JPS63123415A - Filter for filtering yeast - Google Patents
Filter for filtering yeastInfo
- Publication number
- JPS63123415A JPS63123415A JP61266648A JP26664886A JPS63123415A JP S63123415 A JPS63123415 A JP S63123415A JP 61266648 A JP61266648 A JP 61266648A JP 26664886 A JP26664886 A JP 26664886A JP S63123415 A JPS63123415 A JP S63123415A
- Authority
- JP
- Japan
- Prior art keywords
- yeast
- filter
- pore diameter
- average pore
- layer
- 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.)
- Pending
Links
- 240000004808 Saccharomyces cerevisiae Species 0.000 title claims abstract description 48
- 238000001914 filtration Methods 0.000 title claims abstract description 26
- 239000011148 porous material Substances 0.000 claims abstract description 29
- 102000004169 proteins and genes Human genes 0.000 claims abstract description 15
- 108090000623 proteins and genes Proteins 0.000 claims abstract description 15
- 239000000126 substance Substances 0.000 claims abstract description 9
- 239000010419 fine particle Substances 0.000 claims description 15
- 239000000084 colloidal system Substances 0.000 claims description 14
- 239000007788 liquid Substances 0.000 claims description 8
- 239000002002 slurry Substances 0.000 claims description 6
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 abstract description 4
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 abstract description 4
- 239000000463 material Substances 0.000 abstract description 4
- 239000000919 ceramic Substances 0.000 abstract description 3
- 230000008929 regeneration Effects 0.000 abstract description 3
- 238000011069 regeneration method Methods 0.000 abstract description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 2
- 229910052799 carbon Inorganic materials 0.000 abstract description 2
- 229910052878 cordierite Inorganic materials 0.000 abstract description 2
- JSKIRARMQDRGJZ-UHFFFAOYSA-N dimagnesium dioxido-bis[(1-oxido-3-oxo-2,4,6,8,9-pentaoxa-1,3-disila-5,7-dialuminabicyclo[3.3.1]nonan-7-yl)oxy]silane Chemical compound [Mg++].[Mg++].[O-][Si]([O-])(O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2)O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2 JSKIRARMQDRGJZ-UHFFFAOYSA-N 0.000 abstract description 2
- KZHJGOXRZJKJNY-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Si]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O KZHJGOXRZJKJNY-UHFFFAOYSA-N 0.000 abstract description 2
- 229910003465 moissanite Inorganic materials 0.000 abstract description 2
- 229910052863 mullite Inorganic materials 0.000 abstract description 2
- 239000012466 permeate Substances 0.000 abstract description 2
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 abstract description 2
- 229910010271 silicon carbide Inorganic materials 0.000 abstract description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 abstract 2
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 239000000377 silicon dioxide Substances 0.000 abstract 1
- 239000000758 substrate Substances 0.000 abstract 1
- 235000014680 Saccharomyces cerevisiae Nutrition 0.000 description 38
- 239000010410 layer Substances 0.000 description 31
- 238000011001 backwashing Methods 0.000 description 4
- 239000000706 filtrate Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 235000013405 beer Nutrition 0.000 description 2
- 230000033228 biological regulation Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 239000012752 auxiliary agent Substances 0.000 description 1
- 235000013361 beverage Nutrition 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000002356 single layer Substances 0.000 description 1
- 235000013555 soy sauce Nutrition 0.000 description 1
- 239000011550 stock solution Substances 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 235000021419 vinegar Nutrition 0.000 description 1
- 239000000052 vinegar Substances 0.000 description 1
- 235000014101 wine Nutrition 0.000 description 1
- -1 wire mesh Substances 0.000 description 1
Landscapes
- Apparatus Associated With Microorganisms And Enzymes (AREA)
- Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
- Filtering Materials (AREA)
Abstract
Description
【発明の詳細な説明】
（産業上の利用分野）
本発明は、ビール、ワインなどの飲料あるいはしょう油
９食酢などの食品等を生産するに際し、液中に含まれる
酵母を完全に除去し味に関係する蛋白コロイド物質だけ
を直接濾過で透過させるのに使用する酵母除去フィルタ
ーに関するものである。Detailed Description of the Invention (Industrial Application Field) The present invention completely removes yeast contained in the liquid when producing beverages such as beer and wine, or foods such as soy sauce and vinegar. This invention relates to a yeast removal filter that is used to directly filter out only relevant protein colloid substances.
（従来の技術）
従来、酵母のみを除去し蛋白コロイド物質だけを透過さ
せるための直接濾過方法としては、濾布。(Prior Art) Conventionally, a filter cloth has been used as a direct filtration method to remove only yeast and allow only protein colloid substances to pass through.
濾紙、有機膜等を用いるだけのノンプレコート濾過法お
よび濾布、濾紙、有機膜、金網、セラミックフィルター
に濾過助剤を担持させて用いるプレコート濾過法が知ら
れている。A non-precoat filtration method using only filter paper, an organic membrane, etc. and a precoat filtration method using a filter cloth, filter paper, organic membrane, wire mesh, or ceramic filter carrying a filter aid are known.
（発明が解決しようとする問題点）
しかしながら、上述した従来の濾過法においては以下の
ような種々の欠点があった。すなわち、ノンプレコート
濾過においては、濾過機構が内部濾過のため目詰まりが
速く濾過速度の低下が大きいと共に目詰まり後は逆洗再
生がほとんど不可能であるばかりでなく、濾過材の強度
が弱く酵母が流出する危険があった。また、プレコート
濾過においては、濾過助剤を用いるといえども濾過機構
が内部濾過であるため、蛋白コロイド物質も濾過材によ
り捕捉されてしまう欠点があった。さらに、濾過助剤層
が振動などに対してはく離しやすく酵母の流出の危険が
あると共に、濾過助剤のランニングコストが高くなる欠
点もあった。(Problems to be Solved by the Invention) However, the above-mentioned conventional filtration methods have various drawbacks as described below. In other words, in non-precoat filtration, since the filtration mechanism is an internal filtration, clogging occurs quickly and the filtration rate decreases significantly.After clogging, backwashing is almost impossible, and the strength of the filter material is weak and yeast There was a risk of leakage. Furthermore, in precoat filtration, even though a filter aid is used, the filtration mechanism is an internal filtration, so there is a drawback that protein colloid substances are also captured by the filter material. Furthermore, the filter aid layer tends to peel off due to vibrations, etc., posing a risk of yeast leakage, and the running cost of the filter aid increases.
本発明の目的は上述した不具合を解消して、濾過すべき
液中に含まれる酵母のみを完全に除去し、蛋白コロイド
物質だけを直接濾過で透過させるのに好適な酵母除去フ
ィルターを提供しようとするものである。The purpose of the present invention is to solve the above-mentioned problems and provide a yeast removal filter suitable for completely removing only the yeast contained in the liquid to be filtered and allowing only protein colloid substances to pass through by direct filtration. It is something to do.
（問題点を解決するための手段）
本発明の酵母除去フィルターは、濾過部材として多孔質
フィルターを使用して蛋白コロイド物質と酵母を含むス
ラリー液中の酵母を除去する酵母濾過フィルターにおい
て、前記多孔質フィルターの細粒層の平均細孔径が２μ
ｍ以上１０μｍ以下で、細粒層の層厚がその平均細孔径
の１０倍以上であることを特徴とするものである。(Means for Solving the Problems) The yeast removal filter of the present invention uses a porous filter as a filtration member to remove yeast from a slurry containing a protein colloid substance and yeast. The average pore diameter of the fine particle layer of the quality filter is 2μ
m or more and 10 μm or less, and the thickness of the fine grain layer is 10 times or more the average pore diameter.
（作 用）
上述した構成において、所定の平均細孔径と層厚を有す
る細粒層により、濾過すべき液中のサブミクロンオーダ
ーの蛋白コロイド物質のみを透過させて、数μｍ以上の
酵母（例えばビール酵母３〜１０μｍ）のみを完全に除
去することができる。また、助剤を使用していないため
、逆洗再生も容易に行なうことができる。(Function) In the above-mentioned configuration, the fine particle layer having a predetermined average pore diameter and layer thickness allows only submicron-order protein colloid substances in the liquid to be filtered to permeate, and yeasts of several μm or more (e.g. Only brewer's yeast (3-10 μm) can be completely removed. Furthermore, since no auxiliary agent is used, backwashing and regeneration can be performed easily.
なお、本発明において細粒層の平均細孔径を２〜１０μ
ｍと限定した理由は、後述する細粒層の平均細孔径に対
する濾過速度および濾液中の酵母数を示す第１表から明
らかなように、細粒層の平均細孔径が２μ所未満である
と濾過速度が極端に悪化すると共に、１０μｍを超える
と濾液中に酵母が流出するためである。なお、この平均
細孔径は５〜１０μｍであるとさらに好ましい。In addition, in the present invention, the average pore diameter of the fine grain layer is 2 to 10 μm.
The reason why it is limited to m is that, as is clear from Table 1 which shows the filtration rate and the number of yeast in the filtrate with respect to the average pore diameter of the fine grain layer, which will be described later, if the average pore diameter of the fine grain layer is less than 2μ, This is because the filtration rate becomes extremely poor and yeast flows out into the filtrate if the diameter exceeds 10 μm. In addition, this average pore diameter is more preferably 5 to 10 μm.
また、細粒層の層厚については同じく後述する第１表か
ら、層厚が平均細孔径の大きさの１０倍以下の薄い場合
には酵母が流出し好ましくないため平均細孔径の１０倍
以上と規定したが、あまり厚すぎると酵母は流出しない
がフィルター圧損が大きくなるため、１５〜５００倍が
好ましい。Regarding the thickness of the fine grain layer, from Table 1, which will also be described later, if the layer thickness is less than 10 times the average pore diameter, yeast will flow out, which is undesirable, so it is more than 10 times the average pore diameter. However, if it is too thick, the yeast will not flow out, but the filter pressure loss will increase, so it is preferably 15 to 500 times.
（実施例）
第１図（ａ）、 （ｂｌはそれぞれ本発明の酵母濾過フ
ィルターの一実施例を示す部分断面図で、第１図（ａ）
は細粒層ｌのみの単層構造の例を、また第１図中）は細
粒層１と支持層２との二層構造の例を示している。これ
らの酵母濾過フィルターにおいては、細粒層１の平均細
孔径は２〜１０μｍ、好ましくは５〜１０μｍとすると
ともに、その層厚は平均細孔径の１０倍以上、好ましく
は１５〜５００倍となるように、従来公知の方法で作製
している。また、支持Ｎ２の平均細孔径は細粒層の平均
細孔径よりも大きい平均細孔径であればよいが、本実施
例では５〜２００μｍ５好ましくは１０〜１００μｍと
なるよう構成している。また、第１図（ｂｌに示す二層
構造のフィルターにおける細粒層１はフィルターの内側
または外側のどちらか一方に設けられていればよい。細
粒Ｎ１および支持層２の材質としては、シリカ、アルミ
ナ、シリカ−アルミナ、ムライト。(Example) Fig. 1(a) and (bl are partial cross-sectional views showing an example of the yeast filtration filter of the present invention, respectively; Fig. 1(a)
1 shows an example of a single-layer structure with only a fine-grain layer 1, and FIG. 1) shows an example of a two-layer structure with a fine-grain layer 1 and a support layer 2. In these yeast filtration filters, the average pore diameter of the fine particle layer 1 is 2 to 10 μm, preferably 5 to 10 μm, and the layer thickness is 10 times or more, preferably 15 to 500 times the average pore diameter. It is manufactured using a conventionally known method. Further, the average pore diameter of the support N2 may be larger than the average pore diameter of the fine grain layer, but in this example, it is configured to be 5 to 200 μm, preferably 10 to 100 μm. In addition, the fine grain layer 1 in the two-layer structure filter shown in FIG. 1 (bl) may be provided on either the inside or outside of the filter. , alumina, silica-alumina, mullite.
ジルコニア、カーボン、コージェライト、 ＳｉＣ等の
セラミックスが好適であるが、これに限定されるもので
はなく本発明で限定した平均細孔径の条件を達成できる
ものであれば例えば焼結金属等も使用できることはいう
までもない。Ceramics such as zirconia, carbon, cordierite, and SiC are suitable, but the material is not limited thereto, and sintered metals can also be used as long as they can achieve the average pore diameter conditions defined in the present invention. Needless to say.
第２図は上述した二層構造の酵母除去フィルターのうち
内側コート品を使用して直接濾過を行なう方法を説明す
るための線図である。細粒層１１と支持ＪＷ１２とから
構成される本発明の酵母除去フィルターに供給された蛋
白コロイド１３と酵母１４とを含むスラリー液は、２〜
５ ｍ／ＨＲの速度で除去フィルターを通過する。これ
により、蛋白コロイド１３だけが酵母除去フィルターを
通り抜けて濾過液となると共に、酵母１４は酵母除去フ
ィルターの細粒層１１を通り抜けないため細粒層１１の
表面に堆積して、スラリー液を濾過することができる。FIG. 2 is a diagram for explaining a method of performing direct filtration using the inner coated product of the above-mentioned two-layered yeast removal filter. The slurry liquid containing the protein colloid 13 and yeast 14 supplied to the yeast removal filter of the present invention, which is composed of the fine particle layer 11 and the support JW 12, is
Pass through the removal filter at a speed of 5 m/HR. As a result, only the protein colloid 13 passes through the yeast removal filter and becomes the filtrate, and the yeast 14 does not pass through the fine particle layer 11 of the yeast removal filter, so it is deposited on the surface of the fine particle layer 11, and the slurry liquid is filtered. can do.
また、逆洗再生時には、スラリー液の流れを逆にして逆
洗用の液体を流せば節単に堆積物等を除去することがで
きる。Furthermore, during backwashing and regeneration, deposits and the like can be easily removed by reversing the flow of the slurry liquid and flowing the backwashing liquid.
以下、実際の例について説明する。An actual example will be explained below.
尖施炎
第１図（ｂ）に示す本発明の二層構造の酵母除去フィル
ターを使用して、酵母濃度１００個／ｃｃの生ビール原
液を、入口圧力１ ｋｇ／ｃｍ”、濾過速度３ ｍ／Ｈ
Ｒの定速濾過を温度２０℃で実施して、細粒層の平均細
孔径および厚さに対する濾液中の酵母および蛋白コロイ
ド除去率とフィルター圧損ΔＰを測定した。なお、この
ときの酵母除去フィルターとしては内側に細粒層が存在
する内側コート品を使用した。結果を第１表に示す。Using the two-layered yeast removal filter of the present invention shown in Figure 1(b), a draft beer stock solution with a yeast concentration of 100 cells/cc was filtered at an inlet pressure of 1 kg/cm'' and a filtration speed of 3 m/cc. H
Constant rate filtration of R was carried out at a temperature of 20° C., and the removal rate of yeast and protein colloids in the filtrate and the filter pressure drop ΔP with respect to the average pore diameter and thickness of the fine particle layer were measured. In addition, as the yeast removal filter at this time, an inner-coated product with a fine particle layer present inside was used. The results are shown in Table 1.
第 １ 表
第１表の結果から、本発明範囲内の細粒層の平均細孔径
および厚さを有する酵母除去フィルターは、フィルター
圧損ΔＰが小さいとともに蛋白コロイドは透過し酵母の
みを１００％除去することが可能であり、本発明の目的
を達成できることがわかった。すなわち、細粒層の平均
細孔径が２〜１０μｍでかつその厚さが平均細孔径の１
０倍以上である酵母除去フィルターが、蛋白コロイドを
完全透過しかつ酵母のみを１００％除去することができ
た。Table 1 From the results shown in Table 1, a yeast removal filter having a fine particle layer with an average pore diameter and thickness within the range of the present invention has a small filter pressure drop ΔP, allows protein colloid to pass through, and removes only yeast by 100%. It has been found that this is possible and that the object of the present invention can be achieved. That is, the average pore diameter of the fine grain layer is 2 to 10 μm, and the thickness is 1 of the average pore diameter.
The yeast removal filter, which is 0 times or more, completely permeated the protein colloid and was able to remove 100% of only the yeast.
なお、細粒層の厚さは平均細孔径の１０倍以上であれば
酵母のみを完全に除去することが可能であるが、厚さが
厚くなるほどフィルター圧損も大きくなるため好ましく
は５００倍程度までの厚さで使用する必要がある。If the thickness of the fine particle layer is at least 10 times the average pore diameter, it is possible to completely remove only yeast, but the thicker the thickness, the greater the filter pressure loss, so it is preferably about 500 times the average pore diameter. It must be used at a thickness of
（発明の効果）
以上詳細に説明したところから明らかなように、本発明
の酵母除去フィルターによれば、細粒層の平均細孔径の
大きさの規定と層厚の規定との相乗効果により、蛋白コ
ロイド物質を透過させ酵母のみをスラリー液中から完全
に除去することができ、圧力損失も小さく濾材の再生洗
浄が可能でランニングコストが廉価でかつ高品質の製品
を得ることができる。(Effects of the Invention) As is clear from the detailed explanation above, according to the yeast removal filter of the present invention, due to the synergistic effect of the regulation of the average pore diameter of the fine particle layer and the regulation of the layer thickness, Only yeast can be completely removed from the slurry by passing through protein colloid substances, pressure loss is small, filter media can be regenerated and washed, and running costs are low and high quality products can be obtained.
第１図（ａ）、 （ｂ）はそれぞれ本発明の酵母濾過フ
ィルターの一実施例を示す部分断面図、
第２図は第１図（ｂ）に示す二層構造の酵母除去フィル
ターを使用して直接濾過を行なう方法を説明するための
線図である。
１．１１・・・細粒層 ２，１２・・・支持層１
３・・・蛋白コロイド １４・・・酵母第１図
（ａ）
（ｂ）Figures 1(a) and (b) are partial cross-sectional views showing one embodiment of the yeast filtration filter of the present invention, and Figure 2 is a partial cross-sectional view showing an embodiment of the yeast filter of the present invention. FIG. 2 is a diagram for explaining a method of directly performing filtration. 1.11...Fine grain layer 2,12...Support layer 1
3... Protein colloid 14... Yeast Figure 1 (a) (b)
Claims (1)
ロイド物質と酵母を含むスラリー液中の酵母を除去する
酵母濾過フィルターにおいて、前記多孔質フィルターの
細粒層の平均細孔径が２μｍ以上１０μｍ以下で、細粒
層の層厚がその平均細孔径の１０倍以上であることを特
徴とする酵母除去フィルター。 ２、前記多孔質フィルターが、細粒層と細粒層の平均細
孔径よりも大きい平均細孔径を有する支持層との二層構
造よりなる特許請求の範囲第１項記載の酵母除去フィル
ター。[Scope of Claims] 1. In a yeast filtration filter that uses a porous filter as a filtration member to remove yeast from a slurry liquid containing a protein colloid substance and yeast, an average pore diameter of a fine particle layer of the porous filter; is 2 μm or more and 10 μm or less, and the layer thickness of the fine particle layer is 10 times or more the average pore diameter. 2. The yeast removal filter according to claim 1, wherein the porous filter has a two-layer structure including a fine particle layer and a support layer having an average pore diameter larger than the average pore diameter of the fine particle layer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61266648A JPS63123415A (en) | 1986-11-11 | 1986-11-11 | Filter for filtering yeast |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61266648A JPS63123415A (en) | 1986-11-11 | 1986-11-11 | Filter for filtering yeast |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS63123415A true JPS63123415A (en) | 1988-05-27 |
Family
ID=17433750
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61266648A Pending JPS63123415A (en) | 1986-11-11 | 1986-11-11 | Filter for filtering yeast |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS63123415A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02180608A (en) * | 1989-01-06 | 1990-07-13 | Toshiba Corp | Apparatus for treating water produced in cask for use in transportation of used fuel |
| JPH0523194A (en) * | 1991-07-19 | 1993-02-02 | Hitachi Plant Eng & Constr Co Ltd | Method for separating protein by membrane |
| JPH0562930U (en) * | 1992-01-31 | 1993-08-20 | 日本電気ホームエレクトロニクス株式会社 | Switch device |
-
1986
- 1986-11-11 JP JP61266648A patent/JPS63123415A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02180608A (en) * | 1989-01-06 | 1990-07-13 | Toshiba Corp | Apparatus for treating water produced in cask for use in transportation of used fuel |
| JPH0523194A (en) * | 1991-07-19 | 1993-02-02 | Hitachi Plant Eng & Constr Co Ltd | Method for separating protein by membrane |
| JPH0562930U (en) * | 1992-01-31 | 1993-08-20 | 日本電気ホームエレクトロニクス株式会社 | Switch device |
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