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JPS6250199B2 - - Google Patents

Info

Publication number
JPS6250199B2
JPS6250199B2 JP54028644A JP2864479A JPS6250199B2 JP S6250199 B2 JPS6250199 B2 JP S6250199B2 JP 54028644 A JP54028644 A JP 54028644A JP 2864479 A JP2864479 A JP 2864479A JP S6250199 B2 JPS6250199 B2 JP S6250199B2
Authority
JP
Japan
Prior art keywords
scale
aqueous solution
aluminum
fermentation
present
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP54028644A
Other languages
Japanese (ja)
Other versions
JPS55121896A (en
Inventor
Iwao Yashima
Toshiki Mori
Masayoshi Kotake
Toshe Taguchi
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.)
Nissan Chemical Corp
Original Assignee
Nissan Chemical Corp
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 Nissan Chemical Corp filed Critical Nissan Chemical Corp
Priority to JP2864479A priority Critical patent/JPS55121896A/en
Publication of JPS55121896A publication Critical patent/JPS55121896A/en
Publication of JPS6250199B2 publication Critical patent/JPS6250199B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23GCLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
    • C23G1/00Cleaning or pickling metallic material with solutions or molten salts
    • C23G1/02Cleaning or pickling metallic material with solutions or molten salts with acid solutions

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
  • Preventing Corrosion Or Incrustation Of Metals (AREA)
  • Cleaning In General (AREA)
  • Cleaning By Liquid Or Steam (AREA)
  • Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は麦酒の製造工程における醗酵装置内壁
に付着せるスケールを溶解させることにより醗酵
装置内壁から付着スケールを除去する新規な方法
に関する。 従来より、一般にビールを製造する場合には、
澱粉質副原料を添加するか又は添加せずに粉砕麦
芽を水と共に加熱して可溶性醗酵性糖類を含有す
るいわゆる麦汁と称される液が先ず作られる。つ
いでこの麦汁にホツプを加えて煮沸するか、ホツ
プからの抽出物で処理した後、又はこれらの処理
を加えずに醗酵タンク中で適当な温度で酵母を加
え、醗酵性糖類をアルコール、炭酸ガス及び醗酵
副生物に転化させることが行われる。この工程は
前醗酵と称され、得られた醗酵液は通常若ビール
と呼ばれる。若ビールは酵母を分離した後、後醗
酵タンクでさらに後醗酵を行わせることにより、
若ビール臭の除去、ビール蛋白の除去、炭酸ガス
のビールへの溶け込みが行われる。後醗酵により
得られたビールには、カーボネーシヨンと呼ばれ
る炭酸ガス処理が行われ、次いで過することに
より製品が得られる。 上記前醗酵及び後醗酵工程に用いられる醗酵タ
ンクの内壁には次第に不溶性物質が沈積し、遂に
スケールとなつて付着しこのものは伝熱効率を低
下させ、また雑菌の混入の一因ともなる。 そこで通常、冷麦汁等を醗酵タンクに仕込む前
に醗酵タンク内壁のスケール除去及び殺菌洗浄が
行われるが、特にこのスケールを簡易に除去する
ことは困難であり、通常の洗浄方法では殆んど効
率よく除去できない。 通常、醗酵室内には、多数の醗酵タンクが設置
され、それらはいずれも低温、例えば10℃以下の
温度に保たれているので、いずれか一つのタンク
を、特に大型タンクを高温加熱下に洗浄するとき
は、囲りのタンクに悪影響をもたらすのみなら
ず、変形を伴いやすく好ましくない。そこで、通
常、10℃前後から室温付近の温度で洗浄が行われ
るが、かゝる低温では、通常の洗浄水や、苛性ソ
ーダ、苛性カリ、等を含むアルカリ性洗剤等を用
いる方法によつてはスケールは殆んど除去されな
い。また、定期的に、硫酸、硝酸、硝酸尿素等の
強酸等を用いて洗浄することも行われるが、矢張
りスケールは能率よく除去できない上、醗酵タン
ク材質が腐食損傷される等の原因ともなり、好ま
しくない。更に、硝酸尿素とけいそう土を混ぜあ
わせてペースト状にした薬剤を、スケール表面に
塗り付けたり、また、金属性ブラシで直接スケー
ルをけずり落す方法もあるが、これらの方法も作
業性が悪く、好まれない。 通常、醗酵液が接触するタンク材質としては、
アルミニウム、砲金、SUS304、樹脂ライニング
等であるが、苛性ソーダ、苛性カリ等の液はアル
ミニウムに対しては浸食が大きく、硝酸や硝酸尿
素の溶液は、砲金に対して腐食性があり、酸化窒
素の発生を伴つたりする。又、硝酸や硫酸等は劇
薬であり、取り扱い作業が容易でなく特に、硫酸
を使用する時には副生する硫酸カルシウムが再付
着することもありこれによるトラブル等を招くこ
ともある。 本発明者らは、麦酒の醗酵装置内壁に付着せる
スケールを簡易に除去する安全かつ効率的方法を
確立することを意図し、上記スケールに対する各
種薬液の作用効果を詳しく研究した結果、塩基性
塩化アルミニウム、塩基性硝酸アルミニウム及び
塩基性スルフアミン酸アルミニウム等の水溶液が
10〜20℃という低温で、上記スケールを極めて迅
速に溶解する驚くべき新事実を見出し、本発明を
完成した。本発明の目的は麦酒の醗酵装置内壁に
付着せるスケールを簡易に、効率よく、しかも作
業上も安全に溶解する方法を提供することにあ
り、更に他の目的は、装置内壁に腐食損傷等を生
起させない上記スケールの除去方法を提供するこ
とにある。 本発明のスケール除去方法は麦酒の醗酵装置内
壁に付着せるスケールに、塩素イオン、硝酸根、
スルフアミン酸根からなる群より選ばれる1種又
は2種以上の陰イオンとアルミニウムイオンをア
ルミニウムイオン1モルに対して、上記陰イオン
が0.33モル以上3モル未満の割合に共存させた水
溶液を接触させることを特徴とする。 本発明の方法が適用される溶解除去すべきスケ
ールは、前記麦酒製造における前醗酵及び後醗酵
工程の醗酵液が接触する装置内壁に付着せるスケ
ールでありその主成分は、カルシウム分及び修酸
分である。 本発明に用いられる水溶液には、水中に塩素イ
オンン、硝酸根、スルフアミン酸根等とアルミニ
ウムイオンが、アルミニウムイオン1モルに対し
て上記陰イオンが0.33モル以上3モル未満特に好
ましくは1〜2.5モルの割合で共存し、本発明の
目的が達成される限り、他に任意の成分を含有し
て差支えない。上記比率の範囲外のモル比では、
水溶液はスケールを溶解する能力が低下し、好ま
しくない。上記モル比率に上記両イオンが共存す
る本発明に用いられる水溶液は、例えば、塩基性
塩化アルミニウム、塩基性硝酸アルミニウム、塩
基性スルフアミン酸アルミニウム等を水に溶解す
る方法により、また、塩酸、硝酸、スルフアミン
酸等と水酸化アルミニウム又は金属アルミニウム
を水に溶解する方法等により容易に得られ、その
他一般に液中のイオン組成が塩基性塩Al(X)o
(OH)3-o(但し、Xは塩素イオン、硝酸の陰イオ
ン基又はスルフアミン酸の陰イオンを、また、n
は0.33乃至3未満の数を表わす。)の組成となる
ように溶解性物質を水に溶解することにより得ら
れる。 本発明に用いられる水溶液中には、塩素イオ
ン、硝酸根又はスルフアミン酸根とアルミニウム
イオンが含まれているが、前記スケールの溶解に
際しては、スケールを全量溶解するに充分な量の
上記陰イオン及びアルミニウムが含まれねばなら
ない。前記スケールと接触させるべき水溶液の好
ましい量は、含有アルミニウムイオン及び上記陰
イオンの濃度に依存する。水溶液があまり高濃度
では、その割には溶解能力が向上せず、また、あ
まり低濃度では水溶液をスケールに接触すべき時
間が長くなり好ましくない。通常好ましい濃度範
囲はアルミニウムイオンとして0.001〜12.4重量
%、特に0.01〜6重量%程度である。また、前記
付着スケールの除去のために用いられる水溶液の
好ましい濃度及び量は、スケールと接触させる条
件にも依存する。通常、除去すべきスケールの化
学組成は一定していないが、スケール1重量部に
対し上記水溶液を10〜10000重量部の割合でスケ
ールに接触させるのが好ましい。本発明の方法に
より、前記スケールに接触させる際の水溶液の温
度としては、通常0〜80℃好ましくは5〜40℃、
特に望ましくは10〜25℃程度が良い。本発明の方
法により、スケールを迅速に溶解させるには、上
記水溶液を定置洗浄装置等によるスプレー方式に
よりスケールに接触させる方法、また、上記水溶
液を前記醗酵装置内に供給し、貯液を撹拌下に接
触させる方法もよい。 本発明に用いられる前記水溶液には、本発明の
目的が達成されるに限り、前記特定比率の特定イ
オンの他の必要に応じ、界面活性剤、アルコー
ル、酸、エステル、塩、腐食抑制剤、殺菌剤等が
含められても差支えない。また本発明の方法は、
従来から行われているアルカリ性水溶液と殺菌洗
浄剤による洗浄方法、酸性水溶液をスケールに接
触させることによる洗浄方法等と組合せて実施す
ることもできる。また、けいそう土、その他の担
体、研磨材等を更に配合して得られるスラリー、
ペースト等をスケール表面に接触又は塗布するこ
とによりスケール除去を実施することもできる。 次に本発明の好ましい実施態様を例示する。 (1) 塩基性塩化アルミニウム、塩基性硝酸アルミ
ニウム、塩基性スルフアミン酸アルミニウム又
はこれらの混合物を、アルミニウムイオン1モ
ルに対し、酸の陰イオン1〜2.5モルのモル比
に、かつ、アルミニウムイオンとして0.01〜4
重量%となる割合で水に溶解させて得られる水
溶液を、醗酵装置内壁に付着せるスケールに、
2〜25℃で接触させる方法。 (2) 塩酸、硝酸、スルフアミン酸又はこれらの混
合物と水酸化アルミニウムをアルミニウムイオ
ン1モルに対して上記酸の陰イオン1〜2モル
のモル比に、かつ、アルミニウムイオンとして
0.01〜4重量%となる割合で水に溶解させて得
られる水溶液を上記(1)における水溶液の代りに
用いる上記(1)の方法。 本発明の方法は麦酒の製造工程における醗酵装
置内壁に付着せるスケールの溶解除去に用いられ
るが、そのスケールは、カルシウム分及び蓚酸分
が主成分であり、その他少量の有機及び無機物質
を含む。これら主成分が、本発明に用いられる上
記水溶液により極めて良好に溶解されることに基
いてスケールを形成している組織構造物が溶解さ
れ易くなるものと考えられる。本発明の方法は、
極めて有用性が高い。 以下実施例を挙げて更に詳しく説明するが、本
発明の技術的範囲はこれに限定されるものではな
い。 実施例 1 麦酒醸造工場の醗酵タンク内壁に付着せるスケ
ール(A)の1.00gを第1表記載の薬液100g中に投
入し、20℃で同表に記載の時間撹拌した後、0.6
μのミリポアフイルターで過し、過残渣を秤
量することによりスケールの溶解率を求めた。上
記薬液は、水に金属アルミニウムとスルフアミン
酸を第1表記載実験No.1〜3の組成及び濃度とな
るように反応溶解することにより得たものであ
る。結果を第1表に示す。
The present invention relates to a novel method for removing scale that adheres to the inner wall of a fermentation apparatus during the beer manufacturing process by dissolving the scale that adheres to the inner wall of the fermentation apparatus. Conventionally, when producing beer,
A liquid, so-called wort, containing soluble fermentable sugars is first made by heating ground malt with water, with or without the addition of starchy auxiliary materials. Next, hops are added to this wort and boiled, or after treatment with extracts from hops, or without any of these treatments, yeast is added to the wort at an appropriate temperature in a fermentation tank, and the fermentable sugars are converted to alcohol or carbonic acid. Conversion to gas and fermentation by-products takes place. This step is called pre-fermentation, and the resulting fermented liquor is usually called young beer. After separating the yeast, young beer is produced by further post-fermentation in a post-fermentation tank.
It removes the smell of young beer, removes beer proteins, and dissolves carbon dioxide into the beer. The beer obtained by post-fermentation is subjected to a carbon dioxide gas treatment called carbonation, and then filtered to obtain a product. Insoluble substances gradually accumulate on the inner wall of the fermentation tank used in the pre-fermentation and post-fermentation steps, and eventually adhere as scale, which reduces heat transfer efficiency and also causes contamination with bacteria. Therefore, before charging cold wort etc. into the fermentation tank, the inner walls of the fermentation tank are usually descaled and sterilized, but it is particularly difficult to easily remove this scale, and normal cleaning methods are rarely effective. It cannot be removed well. Normally, a large number of fermentation tanks are installed in a fermentation room, and all of them are kept at a low temperature, for example, 10℃ or less, so any one tank, especially a large tank, is cleaned under high temperature heat. When doing so, it not only has an adverse effect on the surrounding tank, but also tends to cause deformation, which is undesirable. Therefore, cleaning is usually carried out at temperatures ranging from around 10°C to around room temperature, but at such low temperatures, scale may be removed by methods that use regular cleaning water or alkaline detergents containing caustic soda, caustic potash, etc. Almost never removed. In addition, periodic cleaning is performed using strong acids such as sulfuric acid, nitric acid, and urea nitrate, but the scale cannot be removed efficiently and may cause corrosion damage to the fermentation tank material. , undesirable. Furthermore, there are methods such as applying a paste made by mixing urea nitrate and diatomaceous earth onto the surface of the scale, or directly scraping off the scale with a metal brush, but these methods also have poor workability. Not liked. Usually, the tank material that the fermentation solution comes into contact with is:
Aluminum, gunmetal, SUS304, resin lining, etc., but solutions such as caustic soda and caustic potash are highly corrosive to aluminum, and solutions of nitric acid and urea nitrate are corrosive to gunmetal and generate nitrogen oxide. accompanied by Furthermore, nitric acid, sulfuric acid, and the like are powerful chemicals that are not easy to handle, and especially when sulfuric acid is used, by-product calcium sulfate may re-deposit, which may cause trouble. The inventors of the present invention aimed to establish a safe and efficient method for easily removing scale that adheres to the inner walls of beer fermentation equipment, and as a result of detailed research on the effects of various chemical solutions on the scale, we found that basic chloride Aqueous solutions of aluminum, basic aluminum nitrate, basic aluminum sulfamate, etc.
We have completed the present invention by discovering a surprising new fact that the scale described above can be dissolved extremely quickly at a low temperature of 10 to 20°C. The purpose of the present invention is to provide a method for easily, efficiently, and safely dissolving scale adhering to the inner walls of beer fermentation equipment.A further object of the present invention is to provide a method for easily, efficiently, and safely dissolving scale adhering to the inner walls of beer fermentation equipment. The object of the present invention is to provide a method for removing the above-mentioned scale that does not cause the scale to occur. The scale removal method of the present invention uses chloride ions, nitrate radicals,
Contacting an aqueous solution in which one or more anions selected from the group consisting of sulfamic acid radicals and aluminum ions are made to coexist at a ratio of 0.33 mol or more and less than 3 mol of the above anions per 1 mol of aluminum ions. It is characterized by The scale to be dissolved and removed to which the method of the present invention is applied is the scale that adheres to the inner wall of the equipment that comes into contact with the fermentation liquid in the pre-fermentation and post-fermentation steps in beer production, and its main components are calcium and oxalic acid. It is. The aqueous solution used in the present invention contains chloride ions, nitrate radicals, sulfamic acid radicals, etc. and aluminum ions in water, and the above anions are preferably 0.33 mol or more and less than 3 mol, particularly preferably 1 to 2.5 mol, per 1 mol of aluminum ions. Any other optional components may be contained as long as they coexist in the same proportions and the object of the present invention is achieved. For molar ratios outside the range of the above ratios,
Aqueous solutions are not preferred because they have a reduced ability to dissolve scale. The aqueous solution used in the present invention in which both of the ions coexist in the above molar ratio can be prepared by, for example, dissolving basic aluminum chloride, basic aluminum nitrate, basic aluminum sulfamate, etc. in water, or by dissolving hydrochloric acid, nitric acid, It can be easily obtained by dissolving sulfamic acid etc. and aluminum hydroxide or metal aluminum in water, and generally the ionic composition in the liquid is a basic salt Al(X) o
(OH) 3-o (However, X is a chlorine ion, an anion group of nitric acid, or an anion of sulfamic acid, and n
represents a number from 0.33 to less than 3. ) can be obtained by dissolving a soluble substance in water so that it has the following composition. The aqueous solution used in the present invention contains chloride ions, nitrate radicals, or sulfamic acid radicals, and aluminum ions, but when dissolving the scale, it is necessary to use the anions and aluminum in sufficient amounts to dissolve the entire scale. must be included. The preferred amount of aqueous solution to be contacted with the scale depends on the aluminum ion content and the concentration of the anion. If the concentration of the aqueous solution is too high, the dissolving ability will not be improved accordingly, and if the concentration is too low, the time for which the aqueous solution should be in contact with the scale will be undesirable. The generally preferred concentration range is about 0.001 to 12.4% by weight, particularly about 0.01 to 6% by weight of aluminum ions. Further, the preferred concentration and amount of the aqueous solution used to remove the attached scale also depend on the conditions for contacting the solution with the scale. Usually, the chemical composition of the scale to be removed is not constant, but it is preferable that the above aqueous solution is brought into contact with the scale at a ratio of 10 to 10,000 parts by weight per 1 part by weight of the scale. According to the method of the present invention, the temperature of the aqueous solution when it is brought into contact with the scale is usually 0 to 80°C, preferably 5 to 40°C,
Particularly preferably, the temperature is about 10 to 25°C. In order to quickly dissolve the scale according to the method of the present invention, the aqueous solution may be brought into contact with the scale by spraying using a cleaning device in place, or the aqueous solution may be supplied into the fermentation device and the stored liquid may be stirred. Another method is to contact the The aqueous solution used in the present invention may include surfactants, alcohols, acids, esters, salts, corrosion inhibitors, etc., as long as the purpose of the present invention is achieved, in addition to the specific ions in the specific ratio. There is no problem even if a bactericide or the like is included. Further, the method of the present invention
It can also be carried out in combination with a conventional cleaning method using an alkaline aqueous solution and a sterilizing detergent, a cleaning method by bringing an acidic aqueous solution into contact with the scale, and the like. In addition, slurry obtained by further blending diatomaceous earth, other carriers, abrasives, etc.
Scale removal can also be carried out by contacting or applying a paste or the like to the scale surface. Next, preferred embodiments of the present invention will be illustrated. (1) Basic aluminum chloride, basic aluminum nitrate, basic aluminum sulfamate, or a mixture thereof, in a molar ratio of 1 to 2.5 moles of acid anion per 1 mole of aluminum ion, and 0.01 mole as aluminum ion. ~4
An aqueous solution obtained by dissolving in water in a proportion of % by weight is applied to a scale that is attached to the inner wall of the fermentation equipment.
Method of contact at 2-25℃. (2) Hydrochloric acid, nitric acid, sulfamic acid, or a mixture thereof and aluminum hydroxide in a molar ratio of 1 to 2 moles of anion of the above acid per mole of aluminum ion, and as aluminum ion.
The method of (1) above, wherein an aqueous solution obtained by dissolving in water at a ratio of 0.01 to 4% by weight is used instead of the aqueous solution in (1) above. The method of the present invention is used to dissolve and remove scale adhering to the inner wall of a fermentation apparatus in the beer manufacturing process, and the scale is mainly composed of calcium and oxalic acid, and also contains small amounts of other organic and inorganic substances. Since these main components are extremely well dissolved by the aqueous solution used in the present invention, it is thought that the tissue structure forming the scale is easily dissolved. The method of the present invention includes:
Extremely useful. The present invention will be described in more detail below with reference to Examples, but the technical scope of the present invention is not limited thereto. Example 1 1.00 g of scale (A) to be attached to the inner wall of a fermentation tank in a beer brewing factory was added to 100 g of the chemical solution listed in Table 1, and after stirring at 20°C for the time listed in the table, 0.6
The scale dissolution rate was determined by passing through a μ Millipore filter and weighing the excess residue. The above chemical solution was obtained by reacting and dissolving metallic aluminum and sulfamic acid in water so as to have the composition and concentration as shown in Experiment Nos. 1 to 3 in Table 1. The results are shown in Table 1.

【表】 実施例 2 実施例1に用いたものと同じスケール(A)0.5g
を、5%の塩基性塩化アルミニウム水溶液50g中
に投入し、20℃で2時間撹拌した後、0.6μのミ
リポアフイルターで未溶解分を別し、スケール
の溶解率を求めた。結果は第1表実験No.4に示
す。 実施例 3 実施例1に用いたものと同じスケール(A)0.5g
を塩基性硝酸アルミニウム水溶液50g中に投入
し、20℃で2時間撹拌し、0.6μのミリポアフイ
ルターで未溶解分を別し溶解率を求めた。結果
は、第1表実験No.5に示す。 実施例 4 麦酒醸造工場の醗酵タンク内壁に付着せる別の
スケール(B)の0.5gを5%塩基性スルフアミン酸
アルミニウム水溶液50g中に投入し第1表記載の
温度で2時間撹拌し、その後、0.6μのミリポア
フイルターで未溶解分を別し、溶解率を求め
た。結果は第1表実験No.6〜7に示す。 別に、本発明に用いられる水溶液及び比較対照
用の水溶液について、下記材質試験片に対する腐
食性試験を行つた。 試験片A:アルミニウム板(JIS H4000、#320
の研磨仕上)、厚さ、縦及び横の寸法はそれぞ
れ1mm、12mm及び75mmであり、アセトンにより
脱脂洗浄処理せるもの。 試験片B:砲金板(JIS H5111、#320の研磨仕
上)、厚さ、縦及び横の寸法はそれぞれ3mm、
12mm及び75mmであり、アセトンにより脱脂洗浄
処理せるもの。 試験片C:SUS304鋼板(JIS G4305、#320の研
磨仕上)、寸法、洗浄処理は試験片Aに同じ。 上記試験片Aを3箇、Bを3箇、及びCを3箇
それぞれ別に9箇の120mlのガラス容器中に立て
掛け、第2表記載の水溶液110gを試験片A、
B、Cの容器に個別に投入し、全面浸漬させた
まゝ20℃で6時間静置した後取り出し、流水で洗
浄した後、アセトン洗浄を行い、乾燥後秤量し減
量を算出し、第2表に示す結果を得た。
[Table] Example 2 Same scale as used in Example 1 (A) 0.5g
was poured into 50 g of a 5% aqueous basic aluminum chloride solution, stirred at 20°C for 2 hours, and undissolved matter was separated using a 0.6μ Millipore filter to determine the scale dissolution rate. The results are shown in Table 1, Experiment No. 4. Example 3 Same scale as used in Example 1 (A) 0.5g
was poured into 50 g of a basic aqueous aluminum nitrate solution, stirred at 20° C. for 2 hours, and undissolved components were separated using a 0.6μ Millipore filter to determine the dissolution rate. The results are shown in Table 1, Experiment No. 5. Example 4 0.5 g of another scale (B) to be attached to the inner wall of a fermentation tank in a beer brewing factory was put into 50 g of a 5% basic aluminum sulfamate aqueous solution, stirred for 2 hours at the temperature listed in Table 1, and then, Undissolved matter was separated using a 0.6μ Millipore filter, and the dissolution rate was determined. The results are shown in Table 1, Experiment Nos. 6 and 7. Separately, a corrosion test was conducted on the following material test pieces for the aqueous solution used in the present invention and the aqueous solution for comparison. Test piece A: Aluminum plate (JIS H4000, #320
Polished finish), thickness, vertical and horizontal dimensions are 1 mm, 12 mm and 75 mm, respectively, and are degreased and cleaned with acetone. Test piece B: Gunmetal plate (JIS H5111, #320 polished finish), thickness, vertical and horizontal dimensions each 3 mm,
12mm and 75mm, and can be degreased and cleaned with acetone. Test piece C: SUS304 steel plate (JIS G4305, #320 polished finish), dimensions and cleaning treatment are the same as test piece A. Three test pieces A, three test pieces B, and three test pieces C were placed in nine 120 ml glass containers, and 110 g of the aqueous solution listed in Table 2 was added to the test pieces A,
They were individually placed in containers B and C, left completely immersed at 20°C for 6 hours, then taken out, washed with running water, washed with acetone, dried and weighed to calculate the weight loss.Table 2 The results shown are obtained.

【表】 第2表に記載の如く、苛性ソーダ水溶液ではア
ルミニウム板の腐食が大であり、硝酸尿素では砲
金に腐食性がある。これに対し本発明に用いられ
る水溶液は、上記のいずれの材質に対しても腐食
性が小さく、充分に実用され得るものであること
を確認した。
[Table] As shown in Table 2, an aqueous solution of caustic soda greatly corrodes aluminum plates, and urea nitrate is corrosive to gunmetal. On the other hand, it was confirmed that the aqueous solution used in the present invention has low corrosiveness to any of the above-mentioned materials, and can be sufficiently put to practical use.

Claims (1)

【特許請求の範囲】 1 麦酒の製造工程における醗酵装置内壁に付着
せるスケールに、 塩素イオン、硝酸根、スルフアミン酸根からな
る群より選ばれる1種又は2種以上の陰イオンと
アルミニウムイオンを アルミニウムイオン1モルに対して上記陰イオ
ンが0.33モル以上3モル未満の割合に共存させた
水溶液を接触させることを特徴とする前記スケー
ルの除去方法。 2 水溶液がアルミニウムとして0.001〜12.4重
量%含む水溶液である特許請求の範囲第1項に記
載のスケールの除去方法。 3 スケールに接触させる水溶液の温度が0〜50
℃である特許請求の範囲第1項又は第2項に記載
のスケールの除去方法。 4 水溶液が、塩基性塩化アルミニウム、塩基性
硝酸アルミニウム、塩基性スルフアミン酸アルミ
ニウム又は、これらの混合物を水に溶解すること
により調製されるものである特許請求の範囲第1
項、第2項又は第3項に記載のスケールの除去方
法。 5 水溶液が塩酸、硝酸、スルフアミン酸又はこ
れらの混合物と水酸化アルミニウムを水に溶解す
ることにより調製されたものである特許請求の範
囲第1項、第2項又は第3項に記載のスケールの
除去方法。
[Claims] 1. One or more anions selected from the group consisting of chloride ions, nitrate radicals, and sulfamic acid radicals and aluminum ions are added to the scale attached to the inner wall of fermentation equipment in the beer manufacturing process. The method for removing scale as described above, comprising contacting with an aqueous solution in which the above-mentioned anions coexist at a ratio of 0.33 mol or more and less than 3 mol per 1 mol. 2. The method for removing scale according to claim 1, wherein the aqueous solution contains 0.001 to 12.4% by weight of aluminum. 3 The temperature of the aqueous solution in contact with the scale is 0 to 50
The method for removing scale according to claim 1 or 2, wherein the temperature is .degree. 4. Claim 1, wherein the aqueous solution is prepared by dissolving basic aluminum chloride, basic aluminum nitrate, basic aluminum sulfamate, or a mixture thereof in water.
The method for removing scale according to item 2, item 3, or item 3. 5. The scale according to claim 1, 2 or 3, wherein the aqueous solution is prepared by dissolving hydrochloric acid, nitric acid, sulfamic acid or a mixture thereof and aluminum hydroxide in water. Removal method.
JP2864479A 1979-03-14 1979-03-14 Scale removing method Granted JPS55121896A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2864479A JPS55121896A (en) 1979-03-14 1979-03-14 Scale removing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2864479A JPS55121896A (en) 1979-03-14 1979-03-14 Scale removing method

Publications (2)

Publication Number Publication Date
JPS55121896A JPS55121896A (en) 1980-09-19
JPS6250199B2 true JPS6250199B2 (en) 1987-10-23

Family

ID=12254216

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2864479A Granted JPS55121896A (en) 1979-03-14 1979-03-14 Scale removing method

Country Status (1)

Country Link
JP (1) JPS55121896A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004066159A (en) * 2002-08-08 2004-03-04 Daisan Kogyo Kk Method of sterilizing and washing material to be washed in foodstuff manufacturing facility

Also Published As

Publication number Publication date
JPS55121896A (en) 1980-09-19

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