JP2004065230A - Method for destroying cell wall - Google Patents

Method for destroying cell wall Download PDF

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Publication number
JP2004065230A
JP2004065230A JP2002266127A JP2002266127A JP2004065230A JP 2004065230 A JP2004065230 A JP 2004065230A JP 2002266127 A JP2002266127 A JP 2002266127A JP 2002266127 A JP2002266127 A JP 2002266127A JP 2004065230 A JP2004065230 A JP 2004065230A
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Japan
Prior art keywords
cell wall
vibration mill
mill
vibration
ball
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JP2002266127A
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Japanese (ja)
Inventor
Hideaki Kiyokawa
清川 英明
Shinkichi Ito
伊藤 新吉
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CHUO KAKOKI
Chuo Kakohki Coltd
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CHUO KAKOKI
Chuo Kakohki Coltd
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Priority to JP2002266127A priority Critical patent/JP2004065230A/en
Publication of JP2004065230A publication Critical patent/JP2004065230A/en
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Abstract

<P>PROBLEM TO BE SOLVED: To enhance digestive efficiency for organisms by crushing cells to destroy cell walls and helping digestion of the organisms. <P>SOLUTION: A treatment for crushing cells to destroy cell walls of cell-containing food, feed and the like is carried out by using a vibration mill. As a powdery medium in the vibration mill, ceramics such asalumina, zirconia or the like can be used, but usually steel (carbon steel) balls, especially stainless steel balls having 1-20 mm (preferably 2-10 mm) particle size (diameter) and ≥3 specific gravity are preferably used. By the method, the cell walls (protective membranes) are surely destroyed, and as for steel balls, high gravity and high hardness balls can be applied; thereby higher crushing performance can be expected. <P>COPYRIGHT: (C)2004,JPO

Description

【0001】
【技術分野】
本発明は、細胞を粉砕処理することにより細胞壁が破壊され、生物内における消化を助けることにより、生き物に対する消化効率を上げることができ、少量により従来の効果を満足させる。
【0002】
ここでは、主として食品及び飼料中の細胞の細胞壁の破壊を例にとり説明するが、これに限られるものではない。例えば、微生物工業(発酵工場:パン・醸造工業等)で発生する微生物等にも本発明は適用できるものである。
【0003】
【背景技術】
従来は、消化効率を上げるために細胞壁を振動ミルを使用して行う技術はない。汚泥中の細胞の細胞壁を破壊して、バクテリアに食べやすくする技術は、特願2001−17338に記した通りである。主に廃棄物スラリー中の細胞である。
【0004】
ここで「細胞壁」とは、「植物細胞や微生物の細胞の外側をとりかこんでいる厚さ数μmの構造、その内側にある細胞膜とは区別される。動物細胞には存在せず、植物細胞でも、鞭毛類や精子、遊走子、粘菌の変形体には見られない。」のことである(「岩波理化学辞典第5版」(1998)岩波書店p.491)。
【0005】
本発明は、細胞を含む食品及び飼料を人間、または生き物が食べるが、細胞壁が固く、消化されることが少ない。従って、新規で有用な従来に無い消化を得ることを提供することを目的とする。
【0006】
【発明の開示】
本発明は、上記課題を下記構成により解決するものである。
【0007】
細胞を含む食品、飼料において、より消化効率を上げる方法として、細胞破壊処理を振動ミルで行うことを特徴とする。
【0008】
上記において振動ミルにおける粉体媒体としては、通常、粉砕媒体として、粒径(直径):1〜20mm(望ましくは2〜10mm)、比重:3以上(望ましくは7以上)のボールを使用することが望ましい。これらの要件を満たすことにより、微生物の細胞壁(保護膜)を確実に粉砕することができる。また、スチールは、比重が高く、硬さも高いものを選択でき、より高い粉砕能力が期待できる。
【0009】
前記振動ミルとして連続タイプを使用することが細胞壁の破壊処理を連続的かつ高能率でできて望ましい。
【0010】
湿式粉砕する場合、振動ミルの運転条件を、振幅5〜40mm、振動数10〜30Hzとすることが、細胞の破壊効率を高めることができる。
【発明を実施するための最良の形態】
次に、本発明を実施するための最良の形態について、細胞壁の破壊処理に本発明を適用した場合を例にとり説明をする。
【0011】
ここで、細胞を含む食品及び飼料の細胞壁とは、細菌(バクテリア)、藻類、菌類、原生動物(繊毛虫類等)、その他動物(顕微鏡的なものから肉眼的なものまで)に含まれる生きた細胞の細胞壁の概念である。
【0012】
細胞壁の破壊装置として、振動ミルを使用する。ここで、振動ミルとは、「円筒ないしトラフ状の容器中にボール(ないしロッドまたはペブ)を入れ、これをスプリング上において外から偏心作用を加えて加振をし、ボール等の細かい振動挙動によって粉砕を進める粉砕機」のことである(「改訂四版化学工学便覧」(昭53−10−25)丸善p.1288)。
【0013】
振動ミルとしては通常円形振動タイプを使用するが螺旋旋動振動タイプであってもよい。振動ミルは回転式ボールミル(攪拌式ボールミルも同様)と異なり、その粉砕力は、回転式ボールミルを1G(重力加速度)としたとき、振動ミルは6〜30Gと大きく、粉砕能力は10〜20倍にも達するものである。
【0014】
具体的には、中央化工機(株)から「CD型」、「MB型」、「FV型」、「FVR型」の各シリーズで製造販売されている振動ミルを好適に使用できる。これらの振動ミルは原則的に、振動方式が機械式で振動源左右一対、または軸心配置方式であるが、振動源片側配置タイプさらには振動方式も、電磁石方式、振動モータ方式等任意である。これらの内で、機械振動方式で連続タイプのものが処理生産性(処理能力・効率)の見地から望ましい。特に、図2に示すような「CD型振動ミル」で、上下二筒駆動方式連続タイプが望ましいが、破壊条件によっては、上下二筒が一筒で行うことがよりベターである。また、連続式にこだわることでなく、バッチ式が使われることも多い。処理能力が大きくかつ微粉砕化が容易であり、連続的に各粉砕筒24の排出口25A、25Bに配されたスリットを介して粉砕媒体(ボール)と被破壊物の分離が容易なためである。
【0015】
この「CD型振動ミル」は、架台18上に圧縮コイルばね(スプリング)20で4点支持された受け台(支持板)22を介して上下にかつ着脱可能に二筒の粉砕筒24が配されている。そして図示しないモータ(電動機)で撓み、継ぎ手を介して駆動させる4個(2個ずつ剛軸直結)の偏心振動源(バランスウェイト)26がスプリング20支持部位に対応させて、受け台22に配されている。なお、28及び30は、それぞれ被破壊処理物投入口接続チューブ及び被破壊処理物排出口接続チューブである。なお、上記において、圧縮コイルばね(スプリング20)の代わりに、空気ばね、コイルばねをゴムで被覆したものも使用可能である。
【0016】
そして、使用する粉砕媒体は、ボール径(直径):1〜20mm、比重:3以上、望ましくは直径:1.5〜15mm、比重:5以上、さらに望ましくは直径:2〜10mm、比重:7以上とする。粒径及び比重が小さすぎると、振動による衝撃・摩擦粉砕が困難となり(細胞壁を粉砕するのに必要なGを得がたい:図1参照)、また、粒径が大きすぎると数μm〜数十μmの微生物の破壊効率が低下する。比重は衝撃力の見地から大きい方が望ましいが、あまり大きすぎると、破壊動力として大出力のものが要求されるため、通常、15以下とする。
【0017】
しかし、本発明では特願2001−17338に記載した湿式攪拌式ミルにおける常識を打ち破ったものである。すなわち、振動ミルを使用すれば十分に上記の数μm〜数十μmの微生物であっても、細胞壁の破壊が可能であることを発見して、本発明に想到した。
【0018】
上記要件を満たす粉砕媒体(ボール)としては、アルミナ、ジルコニア等のセラミックス製であってもよいが、通常、スチール(炭素鋼)製、特にステンレス製のものが望ましい。比重及び硬度として最適なものを使用でき、さらに、ステンレス製の場合は、耐腐食性も有しメンテナンス上も有利である。なお、各粉砕媒体形成材の各比重(密度:g・cm−3)はアルミナ(酸化アルミニウム):4.0、ジルコニア(酸化ジルコニウム(IV)):5.49、鉄:7.874である(大木他編「化学辞典」(1994)東京化学同人)。
【0019】
次に、上記振動ミルを用いての細胞壁破壊の運転条件は、湿式に限ったことでなく、乾燥物の状態で乾式にて破壊することも可能であるが、ここでは下記のごとく湿式の説明とする。
【0020】
振動ミルに投入する被破壊物のスラリー濃度(乾燥固形分濃度:質量%)は、特に限定されないが、通常、3%以上とする。あまり薄すぎては、粉砕効率が低下する。被破壊物のスラリー濃度は、高い方が破壊効率の見地からは有利である。
【0021】
また、被破壊物の滞留時間は、濃度・種類、加振エネルギー等により異なるが、通常、10秒以上とする。滞留時間が短すぎては、細胞壁を生分解消化率の格段の向上に十分に寄与可能な破砕状態を得がたく、生分解率(消化率)の格段の向上を期待しがたい。なお、滞留時間は上記破砕状態を達成できれば、処理効率の見地からは可及的に短い方が望ましい。
【0022】
このときの振動ミルの振幅a及び振動数νは、通常、a=5〜40mm、ν=10〜30Hzの範囲で要求される衝撃・摩擦力に応じて適宜選定する。振幅に比例して、振動数の自乗に比例してそれぞれ衝撃Gは増大するが、モータその他、継ぎ手部等に対する負荷が増大して設計が困難となる。
【0023】
上記において、各粉砕媒体を被破壊物と分離するためのスリット間隙は、ボール径D−(0.2〜2)mm、望ましくはD−(0.5〜1)mmとする。スリット間隙がボール径に比して小さすぎても、大きすぎても、分離効率が低下する。すなわち、ボール径がスリット間隙に近いと、ボール径のばらつきを吸収できず、スリットからボールが落下するおそれがあり、逆にボール径に比してスリット間隙が狭すぎると、相対的に被破壊物の排出効率が低下するためである。
【0024】
【発明の作用・効果】
本発明のごとく、被破壊物を、振動ミルに投入して破壊後、生分解処理(生化学的処理)を行った場合、図2に示すごとく、細胞壁が破砕されているため、微生物等により消化されやすくなり、その消化率は格段に向上するものである。特に、湿式媒体攪拌式ミルのごとく摩擦力のみによる細胞壁の破砕でなく、振動ミルの場合、摩擦力とともに衝撃力も細胞壁の破壊に寄与するため、より効率の高い破壊が期待できる。
【0025】
そして、被破壊物と粉砕媒体(ボール)の分離も、ボールとして大きな径のものでも使用でき、相対的に排出口のスリット間隙も大きなものとすることができて、従来の湿式媒体攪拌式ミルを使用する場合に比して、分離効率、特に連続運転する場合の処理効率も増大させることができる。
【0026】
ボール径の大きな粉砕媒体を使用できるため、相対的に比重の小さなものでも、細胞壁の破砕が可能な衝撃を得ることができ、投入被破壊物の多様性に対応できるとともに、粉砕態様(粉砕媒体も含め)の多様化も可能となる。
【0027】
【試験例】
以下、本発明の効果を確認するために行った試験例について説明をする。
【0028】
試験機としては、中央化工機(株)製の下記仕様の「振動ミルEX−20型」のテスト機を使用した。
【0029】
粉砕筒:200φ×400L(一筒、冷却ジャケット付き、ステンレス製、全内容量約12L)
電動機:2.2kW×6p×2台
粉砕媒体及びその充填量:ステンレス製5mmφ、45kg
振動ミル振幅・振動数:ν=約30mm、ν=16Hz
上記仕様の振動ミルに、飼料のスラリー(スラリー濃度:7〜8%)を、原液のまま汚泥供給量4L/h、滞留時間3minの条件で連続投入して、スラリーの破壊処理を行った。
【0030】
その結果、破壊処理しない場合に比して、破壊された細胞壁によって、吸収(消化)率が格段に向上することが分かった。
【0031】
【産業上の利用の可能性】
本発明は、人間が「食している物」で微生物の作用により、消化・吸収を助けられている食物を湿式破壊処理することに大きな利用の可能性がある。
【0032】
さらには、必要により乾燥した食物を乾式破壊処理を行ってもよい。
【図面の簡単な説明】
【図1】本発明の振動ミルによる細胞壁が破壊されたモデル図である。
【図2】本発明の破壊処理方法における粉砕処理に適用する振動ミルの一例を示す正面図である。
[0001]
【Technical field】
INDUSTRIAL APPLICABILITY According to the present invention, cell walls are destroyed by crushing cells, and the digestion efficiency in living organisms can be increased by assisting digestion in living organisms.
[0002]
Here, description will be made mainly on an example of the destruction of cell walls of cells in food and feed, but the present invention is not limited to this. For example, the present invention can be applied to microorganisms and the like generated in the microbial industry (fermentation factory: bread and brewing industry).
[0003]
[Background Art]
Conventionally, there is no technique for performing cell wall using a vibrating mill to increase digestion efficiency. The technology for breaking down the cell wall of the cells in the sludge to make it easier for bacteria to eat is as described in Japanese Patent Application No. 2001-17338. Mainly cells in waste slurry.
[0004]
As used herein, the term “cell wall” refers to a structure having a thickness of several μm that surrounds the outside of a plant cell or a microbial cell, and is distinguished from a cell membrane inside the plant cell. However, it is not found in flagellates, sperm, zoospores, and slime mold variants. "(Iwanami Physical and Chemical Dictionary 5th Edition (1998) Iwanami Shoten p.491).
[0005]
According to the present invention, foods and feeds containing cells are eaten by humans or living creatures, but the cell walls are hard and are hardly digested. It is therefore an object to provide a new and useful unprecedented digestion.
[0006]
DISCLOSURE OF THE INVENTION
The present invention solves the above problems by the following configurations.
[0007]
In foods and feeds containing cells, as a method for further improving digestion efficiency, cell destruction treatment is performed using a vibration mill.
[0008]
In the above, a ball having a particle diameter (diameter) of 1 to 20 mm (preferably 2 to 10 mm) and a specific gravity of 3 or more (preferably 7 or more) is usually used as a pulverizing medium as a powder medium in the vibration mill. Is desirable. By satisfying these requirements, the cell wall (protective film) of the microorganism can be reliably crushed. Further, steel having high specific gravity and high hardness can be selected, and higher crushing ability can be expected.
[0009]
It is desirable to use a continuous type as the vibrating mill because the cell wall can be continuously and efficiently destroyed.
[0010]
In the case of wet pulverization, setting the operating conditions of the vibration mill to an amplitude of 5 to 40 mm and a frequency of 10 to 30 Hz can enhance the cell destruction efficiency.
BEST MODE FOR CARRYING OUT THE INVENTION
Next, the best mode for carrying out the present invention will be described by taking as an example a case where the present invention is applied to a cell wall destruction treatment.
[0011]
Here, the cell walls of food and feed containing cells are defined as living cells contained in bacteria (bacteria), algae, fungi, protozoa (ciliates, etc.), and other animals (from microscopic to macroscopic). This is the concept of the cell wall of a cell.
[0012]
A vibrating mill is used as a cell wall breaking device. Here, the vibrating mill refers to "a ball (or rod or peb) is placed in a cylindrical or trough-shaped container, and this is vibrated by applying an eccentric action from the outside on a spring, and the fine vibration of the ball or the like is performed. "Pulverizer that advances pulverization by behavior"("Revised 4th Edition Chemical Engineering Handbook" (Showa 53-10-25) Maruzen p. 1288).
[0013]
As the vibration mill, a circular vibration type is usually used, but a spiral oscillating vibration type may be used. The vibrating mill is different from a rotary ball mill (the same applies to a stirring ball mill), and its crushing power is as large as 6 to 30 G when the rotary ball mill is 1 G (gravitational acceleration), and the crushing power is 10 to 20 times. Also reach.
[0014]
Specifically, vibration mills manufactured and sold by Chuo Kakoki Co., Ltd. in each series of "CD type", "MB type", "FV type", and "FVR type" can be suitably used. In principle, these vibration mills have a mechanical vibration system and a pair of left and right vibration sources, or a shaft center arrangement system. However, the vibration source one side arrangement type and the vibration system are also optional such as an electromagnet system and a vibration motor system. . Among these, a continuous type mechanical vibration method is desirable from the viewpoint of processing productivity (processing capacity and efficiency). In particular, a "CD-type vibration mill" as shown in FIG. 2 is preferably a two-cylinder drive type continuous type, but depending on the destruction condition, it is more preferable to perform the two-cylinder drive with one cylinder. In addition, a batch system is often used instead of a continuous system. This is because the processing capacity is large, the pulverization is easy, and the pulverizing medium (ball) and the object to be destroyed are easily separated through the slits arranged at the discharge ports 25A and 25B of each pulverizing cylinder 24 continuously. is there.
[0015]
In the "CD type vibration mill", two pulverizing cylinders 24 are vertically and detachably mounted on a mount 18 via a support (support plate) 22 supported at four points by compression coil springs (springs) 20. Have been. Four eccentric vibration sources (balance weights) 26 that are bent by a motor (not shown) and driven through joints (two rigid shafts are directly connected to the rigid shaft) are arranged on the cradle 22 in correspondence with the spring 20 support portions. Have been. Reference numerals 28 and 30 denote a destruction target connection port tube and a destruction target discharge port connection tube, respectively. In the above, instead of the compression coil spring (spring 20), an air spring or a coil spring covered with rubber can be used.
[0016]
The grinding medium used is a ball diameter (diameter): 1 to 20 mm, a specific gravity: 3 or more, preferably a diameter: 1.5 to 15 mm, a specific gravity: 5 or more, more preferably a diameter: 2 to 10 mm, and a specific gravity: 7 Above. If the particle size and specific gravity are too small, it becomes difficult to perform impact / friction pulverization by vibration (it is difficult to obtain G necessary for pulverizing the cell wall: see FIG. 1), and if the particle size is too large, several μm to several tens μm. Of microorganisms is reduced. It is desirable that the specific gravity be large from the viewpoint of the impact force, but if it is too large, a high output is required as the breaking power, so that the specific gravity is usually 15 or less.
[0017]
However, in the present invention, common sense in a wet stirring type mill described in Japanese Patent Application No. 2001-17338 is broken. In other words, the present inventors have found that the cell wall can be destroyed even with the above-mentioned microorganism having a size of several μm to several tens of μm by using a vibration mill, and reached the present invention.
[0018]
The pulverizing medium (ball) satisfying the above requirements may be made of ceramics such as alumina and zirconia, but usually is preferably made of steel (carbon steel), particularly stainless steel. Optimum specific gravity and hardness can be used, and in the case of stainless steel, it has corrosion resistance and is advantageous in maintenance. The specific gravity (density: g · cm −3 ) of each pulverization medium forming material is alumina (aluminum oxide): 4.0, zirconia (zirconium oxide (IV)): 5.49, and iron: 7.874. (Oki et al., “Chemical Dictionary” (1994) Tokyo Chemical Dojin).
[0019]
Next, the operating condition of cell wall destruction using the above-mentioned vibration mill is not limited to the wet type, and it is possible to destroy the cell type in a dry state in a dry state. And
[0020]
The slurry concentration (dry solid content: mass%) of the object to be broken into the vibrating mill is not particularly limited, but is usually 3% or more. If it is too thin, the crushing efficiency will decrease. The higher the slurry concentration of the object to be destroyed, the more advantageous from the viewpoint of the destruction efficiency.
[0021]
The residence time of the object to be destroyed varies depending on the concentration, type, excitation energy, and the like, but is usually 10 seconds or more. If the residence time is too short, it is difficult to obtain a crushed state in which the cell wall can sufficiently contribute to a marked improvement in the biodegradation and digestibility, and it is difficult to expect a marked improvement in the biodegradation rate (digestion rate). The residence time is desirably as short as possible from the viewpoint of processing efficiency, if the above-mentioned crushing state can be achieved.
[0022]
At this time, the amplitude a and the frequency ν of the vibrating mill are appropriately selected according to the impact / frictional force required in the range of a = 5 to 40 mm and ν = 10 to 30 Hz. The impact G increases in proportion to the amplitude and in proportion to the square of the frequency, but the load on the motor and other joints increases, making the design difficult.
[0023]
In the above description, the slit gap for separating each grinding medium from the object to be destroyed has a ball diameter of D- (0.2 to 2) mm, preferably D- (0.5 to 1) mm. If the slit gap is too small or too large compared to the ball diameter, the separation efficiency will decrease. That is, if the ball diameter is close to the slit gap, variations in the ball diameter cannot be absorbed, and the ball may fall from the slit. Conversely, if the slit gap is too narrow compared to the ball diameter, the ball is relatively damaged. This is because the efficiency of discharging the material is reduced.
[0024]
[Action and Effect of the Invention]
As in the present invention, when the object to be destroyed is put into a vibrating mill and destroyed, and then subjected to biodegradation treatment (biochemical treatment), as shown in FIG. It is easily digested, and its digestibility is significantly improved. In particular, in the case of a vibration mill, not only the frictional force but also the crushing of the cell wall as in the wet medium stirring type mill, the frictional force and the impact force also contribute to the destruction of the cell wall, so that more efficient destruction can be expected.
[0025]
Also, the separation of the object to be destroyed and the pulverizing medium (ball) can be performed using a ball having a large diameter, and the slit gap at the outlet can be relatively large. Separation efficiency, especially processing efficiency in continuous operation, can be increased as compared with the case where is used.
[0026]
Since it is possible to use a grinding medium having a large ball diameter, it is possible to obtain an impact capable of crushing the cell wall even with a relatively small specific gravity, and to cope with a variety of input destruction objects, and to perform a pulverization mode (pulverization medium). ) Can be diversified.
[0027]
[Test example]
Hereinafter, test examples performed to confirm the effects of the present invention will be described.
[0028]
As a test machine, a test machine of "vibration mill EX-20 type" manufactured by Chuo Kakoki Co., Ltd. having the following specifications was used.
[0029]
Crushing cylinder: 200φ × 400L (one cylinder, with cooling jacket, made of stainless steel, total content about 12L)
Electric motor: 2.2kW x 6p x 2 units Grinding media and filling amount: stainless steel 5mmφ, 45kg
Vibration mill amplitude / frequency: ν = about 30 mm, ν = 16 Hz
Feed slurry (slurry concentration: 7 to 8%) was continuously charged into the vibrating mill having the above specifications under the conditions of a sludge supply rate of 4 L / h and a residence time of 3 min as a stock solution to perform a destruction treatment of the slurry.
[0030]
As a result, it was found that the absorption (digestion) rate was significantly improved by the disrupted cell wall as compared with the case where the disruption treatment was not performed.
[0031]
[Possibility of industrial use]
INDUSTRIAL APPLICABILITY The present invention has great potential for wet destruction of food that has been assisted in digestion and absorption by the action of microorganisms on "food" by humans.
[0032]
Further, if necessary, dry food may be subjected to dry destruction treatment.
[Brief description of the drawings]
FIG. 1 is a model diagram in which a cell wall is broken by a vibration mill of the present invention.
FIG. 2 is a front view showing an example of a vibration mill applied to a pulverizing process in the destructive processing method of the present invention.

Claims (7)

細胞を含む食品及び飼料等の細胞壁を振動ミルで破壊することを特徴とする細胞壁の破壊方法。A method for breaking a cell wall, comprising breaking a cell wall of food and feed containing cells with a vibration mill. 前記振動ミルにおける粉砕媒体として、直径:1〜20mm、比重:3以上のボールを使用することを特徴とする請求項1記載の細胞壁の破壊方法。The method according to claim 1, wherein a ball having a diameter of 1 to 20 mm and a specific gravity of 3 or more is used as a grinding medium in the vibration mill. 前記振動ミルにおける粉砕媒体として、直径:2〜10mm、比重:7以上のボールを使用することを特徴とする請求項2記載の細胞壁の破壊方法。The method according to claim 2, wherein a ball having a diameter of 2 to 10 mm and a specific gravity of 7 or more is used as a grinding medium in the vibration mill. 前記振動ミルとして連続タイプを使用することを特徴とする請求項1、2または3記載の細胞壁の破壊方法。The method according to claim 1, 2 or 3, wherein a continuous type is used as the vibrating mill. 前記振動ミルとしてバッチタイプを使用することを特徴とする請求項1、2または3記載の細胞壁の破壊方法。4. The method according to claim 1, wherein a batch type is used as the vibration mill. 前記振動ミルの湿式粉砕における運転条件が、振幅5〜40mm、振動数10〜30Hzであることを特徴とする請求項4、または5記載の細胞壁の破壊方法。The method according to claim 4 or 5, wherein operating conditions in the wet milling of the vibration mill are an amplitude of 5 to 40 mm and a frequency of 10 to 30 Hz. 前記振動ミルの乾式粉砕における運転条件が振幅5〜40mm、振動数10〜30Hzであることを特徴とする。請求項4または5記載の細胞壁の破壊方法。The operating conditions in the dry milling of the vibration mill are an amplitude of 5 to 40 mm and a frequency of 10 to 30 Hz. The method for destroying a cell wall according to claim 4 or 5.
JP2002266127A 2002-08-07 2002-08-07 Method for destroying cell wall Pending JP2004065230A (en)

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0610288A (en) * 1992-06-24 1994-01-18 New Oji Paper Co Ltd Production of fine fibrous cellulose
JP2000316564A (en) * 1999-03-04 2000-11-21 Qiagen Gmbh Disintegration of biomaterial and apparatus therefor
WO2001060977A1 (en) * 2000-02-17 2001-08-23 Biochem Industrial Co., Ltd. Purple photosynthetic bacteria and health foods
JP2002017340A (en) * 2000-07-04 2002-01-22 Minoru Takizawa Flavored butyric acid bacterium powder, method for producing the same and material for food and preservative

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0610288A (en) * 1992-06-24 1994-01-18 New Oji Paper Co Ltd Production of fine fibrous cellulose
JP2000316564A (en) * 1999-03-04 2000-11-21 Qiagen Gmbh Disintegration of biomaterial and apparatus therefor
WO2001060977A1 (en) * 2000-02-17 2001-08-23 Biochem Industrial Co., Ltd. Purple photosynthetic bacteria and health foods
JP2002017340A (en) * 2000-07-04 2002-01-22 Minoru Takizawa Flavored butyric acid bacterium powder, method for producing the same and material for food and preservative

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