や気液
混合ミキサー等を用いる蒸気殺菌の場合、温度を120
℃以上に維持する為に蒸気圧カフ〜10kg/c+aG
の高圧蒸気が用いられており、かなり大きな騒音と振動
の発生が避けられないが、本発明の場合は、従来法に比
べて低圧蒸気(2,5〜4kt/cdG)を用いること
ができるので騒音や振動の発生は著しく小さい。Furthermore, a major feature of the present invention is that noise during sterilization is extremely low. In the case of steam sterilization using a conventional sparger or gas-liquid mixer, the temperature should be set to 120℃.
Steam pressure cuff ~10kg/c+aG to maintain temperature above ℃
However, in the case of the present invention, lower pressure steam (2.5 to 4 kt/cdG) can be used compared to the conventional method. The generation of noise and vibration is extremely low.
第1図は、本発明に用いられる装置の一例を示す概要図
である。
1・・・多孔管、 2・・・外筒管3・・・蒸気室
、 4・・・蒸気人口5・・・蒸気出口、 6
・・・圧力調節弁7・・・温度コントローラー
8・・・ドレイントラップ
特許出願人 鐘淵化学工業株式会社
第1 図FIG. 1 is a schematic diagram showing an example of a device used in the present invention. 1... Porous pipe, 2... Outer cylinder pipe 3... Steam chamber, 4... Steam population 5... Steam outlet, 6
...Pressure control valve 7 ...Temperature controller 8 ...Drain trap Patent applicant Kanebuchi Chemical Industry Co., Ltd. Figure 1
Claims (1)
、管の外部から水蒸気を供給することを特徴とする醗酵
原料の蒸煮殺菌方法。1. A method for steaming and sterilizing fermentation raw materials, characterized by flowing the fermentation raw materials inside a porous tube with a pore diameter of 0.5 to 5 mm, and supplying steam from the outside of the tube.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63270321A JPH02116375A (en) | 1988-10-26 | 1988-10-26 | Disinfecting method for fermentation raw materials |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63270321A JPH02116375A (en) | 1988-10-26 | 1988-10-26 | Disinfecting method for fermentation raw materials |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02116375A true JPH02116375A (en) | 1990-05-01 |
| JPH0546821B2 JPH0546821B2 (en) | 1993-07-15 |
Family
ID=17484640
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63270321A Granted JPH02116375A (en) | 1988-10-26 | 1988-10-26 | Disinfecting method for fermentation raw materials |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02116375A (en) |
-
1988
- 1988-10-26 JP JP63270321A patent/JPH02116375A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0546821B2 (en) | 1993-07-15 |
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