JPH08198616A - Silicon dioxide for stabilizing beer and its production - Google Patents

Silicon dioxide for stabilizing beer and its production

Info

Publication number
JPH08198616A
JPH08198616A JP7024745A JP2474595A JPH08198616A JP H08198616 A JPH08198616 A JP H08198616A JP 7024745 A JP7024745 A JP 7024745A JP 2474595 A JP2474595 A JP 2474595A JP H08198616 A JPH08198616 A JP H08198616A
Authority
JP
Japan
Prior art keywords
beer
silicon dioxide
stabilizing
water
acid
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
Application number
JP7024745A
Other languages
Japanese (ja)
Other versions
JP3460357B2 (en
Inventor
Ikuo Uno
幾雄 鵜野
Yasutaka Chikaki
康高 親木
Seiichi Horiuchi
誠一 堀内
Hiroaki Sumi
博明 角
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.)
Asahi Breweries Ltd
Shionogi and Co Ltd
Original Assignee
Asahi Breweries Ltd
Shionogi and 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 Breweries Ltd, Shionogi and Co Ltd filed Critical Asahi Breweries Ltd
Priority to JP02474595A priority Critical patent/JP3460357B2/en
Publication of JPH08198616A publication Critical patent/JPH08198616A/en
Application granted granted Critical
Publication of JP3460357B2 publication Critical patent/JP3460357B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE: To obtain silicon dioxide for stabilizing beer, which give excellent stabilizing effect without dajnaging the foam property of the beer. CONSTITUTION: Silicon dioxide for stabilizing the beer, which has 500-800m<2> /g specific surface area by BET method, shows pH8.0-9.3 in 5wt.% aq. suspension, is <=+4.8 in acid strength H0 and 0.8-1.2μmol/m<2> in acid quantity, is obtained by adding simultaneously sodium silicate and a mineral acid into a salt aq. solution under stirring to allow to react with each other at pH3.0-7.0 and 80 deg.C, adjusting the pH of the resulting silica suspension to 3.0-7.0, filtering, washing and dispersing again the resulting silica hydrogel into water and after adjusting the pH to 5.5-8.5, filtering, washing and drying.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、ビールの泡特性を損う
ことがなく、かつ、ビールの安定性向上(混濁防止)に
対して優れた性能を有するビールの安定化処理用二酸化
ケイ素及びその製造方法に関する。
BACKGROUND OF THE INVENTION The present invention relates to a silicon dioxide for stabilizing beer, which does not impair the foam characteristics of beer and has excellent performance for improving the stability of beer (preventing turbidity). The manufacturing method is related.

【0002】[0002]

【従来の技術及び発明が解決しようとする課題】コハク
色をした透明感のあるビールは、その香味や泡特性と共
にビールの商品価値を決める重要な要素となっている。
Amber-colored and transparent beer is an important factor that determines the commercial value of beer together with its flavor and foam characteristics.

【0003】製品化されたビールは、その後、日数と共
にビール中のタンパク質が凝集して徐々に透明度が下が
っていくが、特に、低温で長期に保管されたときには見
た目にもわかる程度に濁りが発生する場合があり、この
現象は寒冷混濁と呼ばれている。
The commercialized beer then gradually becomes less transparent as protein in the beer aggregates with the number of days. Especially, when it is stored at a low temperature for a long period of time, turbidity occurs to the extent that it can be seen visually. This phenomenon is called cold turbidity.

【0004】この混濁の原因としては、ビールの原料で
ある大麦やホップに由来するある種のタンパク質やポリ
フェノールなどのコロイド成分が、会合又は凝集して起
こると一般的に考えられている。
It is generally considered that the cause of this turbidity is that a certain protein or colloidal component such as polyphenol derived from barley or hop which is a raw material of beer is associated or aggregated.

【0005】従って、ビールの混濁を防止し、その安定
性を高めるためには、ビールの製造工程において、これ
ら混濁の原因となる成分を除去もしくは減少させること
が必要であり、この目的のために従来より二酸化ケイ素
(シリカゲル)が比較的安価で、ビールの香味や泡、そ
の他の品質への影響が少ないので広く使用されている。
Therefore, in order to prevent turbidity of beer and increase its stability, it is necessary to remove or reduce the components that cause turbidity in the process of producing beer. For this purpose, Silicon dioxide (silica gel) has been widely used since it is relatively inexpensive and has little influence on beer flavor, foam, and other qualities.

【0006】この二酸化ケイ素をビールの安定化処理剤
とすることについては、従来から種々の提案がある。
Various proposals have heretofore been made to use this silicon dioxide as a stabilizing treatment agent for beer.

【0007】例えば、英国特許第981715号には、
比表面積200〜600m2/g、細孔容積0.5〜
1.5ml/g、平均細孔径40〜180Å、5%水懸
濁液とした場合のpHが4.0〜8.0の物性を有する
二酸化ケイ素が、ビールの混濁防止(安定化)に優れた
効果を示すことが記載されている。
For example, British Patent No. 981715 discloses
Specific surface area 200 to 600 m 2 / g, pore volume 0.5 to
Silicon dioxide, which has the physical properties of 1.5 ml / g, average pore size 40 to 180Å and pH of 5% water suspension of 4.0 to 8.0, is excellent in preventing beer turbidity (stabilization). It is described that the above effect is exhibited.

【0008】また、特公平3−27483号公報には、
ビールの安定化処理に使用する比表面積530〜720
2/g、細孔容積0.9〜1.5ml/g、平均細孔
径50〜120Å及び含水量7〜25重量%(湿量基
準)で、かつ、5%水懸濁液とした場合のpHが6.0
〜8.0であることを特徴とする微細なビールの安定化
処理用含水シリカゲルが提案されている。更に、特開平
1−165363号公報には、ビールを吸着剤と接触さ
せてビールを安定化する方法において、低温熟成中のビ
ールに吸着剤として比表面積300〜700m2/g、
細孔容積1.0〜2.0ml/g、平均細孔径100〜
180Å、平均粒子径5〜20μの球状シリカゲルを添
加接触させた後濾過することを特徴とするビールの安定
化処理方法が提案され、特開平4−79876号公報に
は、BET法による比表面積が250乃至500m2
gの範囲で、かつ酸度関数H0で+1.5以下の酸強度
における固体酸酸量が零で、酸度関数H0で+4.8迄
の酸強度における固体酸酸量が0.01乃至0.40m
mol/gの範囲にあるシリカゲルの微粉末よりなるこ
とを特徴とするビール用安定化処理剤が提案されてい
る。
Further, Japanese Patent Publication No. 3-27483 discloses that
Specific surface area 530-720 used for stabilizing beer
m 2 / g, pore volume 0.9 to 1.5 ml / g, average pore diameter 50 to 120Å, water content 7 to 25% by weight (wet amount basis), and 5% water suspension PH of 6.0
A hydrous silica gel for stabilizing beer is proposed, which is characterized in that it is ˜8.0. Further, in JP-A-1-165363, in a method of stabilizing beer by contacting beer with an adsorbent, a specific surface area of 300 to 700 m 2 / g as an adsorbent for beer during low temperature aging,
Pore volume 1.0-2.0 ml / g, average pore size 100-
A method for stabilizing beer is proposed, which is characterized in that spherical silica gel having an average particle diameter of 5 to 20 μm is added and brought into contact with the mixture, followed by filtration. JP-A-4-79876 discloses a method for stabilizing a beer having a specific surface area by the BET method. 250 to 500 m 2 /
In the range of g, the acidity function H 0 has a solid acidity of 0 or less at an acid strength of +1.5 or less, and the acidity function H 0 has a solid acidity of 0.01 to 0 at an acid strength of up to +4.8. .40m
A stabilizing agent for beer characterized by comprising fine powder of silica gel in the range of mol / g has been proposed.

【0009】これらの提案は、主として二酸化ケイ素の
比表面積や、細孔径、細孔容積などの物理的構造を制御
し、ビール中の混濁に関与するタンパク質を選択的に吸
着、除去しようとするものであるが、ビール中に含まれ
るタンパク質には、上述したような混濁タンパク(ビー
ルの混濁に関与するタンパク質)と起泡タンパク(ビー
ルの泡特性に寄与するタンパク質)とがあり、混濁タン
パクはビールの安定性に悪影響を与えるのでこれを除去
する必要があるが、起泡タンパクはビールの泡持ち、泡
つきなどの泡特性を良好にし、これを除去してしまうと
ビール本来の特性を損うことになる。
These proposals are intended to selectively adsorb and remove proteins involved in turbidity in beer by mainly controlling the physical surface area of silicon dioxide and the physical structure such as pore diameter and pore volume. However, the proteins contained in beer include turbid proteins (proteins involved in beer turbidity) and foaming proteins (proteins that contribute to beer's foam characteristics) as described above, and turbid proteins are beer. Since it adversely affects the stability of beer, it is necessary to remove it, but foaming protein improves the beer's foam characteristics such as foam retention and stickiness, and if this is removed, the original characteristics of beer are impaired. It will be.

【0010】上記従来の提案は、起泡タンパクが混濁タ
ンパクとは分子量や物理的な大きさが相違するというこ
とから、混濁タンパクを除去する場合に起泡タンパクに
ついては十分な考慮を払っていないものであるが、しか
し実際には混濁タンパクと起泡タンパクとは単純にその
分子量や物理的な大きさだけで分別されるものではない
ので、かなり厳密に二酸化ケイ素の細孔構造を制御して
も起泡タンパクの一部も吸着除去され、泡持ち、泡つき
などの泡特性も低下するという問題がある。
The above-mentioned conventional proposals do not give sufficient consideration to the foaming protein when removing the cloudy protein, because the foaming protein differs from the cloudy protein in molecular weight and physical size. However, in reality, cloudy proteins and foaming proteins are not simply separated by their molecular weight and physical size, so controlling the pore structure of silicon dioxide fairly strictly. Also, a part of the foaming protein is adsorbed and removed, and there is a problem that foam characteristics such as foam retention and foaming are deteriorated.

【0011】本発明は、上記事情に鑑みなされたもの
で、ビールの泡特性を損うことなくビールを安定化処理
して、泡持ち、泡つきの良好なかつ安定性の高いビール
を得ることができるビールの安定化処理用二酸化ケイ素
及びその製造方法を提供することを目的とする。
The present invention has been made in view of the above circumstances, and it is possible to obtain a beer having good foam retention and foaming and high stability by stabilizing the beer without impairing the foam characteristics of the beer. An object of the present invention is to provide silicon dioxide for stabilizing beer and a method for producing the same.

【0012】[0012]

【課題を解決するための手段及び作用】本発明者らは、
上記目的を達成するため鋭意検討を行った結果、二酸化
ケイ素として、BET法による比表面積が500〜80
0m2/g、5重量%の濃度に水に懸濁させたときの懸
濁液pHが8.0〜9.3、酸強度H0が+4.8以下
の酸量が0.8〜1.2μmol/m2のものをビール
の安定化処理に使用することにより、長期保存後の混濁
が効果的に防止されて安定性が高く、しかも泡持ち、泡
つきが良好でビールの泡特性が維持されたビールを得る
ことができることを知見した。
Means and Action for Solving the Problems The present inventors have
As a result of earnest studies to achieve the above object, as a result of silicon dioxide, the specific surface area by the BET method is 500 to 80.
When suspended in water at a concentration of 0 m 2 / g, 5% by weight, the suspension pH is 8.0 to 9.3, the acid strength H 0 is +4.8 or less, and the acid amount is 0.8 to 1 By using 2 μmol / m 2 for stabilizing beer, turbidity after long-term storage is effectively prevented, stability is high, and foam retention and foaming are good and beer foam characteristics are improved. It was found that sustained beer could be obtained.

【0013】またこの場合、塩類水溶液中にケイ酸ナト
リウムと鉱酸とを撹拌しながら同時に加えて反応を行
い、二酸化ケイ素を得るに際し、反応pHを3.0〜
7.0、反応温度を80℃以下とすること、更に得られ
たシリカ懸濁液につき、まずpH3.0〜7.0に調整
し、次いで濾過、水洗してシリカハイドロゲルを得ると
共に、このシリカハイドロゲルを水に再分散させ、その
pHを5.5〜8.5に調整するという二段階pH調整
を行うことにより、上記のようなビールの泡特性を損う
ことがなく、かつ、ビールの安定性向上(混濁防止)に
対して優れた性能を有する二酸化ケイ素を得ることがで
きることを見い出し、本発明をなすに至ったものであ
る。
Further, in this case, sodium silicate and mineral acid are simultaneously added to the aqueous solution of salt with stirring to carry out the reaction to obtain silicon dioxide.
7.0, the reaction temperature is set to 80 ° C. or lower, and the obtained silica suspension is first adjusted to pH 3.0 to 7.0, and then filtered and washed with water to obtain silica hydrogel. By redispersing the silica hydrogel in water and adjusting the pH of the silica hydrogel to 5.5 to 8.5, two-step pH adjustment is performed without impairing the foam characteristics of beer as described above, and The present invention has been completed by finding that silicon dioxide having excellent performance for improving the stability of beer (preventing turbidity) can be obtained.

【0014】従って、本発明は、(1)BET法による
比表面積が500〜800m2/gであり、5重量%の
水懸濁液としたときのpHが8.0〜9.3であり、か
つ酸強度H0が+4.8以下の酸量が0.8〜1.2μ
mol/m2であることを特徴とするビールの安定化処
理用二酸化ケイ素、及び、(2)塩類水溶液中にケイ酸
ナトリウムと鉱酸とを撹拌しながら同時に加えてpH
3.0〜7.0において80℃以下で反応を行った後、
得られたシリカ懸濁液をpH3.0〜7.0に調整し、
次いで濾過、水洗し、得られたシリカハイドロゲルを水
に再分散すると共に、そのpHを5.5〜8.5に調整
し、これを濾過、水洗した後、乾燥することを特徴とす
るビールの安定化処理用二酸化ケイ素の製造方法を提供
する。
Therefore, according to the present invention, (1) the specific surface area according to the BET method is 500 to 800 m 2 / g, and the pH of a 5% by weight aqueous suspension is 8.0 to 9.3. And acid strength H 0 is +4.8 or less and the amount of acid is 0.8 to 1.2 μ.
mol / m 2 of silicon dioxide for stabilizing beer, and (2) sodium silicate and mineral acid are simultaneously added to an aqueous solution of a salt with stirring to obtain a pH.
After performing the reaction at 80 to 80 ° C. in 3.0 to 7.0,
The obtained silica suspension was adjusted to pH 3.0 to 7.0,
Then, the beer is characterized by being filtered and washed with water, redispersing the obtained silica hydrogel in water, adjusting the pH thereof to 5.5 to 8.5, filtering this, washing with water, and then drying. The present invention provides a method for producing silicon dioxide for stabilizing treatment of.

【0015】以下、本発明につき更に詳しく説明する。
本発明のビールの安定化処理用二酸化ケイ素は、比表面
積が500〜800m2/g、好ましくは520〜78
0m2/gである。比表面積が500m2/gより小さい
とビールに対する安定化(混濁防止)機能が十分発揮さ
れず、本発明の目的を達成し得ない。また、比表面積が
800m2/gを超えると、高分子のタンパク質が物理
的に入れないような微細孔が多く、混濁タンパクの吸着
に寄与しない傾向になる。
The present invention will be described in more detail below.
The silicon dioxide for stabilizing beer of the present invention has a specific surface area of 500 to 800 m 2 / g, preferably 520 to 78.
It is 0 m 2 / g. When the specific surface area is less than 500 m 2 / g, the function of stabilizing beer (preventing turbidity) against beer is not sufficiently exerted, and the object of the present invention cannot be achieved. Further, when the specific surface area exceeds 800 m 2 / g, there are many fine pores in which high molecular weight proteins cannot physically enter and tend not to contribute to adsorption of cloudy proteins.

【0016】また、本発明のビール安定化処理用二酸化
ケイ素は、5重量%の水懸濁液としたときのpH(5%
水懸濁液pH)が8.0〜9.3、好ましくは8.2〜
9.0であるのが特徴であり、pHがアルカリ側にある
ことで二酸化ケイ素の表面酸性度が弱められ、ビールに
添加されたときに二酸化ケイ素の表面と混濁タンパクや
泡タンパクとの相互作用(親和性)が制御され、その結
果、ビールの泡特性を損うことなく、ビールの安定性向
上に対して優れた性能を有するものである。これに対
し、このpHが8.0より低いとビールの泡特性(泡持
ちや泡つき)が劣り、本発明の目的が達成されない。ま
た、このpHが9.3より高くなると、二酸化ケイ素中
のアルカリ成分がビール中に溶出して香味に悪影響を及
ぼすことが懸念される。
Further, the silicon dioxide for beer stabilization treatment of the present invention has a pH (5%
Aqueous suspension pH) is 8.0 to 9.3, preferably 8.2.
Its characteristic is that it is 9.0, and the pH on the alkaline side weakens the surface acidity of silicon dioxide, and when added to beer, the interaction between the surface of silicon dioxide and turbid proteins or foam proteins. The (affinity) is controlled, and as a result, it has excellent performance for improving the stability of beer without impairing the foam characteristics of beer. On the other hand, when the pH is lower than 8.0, the beer foam characteristics (foam holding and foaming) are inferior, and the object of the present invention cannot be achieved. Further, if the pH is higher than 9.3, it is feared that the alkaline component in silicon dioxide is dissolved in beer and adversely affects the flavor.

【0017】更に、本発明のビール安定化処理用二酸化
ケイ素は、酸強度H0が+4.8以下の酸量が0.8〜
1.2μmol/m2であることが必要であり、このよ
うな酸強度を有することにより、ビールの泡持ちに好結
果を与えることができる。これに対し、上記酸強度が
1.2μmol/m2を超えるとビールの泡持ちが悪く
なり、0.8μmol/m2を下まわると二酸化ケイ素
中の残存アルカリ成分が多くなり、前述したように該ア
ルカリ分がビール中に溶出してビールの香味に悪影響を
及ぼし、またビールの物理的安定性が低下する。
Furthermore, the beer stabilizing silicon dioxide of the present invention has an acid strength H 0 of +4.8 or less and an acid amount of 0.8 to 0.8.
It needs to be 1.2 μmol / m 2 , and having such an acid strength can give a favorable result to the foam retention of beer. On the other hand, when the acid strength exceeds 1.2 μmol / m 2 , the foam retention of beer becomes poor, and when it falls below 0.8 μmol / m 2 , the residual alkali component in silicon dioxide increases, and as described above. The alkali content dissolves in beer and adversely affects the flavor of beer, and the physical stability of beer decreases.

【0018】図1は、後述する実施例で示した方法によ
り測定したビールの泡持ちと二酸化ケイ素の上記酸強度
との関係をプロットしたもので、この結果より、酸強度
0が+4.8以下の酸量が1.2μmol/m2を境に
してそれを超えると明らかに泡持ちが悪くなることがわ
かる。この理由については、現在のところ十分には解明
されていないが、本発明者らは以下の理由によるものと
推定している。
FIG. 1 is a plot of the relationship between the foam retention of beer and the above-mentioned acid strength of silicon dioxide, which was measured by the method shown in Examples described later. From this result, the acid strength H 0 is +4.8. It can be seen that when the following acid amount exceeds 1.2 μmol / m 2 as a boundary, the foam retention is obviously deteriorated. The reason for this has not been sufficiently clarified at present, but the present inventors presume that the reason is as follows.

【0019】即ち、ビールのpHは4〜4.2程度であ
り、二酸化ケイ素の等電点は2、もしくは不純物の影響
でそれより少し高いぐらいである(化学便覧より)。従
って、ビール中で二酸化ケイ素の表面はマイナスの電荷
を持っている。一方、ビール中の混濁タンパクと泡タン
パクは、それぞれ等電点が4付近と7以上といわれてお
り(“Stabilization of beer
using silica gel” Proc.Cn
ov.of Inst.Brew.より)、従って、ビ
ール中において、混濁タンパクは電荷的にほとんど中性
で、泡タンパクはプラスの電荷を有しているものと考え
られる。それ故、ビール中でマイナスの電荷を持った二
酸化ケイ素の表面は、電気的に中性の混濁タンパクより
もプラスの電荷を持った泡タンパクとの相互作用(吸着
性)が大きいと考えられる。
That is, the pH of beer is about 4 to 4.2, and the isoelectric point of silicon dioxide is 2, or a little higher than that due to the influence of impurities (from Chemical Handbook). Therefore, in beer, the surface of silicon dioxide has a negative charge. On the other hand, the turbid protein and foam protein in beer are said to have isoelectric points around 4 and 7 and above, respectively (“Stabilization of beer”).
using silica gel ”Proc. Cn
ov. of Inst. Brew. Therefore, it is considered that in beer, cloudy proteins are almost neutral in charge and foam proteins have a positive charge. Therefore, it is considered that the surface of silicon dioxide, which has a negative charge in beer, has a larger interaction (adsorption) with the foam protein, which has a positive charge, than the electrically neutral turbid protein.

【0020】以上のことから、混濁タンパクは電気的な
相互作用よりも二酸化ケイ素の物理的な細孔構造(比表
面積、細孔径など)により、選択的に吸着除去されるこ
とが考えられるが(gel−permiation効
果)、二酸化ケイ素の表面のマイナスの電荷量が多い、
即ち、上記酸強度(表面酸性度)が大きいと泡タンパク
の吸着性が高くなるため、ビールの泡特性が悪くなると
考えられる。従って、本発明による二酸化ケイ素は、5
00〜800m2/gといった大きな比表面積を有して
いるだけでなく、その表面酸性度を弱める、即ち、酸強
度H0が+4.8以下の酸量を1.2μmol/m2以下
とすることで、ビールの泡特性を損うことなく、ビール
の安定性向上に対して優れた性能を示すと考えられる。
From the above, it is considered that cloudy proteins are selectively adsorbed and removed by the physical pore structure (specific surface area, pore diameter, etc.) of silicon dioxide rather than electrical interaction ( gel-permiation effect), the amount of negative charges on the surface of silicon dioxide is large,
That is, when the above-mentioned acid strength (surface acidity) is high, the adsorption property of the foam protein becomes high, so that the foam characteristic of beer is considered to be deteriorated. Therefore, the silicon dioxide according to the present invention is 5
Not only has a large specific surface area of 00 to 800 m 2 / g, but also weakens its surface acidity, that is, the acid amount having an acid strength H 0 of +4.8 or less is 1.2 μmol / m 2 or less. Thus, it is considered that the beer exhibits excellent performance for improving the stability of beer without deteriorating the foam characteristics of beer.

【0021】ここで、特開平4−79876号公報の提
案においても、二酸化ケイ素の酸強度(表面酸性度)を
重要項目としているが、この提案において表面酸性度を
制御する意味は、特定された酸強度分布の固体酸酸量を
有しているシリカゲルをビール中に配合すると、このシ
リカゲルの触媒作用により、ビール中のタンパク質とタ
ンニンとが常温で速やかに複合体を生成し、その結果、
ビールの混濁に関与するタンニン類の除去が有効に行え
るというものであり、酸強度を混濁タンパクの除去、ビ
ールの安定化の点のみからとらえており、泡タンパクの
保持の面、ビールの泡持ちの点から酸強度に着目してい
るものではない。これに対し、本発明は、二酸化ケイ素
とビール中の種々のタンパク質との相互作用(親和性)
において、泡タンパクの吸着を極力少なくして、混濁タ
ンパクのみを選択的に吸着除去するために表面酸性度を
制御するものである。実際、上記提案においては、表面
酸性度の単位がmmol/g、即ち、単位重量当りの酸
量であるのに対して、本発明では、μmol/m2、即
ち、単位表面積当りの酸量として定義している。従っ
て、上記提案の場合は、単にシリカ表面の酸性サイトの
総量であるのに対して、本発明では、シリカ表面の固体
酸密度を意味しており、このことがビール中の種々のタ
ンパク質とシリカとの相互作用、吸着(配向)状態など
と密接に関係しており、ビール中の混濁タンパクをより
選択的に吸着除去できるものである。
Here, in the proposal of Japanese Patent Laid-Open No. 4-79876, the acid strength (surface acidity) of silicon dioxide is also an important item, but the meaning of controlling the surface acidity in this proposal has been specified. When silica gel having a solid acid amount of acid strength distribution is mixed in beer, the catalyst of this silica gel rapidly forms a complex between protein and tannin in beer at room temperature, and as a result,
The tannins involved in beer turbidity can be effectively removed.According to acid strength only from the viewpoint of removing turbid proteins and stabilizing beer, the retention of foam proteins and the retention of beer foam. Therefore, it does not focus on the acid strength. On the other hand, the present invention relates to the interaction (affinity) between silicon dioxide and various proteins in beer.
In the above, the adsorption of the foam protein is minimized and the surface acidity is controlled in order to selectively adsorb and remove only the turbid protein. In fact, in the above proposal, the unit of surface acidity is mmol / g, that is, the amount of acid per unit weight, whereas in the present invention, μmol / m 2 , that is, the amount of acid per unit surface area is It is defined. Therefore, in the case of the above proposal, while it is simply the total amount of acidic sites on the silica surface, the present invention means the solid acid density on the silica surface, which means that various proteins and silica in beer are present. It is closely related to the interaction with, the adsorption (orientation) state, etc., and is capable of more selectively adsorbing and removing the cloudy protein in beer.

【0022】本発明のビール安定化処理用二酸化ケイ素
は、更に吸着した混濁タンパクを細孔内に保持する必要
があるという点から細孔容積が0.5〜1.5ml/
g、特に0.6〜1.2ml/gであることが好まし
く、混濁タンパクがより選択的に細孔内に入り、吸着除
去されるという点から平均細孔径が4〜12nm、特に
5〜10nmであることが好ましい。また、乾燥効率や
作業性などの点から、そして保管中の微生物の繁殖を抑
えるという点から水分含有量が3〜15重量%、特に5
〜12重量%であることが好ましい。なお、使用する二
酸化ケイ素の平均粒子径は、ビールに対する濾過性を考
慮して通常10〜20μmであり、より好ましくは12
〜18μmである。
The silicon dioxide for beer stabilization treatment of the present invention has a pore volume of 0.5 to 1.5 ml / in that the adsorbed cloudy protein must be retained in the pores.
g, particularly 0.6 to 1.2 ml / g, and the average pore diameter is 4 to 12 nm, particularly 5 to 10 nm from the viewpoint that the turbid protein more selectively enters the pores and is adsorbed and removed. Is preferred. Further, from the viewpoint of drying efficiency and workability, and from the viewpoint of suppressing the growth of microorganisms during storage, the water content is 3 to 15% by weight, particularly 5%.
It is preferably ˜12% by weight. The average particle size of the silicon dioxide used is usually 10 to 20 μm in view of the filterability for beer, and more preferably 12
-18 μm.

【0023】上記二酸化ケイ素は、硫酸ナトリウム、塩
化ナトリウム、リン酸ナトリウム等の塩類水溶液中にケ
イ酸ナトリウム溶液と硫酸、塩酸等の鉱酸を同時に加え
て二酸化ケイ素を析出させる方法(同時注加法)によっ
て得ることができる。この場合、反応は80℃以下、好
ましくは75℃以下、更に好ましくは70℃以下で行
い、また反応中のpHは3.0〜7.0、好ましくは
3.5〜6.0とする。反応温度が80℃より高いと、
得られる二酸化ケイ素の比表面積が小さいものとなり、
また酸強度も大きいものになる。なお、室温以下で反応
を行ってもよいが、この場合、生成する反応スラリーは
濾過性が悪いため、その後の濾過(固液分離)・水洗の
効率がかなり悪くなる上、特にケイ酸ナトリウムの濃度
が高いと反応中に液全体が固化する場合があるので、4
0℃以上で反応を行うことが好ましい。また、反応中の
pHが3.0より低いと通常の工業的な設備では耐酸性
において材質的な問題がある。また、pHが7.0より
も高いと最終的に得られる二酸化ケイ素の比表面積が目
標とするものよりも小さくなり、ビールの安定性向上に
対して十分な効果が得られない。
The silicon dioxide is prepared by simultaneously adding a sodium silicate solution and a mineral acid such as sulfuric acid or hydrochloric acid to an aqueous salt solution of sodium sulfate, sodium chloride, sodium phosphate or the like to precipitate silicon dioxide (simultaneous injection method). Can be obtained by In this case, the reaction is carried out at 80 ° C. or lower, preferably 75 ° C. or lower, more preferably 70 ° C. or lower, and the pH during the reaction is 3.0 to 7.0, preferably 3.5 to 6.0. If the reaction temperature is higher than 80 ° C,
The resulting silicon dioxide has a small specific surface area,
Moreover, the acid strength is also high. The reaction may be carried out at room temperature or lower, but in this case, the resulting reaction slurry has poor filterability, so that the efficiency of subsequent filtration (solid-liquid separation) / water washing is considerably deteriorated, and in particular, sodium silicate If the concentration is high, the entire liquid may solidify during the reaction, so 4
It is preferable to carry out the reaction at 0 ° C. or higher. Further, if the pH during the reaction is lower than 3.0, there is a material problem in acid resistance in ordinary industrial equipment. If the pH is higher than 7.0, the specific surface area of the finally obtained silicon dioxide will be smaller than the target, and a sufficient effect for improving the stability of beer cannot be obtained.

【0024】また、本発明の製造方法においては、反応
後のシリカ懸濁液のpHを3.0〜7.0、好ましくは
3.5〜6.0に調整する(一段目pH調整)ことが必
要であるが、この必要性については、反応中のpH制御
と同様の理由によるものである。
In the production method of the present invention, the pH of the silica suspension after the reaction is adjusted to 3.0 to 7.0, preferably 3.5 to 6.0 (first step pH adjustment). Is necessary for the same reason as the pH control during the reaction.

【0025】更に、反応生成物を濾過・水洗して得られ
たシリカハイドロゲルを水に再分散したときに、懸濁液
のpHを5.5〜8.5、好ましくは6.0〜8.0に
調整する(二段目pH調整)ことが必須であり、調整p
Hがこの範囲以外であると、最終的に得られる二酸化ケ
イ素の製品pH及び酸強度(表面酸性度)が目標とする
ものからはずれるためにビールの泡特性が悪くなってし
まう。
When the silica hydrogel obtained by filtering and washing the reaction product is redispersed in water, the pH of the suspension is 5.5 to 8.5, preferably 6.0 to 8. It is indispensable to adjust to 0.0 (second-step pH adjustment), and adjustment p
If H is out of this range, the product pH and acid strength (surface acidity) of the finally obtained silicon dioxide deviate from the target values, and thus the beer foam characteristics deteriorate.

【0026】即ち、本発明の製造方法にあっては、この
ように二段階のpH調整を行うこと、しかもそのpH調
整範囲を上記のようにすることにより、上述した特性の
ビール安定化処理用二酸化ケイ素を得ることができるも
のである。
That is, in the production method of the present invention, by performing the two-step pH adjustment as described above, and by setting the pH adjustment range as described above, the beer stabilization treatment having the above-mentioned characteristics is performed. It is possible to obtain silicon dioxide.

【0027】ここで、上記一段目pH調整した後の放置
時間は30分〜5時間が好ましく、また二段目pH調整
した後の放置時間は30分〜3時間が好ましい。放置時
間が30分より短いとpH調整の効果が充分に現われ
ず、また、逆に放置が長すぎてもpH調整の効果はあま
り変わらず生産性が低下するだけである。さらにスラリ
ーのpHが7以上の場合はあまり長時間放置すると最終
的に得られる二酸化ケイ素の比表面積が小さくなる傾向
がある。
Here, the standing time after the first-step pH adjustment is preferably 30 minutes to 5 hours, and the standing time after the second-step pH adjustment is preferably 30 minutes to 3 hours. If the standing time is shorter than 30 minutes, the effect of pH adjustment does not sufficiently appear. On the contrary, if the standing time is too long, the effect of pH adjustment does not change so much and the productivity only decreases. Further, when the pH of the slurry is 7 or more, the specific surface area of the finally obtained silicon dioxide tends to be small if left for a long time.

【0028】なお、pH調整後の処理は、一般に微粉状
二酸化ケイ素が製造される公知の方法で濾過・水洗・乾
燥し、更に必要に応じて所定の粒度に粉砕(及び、分
級)すればよい。
The treatment after pH adjustment may be carried out by filtration, washing with water and drying by a known method for producing finely powdered silicon dioxide, and further pulverizing (and classifying) to a predetermined particle size if necessary. .

【0029】本発明のビール安定化処理用二酸化ケイ素
は、公知のビール安定化処理用二酸化ケイ素と同様にし
て使用することができ、後醗酵・熟成させたビールの濾
過に有効に用いられる。この場合、ケイソウ土等の濾過
助剤と一緒に用いることができる。
The beer-stabilizing silicon dioxide of the present invention can be used in the same manner as the known beer-stabilizing silicon dioxide, and is effectively used for filtering beer that has been post-fermented and aged. In this case, it can be used together with a filter aid such as diatomaceous earth.

【0030】本発明に係る二酸化ケイ素で処理されたビ
ールは、安定性に優れている上、泡特性が良好なものと
なり、総合的に優れたビールを得ることができる。
The beer treated with silicon dioxide according to the present invention is excellent in stability and also has good foaming characteristics, and an excellent beer can be obtained as a whole.

【0031】[0031]

【実施例】以下、実施例と比較例を示し、本発明を具体
的に説明するが、本発明は下記の実施例に制限されるも
のではない。
EXAMPLES The present invention will be described below in detail with reference to examples and comparative examples, but the present invention is not limited to the following examples.

【0032】〔実施例1〕市販のJIS3号ケイ酸ナト
リウムを希釈した溶液と希硫酸とを硫酸ナトリウム溶液
中に撹拌しながら同時に加え、反応中のpHを5.0〜
5.5の間に保ちながら65℃で反応を行う。
[Example 1] A commercially available solution of diluted JIS No. 3 sodium silicate and dilute sulfuric acid were simultaneously added to a sodium sulfate solution while stirring, and the pH during the reaction was adjusted to 5.0 to 5.0.
The reaction is carried out at 65 ° C, keeping it between 5.5.

【0033】次に、反応後のシリカ懸濁液のpHを5.
0に調整し、1時間放置後、濾過・水洗を行い、得られ
たシリカハイドロゲルを水に再分散し、そのときの懸濁
液のpHを7.0に調整し、1時間放置した。
Next, the pH of the silica suspension after the reaction was adjusted to 5.
It was adjusted to 0 and left for 1 hour, then filtered and washed with water, the obtained silica hydrogel was redispersed in water, the pH of the suspension at that time was adjusted to 7.0, and left for 1 hour.

【0034】pH調整後の処理は、一般に微粉状二酸化
ケイ素を製造する公知の方法で濾過・水洗・乾燥し、更
に粉砕(及び分級)して、所定の粒度に調整した。
The treatment after pH adjustment was generally carried out by filtration, washing with water and drying by a known method for producing finely powdered silicon dioxide, and further pulverization (and classification) to adjust to a predetermined particle size.

【0035】〔実施例2、比較例1〜7〕反応温度、反
応後のシリカ懸濁液のpH(一段目pH調整)、得られ
たハイドロゲルを水に再分散させたときの懸濁液のpH
(二段目pH調整)を表1に示した通りとした以外は実
施例1と同様に操作した。
[Example 2, Comparative Examples 1 to 7] Reaction temperature, pH of silica suspension after reaction (first step pH adjustment), suspension obtained by redispersing the obtained hydrogel in water PH of
The same operation as in Example 1 was performed except that (second step pH adjustment) was as shown in Table 1.

【0036】〔比較例8,9〕反応温度を表1に示す通
りとし、一段目のpH調整を表1に示すpHで行い、二
段目のpH調整を行わなかった以外は実施例1と同様に
操作した。
Comparative Examples 8 and 9 As in Example 1 except that the reaction temperature was as shown in Table 1, the first-step pH adjustment was performed at the pH shown in Table 1, and the second-step pH adjustment was not performed. The same operation was performed.

【0037】得られた二酸化ケイ素の物性、これらを用
いてビールを安定化処理した場合のビール評価結果を表
1に併記する。なお、二酸化ケイ素の物性及びビールの
評価は下記方法によって行った。二酸化ケイ素の物性測定方法 〔比表面積〕日本ベル(株)製全自動比表面積/細孔分
布測定装置(BELSORP 28)を用いて、窒素吸
着法(BET法)により比表面積を測定した。なお、試
料の前処理は、160℃で2時間、真空脱気した。 (参考文献:S.Brunauer,P.H.Emme
tt,E.Teller,J.Amer.Chem.S
oc.,60,309(1938)) 〔製品pH〕試料5gをイオン交換水100ml中に分
散させ、一旦沸騰させた後、室温まで冷却し、スラリー
のpHを測定する。 〔酸強度(表面酸性度)〕表面酸性度は、単位重量或い
は単位体積当りの酸性点の数もしくはモル数と定義され
る。共栓付き三角フラスコに試料を入れ、140〜15
0℃で3時間乾燥した後、そのときの試料重量を精秤す
る。精製したベンゼンを投入し、指示薬(ハメット指示
薬)としてメチルレッド(pKa=+4.8)を添加し
た後、n−ブチルアミンで滴定する。このときの滴定量
(モル数)と前述の比表面積から、単位表面積当りの酸
性度〔酸強度H0が+4.8以下の酸量〕を算出した。 (参考文献:「吸着」,慶伊富長著,共立全書,p.7
2〜、及び、触媒工学講座4,「触媒基礎測定法」,触
媒学会編,p.161〜) 〔細孔容積〕前述のBELSORP 28を用いて窒素
の吸着等温線を求め、JIS−K1150に準拠してド
リモアヒールの解析法により、細孔径2〜60nmの細
孔容積を求めた。 〔平均細孔径〕前述した比表面積と細孔容積から以下の
式により平均細孔径を求めた。 平均細孔径(nm)=4000×細孔容積(ml/g)
/比表面積(m2/g) 〔水分含有量〕105℃で4時間乾燥した時の重量減量
を水分含有量とした。
Table 1 also shows the physical properties of the obtained silicon dioxide and the results of beer evaluation when the beer was stabilized with these materials. The physical properties of silicon dioxide and beer were evaluated by the following methods. Method for measuring physical properties of silicon dioxide [specific surface area] The specific surface area was measured by a nitrogen adsorption method (BET method) using a fully automatic specific surface area / pore distribution measuring device (BELSORP 28) manufactured by Nippon Bell Co., Ltd. The sample was pretreated by vacuum degassing at 160 ° C. for 2 hours. (Reference: S. Brunauer, PH Emme.
tt, E.I. Teller, J .; Amer. Chem. S
oc. , 60, 309 (1938)) [Product pH] Disperse 5 g of a sample in 100 ml of ion-exchanged water, boil once, cool to room temperature, and measure the pH of the slurry. [Acid Strength (Surface Acidity)] The surface acidity is defined as the number of acid points or the number of moles per unit weight or unit volume. Put the sample in an Erlenmeyer flask with a ground stopper, 140 ~ 15
After drying at 0 ° C. for 3 hours, the sample weight at that time is precisely weighed. Purified benzene is added, methyl red (pKa = + 4.8) is added as an indicator (Hamet indicator), and then titrated with n-butylamine. The acidity per unit surface area [the amount of acid having an acid strength H 0 of +4.8 or less] was calculated from the titration amount (number of moles) at this time and the specific surface area described above. (Reference: "Adsorption", Tominaga Keiitoshi, Kyoritsu Zensho, p.7.
2 and 2, Catalytic Engineering Course 4, "Catalyst Basic Measurement Method", edited by The Catalysis Society of Japan, p. 161-) [Pore volume] The adsorption isotherm of nitrogen was obtained using the above-mentioned BELSORP 28, and the pore volume having a pore diameter of 2 to 60 nm was obtained by the analysis method of Dorymore heel according to JIS-K1150. [Average Pore Diameter] The average pore diameter was calculated from the above-mentioned specific surface area and pore volume by the following formula. Average pore diameter (nm) = 4000 × pore volume (ml / g)
/ Specific surface area (m 2 / g) [Water content] The water content was defined as the weight loss when dried at 105 ° C for 4 hours.

【0038】ビールでの性能評価方法 〔二酸化ケイ素によるビールの処理方法〕貯酒ビール
(若ビール)3Lに試験品である二酸化ケイ素1.5g
とケイソウ土3.0gを添加し、30分間撹拌した後、
フィルタープレスによるケイソウ土プリコート濾過を行
った。得られた濾過後ビールは、以下の各種分析に供し
た。 〔泡持ち〕ビールをガス抜きした後20℃に保持し、R
udin法に準拠して測定した(Institute
of Brewing誌)。即ち、二酸化炭素でビール
を泡立て、一定の高さの泡がビールに戻るまでの時間を
測定する。従って、泡持ちの良いビールはその時間が長
くなる。 〔泡つき〕Bamforth法を改良して測定を行った
(Institute of Brewing誌)。即
ち、コップ内でガス抜きしたビールを二酸化炭素により
泡立て、一定時間放置した後、コップの壁に付着した泡
を水で回収し、その吸光度から算出する。従って、この
数値が大きいほど泡つきが良い。 〔SASPL値〕ガス抜きしたビールに飽和硫安溶液を
一定量ずつ添加していき、タンパク質の不溶化による濁
度の上昇曲線から沈殿限界量を求める。従って、この値
が大きいほど混濁が起こりにくいことになる。 〔強制劣化濁度〕濾過直後にビールを50℃で1週間保
存し、更に0℃で24時間後の濁度(EBC濁度単位)
を測定する。
Method for evaluating performance with beer [Method for treating beer with silicon dioxide] 3 L of stored beer (young beer) was tested with 1.5 g of silicon dioxide.
And diatomaceous earth (3.0 g) were added and stirred for 30 minutes,
Diatomaceous earth precoat filtration was performed with a filter press. The obtained beer after filtration was subjected to the following various analyses. [Bubbling] Beer is degassed and then kept at 20 ° C
It was measured according to the udin method (Institute
of Brewing magazine). That is, beer is bubbled with carbon dioxide, and the time required for bubbles of a certain height to return to beer is measured. Therefore, beer with good foam lasts longer. [Bubbling] The measurement was carried out by modifying the Bamforth method (Institute of Brewing). That is, beer degassed in a cup is bubbled with carbon dioxide, left for a certain period of time, and then the bubbles adhering to the wall of the cup are collected with water, and the absorbance is calculated. Therefore, the larger this value is, the better the bubbles are. [SASPL value] A saturated ammonium sulfate solution is added to degassed beer in fixed amounts, and the precipitation limit amount is determined from the turbidity increase curve due to protein insolubilization. Therefore, the larger this value, the less likely turbidity occurs. [Forced deterioration turbidity] Beer is stored at 50 ° C for 1 week immediately after filtration, and turbidity after 24 hours at 0 ° C (EBC turbidity unit)
To measure.

【0039】[0039]

【表1】 [Table 1]

【0040】表1の結果より、本発明に係る二酸化ケイ
素(実施例1,2)は、泡持ち、泡つきが良好で、SA
SPLも大きく、強制劣化濁度も少ないことが認められ
る。
From the results shown in Table 1, the silicon dioxide according to the present invention (Examples 1 and 2) had good foam retention and foaming, and SA
It is recognized that the SPL is large and the forced deterioration turbidity is small.

【0041】これに対し、比較例1の二酸化ケイ素は、
二段目の調整pHが4.0と低く、製品pHが低い上、
表面酸性度も高いため、ビールの泡特性が悪くなる。比
較例2の二酸化ケイ素は反応温度が85℃と高く、比較
例3の二酸化ケイ素は一段目の調整pHが8.0と高
く、これらはいずれも比表面積が小さくなると共に、表
面酸性度が大きくなるため、泡持ちが劣り、かつ、ビー
ルの安定性も悪い。比較例4は、比表面積が大きすぎ、
また製品pHが低いため、泡持ち、泡つきが悪い。比較
例5は、一段目及び二段目の調整pHが本発明の条件か
ら外れ、比表面積、製品pH、表面酸性度がいずれも本
発明の範囲外であるため、ビールの泡特性も安定性も悪
いものである。比較例6は、表面酸性度が高く、泡持ち
が悪いと共に、ビールの安定性も劣る。比較例7は製品
pHが低く、泡特性が低下する。更に、比較例8,9は
pH調整を一段で行ったもので、比較例8の二酸化ケイ
素は製品pHが低く、泡特性が悪く、ビールの安定性も
不十分であり、比較例9の二酸化ケイ素は比表面積が小
さく、ビールの安定性が悪いものである。
On the other hand, the silicon dioxide of Comparative Example 1 is
The adjusted pH of the second step is as low as 4.0, the product pH is low, and
The high surface acidity also results in poor beer foam properties. The reaction temperature of the silicon dioxide of Comparative Example 2 was as high as 85 ° C., and the pH of the silicon dioxide of Comparative Example 3 was as high as 8.0 in the first step, and both of them have a small specific surface area and a large surface acidity. As a result, the foam retention is poor and the stability of beer is poor. Comparative Example 4 has a too large specific surface area,
In addition, since the product pH is low, foam retention and foaming are poor. In Comparative Example 5, the adjusted pH of the first step and the second step deviates from the conditions of the present invention, and the specific surface area, product pH, and surface acidity are all outside the ranges of the present invention, so the foam characteristics of beer are stable. Is also bad. Comparative Example 6 has high surface acidity, poor foam retention, and poor beer stability. In Comparative Example 7, the product pH is low and the foam property is deteriorated. Furthermore, in Comparative Examples 8 and 9, the pH adjustment was carried out in a single step. The silicon dioxide of Comparative Example 8 had a low product pH, had poor foam characteristics, and had insufficient beer stability. Silicon has a small specific surface area and has poor beer stability.

【0042】[0042]

【発明の効果】本発明のビールの安定化処理用二酸化ケ
イ素は、ビールの泡特性を損うことなく、優れたビール
の安定化処理(混濁防止)効果を与える。また、本発明
の製造方法によれば、かかる二酸化ケイ素を確実に製造
することができる。
EFFECT OF THE INVENTION The silicon dioxide for stabilizing beer of the present invention provides an excellent effect of stabilizing beer (preventing turbidity) without impairing the foam characteristics of beer. Moreover, according to the manufacturing method of the present invention, such silicon dioxide can be reliably manufactured.

【図面の簡単な説明】[Brief description of drawings]

【図1】二酸化ケイ素のH0が+4.8以下の酸量とビ
ールの泡持ちとの関係を示すグラフである。
FIG. 1 is a graph showing the relationship between the acid amount of silicon dioxide having H 0 of +4.8 or less and the foam retention of beer.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 堀内 誠一 東京都大田区大森北2−13−1 アサヒビ ール株式会社酒類開発研究所内 (72)発明者 角 博明 鳥取県倉吉市宮川町129 グランフォルム 倉吉405号 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Seiichi Horiuchi 2-13-1, Omorikita, Ota-ku, Tokyo Asahi Biru Co., Ltd. Alcoholic Beverages Research Institute (72) Inventor Hiroaki Kaku 129 Grandform, Miyagawa-cho, Kurayoshi-shi, Tottori Prefecture Kurayoshi 405

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 BET法による比表面積が500〜80
0m2/gであり、5重量%の水懸濁液としたときのp
Hが8.0〜9.3であり、かつ酸強度H0が+4.8
以下の酸量が0.8〜1.2μmol/m2であること
を特徴とするビールの安定化処理用二酸化ケイ素。
1. A specific surface area according to the BET method of 500 to 80.
0 m 2 / g, p when 5% by weight of water suspension
H is 8.0 to 9.3, and acid strength H 0 is +4.8.
The following acid amount is 0.8-1.2 micromol / m < 2 >, The silicon dioxide for stabilization processing of beer characterized by the above-mentioned.
【請求項2】 細孔容積が0.5〜1.5ml/g、平
均細孔径が4〜12nm、水分含有量が3〜15重量%
である請求項1記載のビールの安定化処理用二酸化ケイ
素。
2. A pore volume of 0.5 to 1.5 ml / g, an average pore diameter of 4 to 12 nm, and a water content of 3 to 15% by weight.
The silicon dioxide for stabilizing beer according to claim 1, which is
【請求項3】 塩類水溶液中にケイ酸ナトリウムと鉱酸
とを撹拌しながら同時に加えてpH3.0〜7.0にお
いて80℃以下で反応を行った後、得られたシリカ懸濁
液をpH3.0〜7.0に調整し、次いで濾過、水洗
し、得られたシリカハイドロゲルを水に再分散すると共
に、そのpHを5.5〜8.5に調整し、これを濾過、
水洗した後、乾燥することを特徴とするビールの安定化
処理用二酸化ケイ素の製造方法。
3. A solution of sodium silicate and a mineral acid are simultaneously added to an aqueous salt solution with stirring to carry out a reaction at a temperature of 3.0 to 7.0 at 80 ° C. or lower, and then the obtained silica suspension is adjusted to pH 3 It is adjusted to 0.0 to 7.0, then filtered and washed with water to redisperse the obtained silica hydrogel in water, and its pH is adjusted to 5.5 to 8.5, which is filtered,
A method for producing silicon dioxide for stabilizing beer, which comprises washing with water and then drying.
JP02474595A 1995-01-19 1995-01-19 Silicon dioxide for stabilizing beer and method for producing the same Expired - Fee Related JP3460357B2 (en)

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Application Number Priority Date Filing Date Title
JP02474595A JP3460357B2 (en) 1995-01-19 1995-01-19 Silicon dioxide for stabilizing beer and method for producing the same

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JPH08198616A true JPH08198616A (en) 1996-08-06
JP3460357B2 JP3460357B2 (en) 2003-10-27

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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998013138A1 (en) * 1996-09-27 1998-04-02 W.R. Grace & Co.-Conn Adsorbent compositions for odor removal
WO2002004593A1 (en) * 2000-07-11 2002-01-17 Sapporo Breweries Limited Process for producing malt alcoholic drink
JP2002243627A (en) * 2001-02-19 2002-08-28 Asahi Breweries Ltd Forced deterioration apparatus and turbidity capacity prediction method
JP2003057226A (en) * 2001-08-10 2003-02-26 Asahi Breweries Ltd Method of evaluating influence of shaking upon deterioration of beer
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CN104066683A (en) * 2012-01-25 2014-09-24 罗地亚运作公司 Precipitated-silica production method
WO2016075906A1 (en) * 2014-11-11 2016-05-19 パナソニックIpマネジメント株式会社 Aerogel and manufacturing method thereof
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Publication number Priority date Publication date Assignee Title
US5858909A (en) * 1996-09-27 1999-01-12 W. R. Grace & Co.-Conn. Siliceous oxide comprising an alkaline constituent
WO1998013138A1 (en) * 1996-09-27 1998-04-02 W.R. Grace & Co.-Conn Adsorbent compositions for odor removal
WO2002004593A1 (en) * 2000-07-11 2002-01-17 Sapporo Breweries Limited Process for producing malt alcoholic drink
US7135200B2 (en) 2000-07-11 2006-11-14 Sapporo Breweries Limited Process for producing malt alcoholic drink
EP1702977A3 (en) * 2000-07-11 2006-12-06 Sapporo Breweries Limited Method of producing malt alcohol beverages
JP4628559B2 (en) * 2001-02-19 2011-02-09 アサヒビール株式会社 Forced deterioration device and turbidity prediction method
JP2002243627A (en) * 2001-02-19 2002-08-28 Asahi Breweries Ltd Forced deterioration apparatus and turbidity capacity prediction method
JP2003057226A (en) * 2001-08-10 2003-02-26 Asahi Breweries Ltd Method of evaluating influence of shaking upon deterioration of beer
JP4659293B2 (en) * 2001-08-10 2011-03-30 アサヒビール株式会社 A method to assess the impact of shaking on beer degradation
JP2010500010A (en) * 2006-08-07 2010-01-07 グレース・ゲーエムベーハー・ウント・コムパニー・カーゲー Beer clarification aid based on silica xerogel with high filtration rate
US10633621B2 (en) 2006-08-07 2020-04-28 Grace Gmbh Beer clarification aid based on silica xerogel with high filterability
CN104066683A (en) * 2012-01-25 2014-09-24 罗地亚运作公司 Precipitated-silica production method
WO2016075906A1 (en) * 2014-11-11 2016-05-19 パナソニックIpマネジメント株式会社 Aerogel and manufacturing method thereof
JPWO2016075906A1 (en) * 2014-11-11 2017-07-06 パナソニックIpマネジメント株式会社 Airgel and method for producing the same
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