JPS6060905A - Manufacture of peroxide having superior disintegrability in water - Google Patents

Manufacture of peroxide having superior disintegrability in water

Info

Publication number
JPS6060905A
JPS6060905A JP16415183A JP16415183A JPS6060905A JP S6060905 A JPS6060905 A JP S6060905A JP 16415183 A JP16415183 A JP 16415183A JP 16415183 A JP16415183 A JP 16415183A JP S6060905 A JPS6060905 A JP S6060905A
Authority
JP
Japan
Prior art keywords
peroxide
water
granular
disintegrability
superior
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
JP16415183A
Other languages
Japanese (ja)
Other versions
JPS6319441B2 (en
Inventor
Ryuichi Kayama
隆一 香山
Eiji Usu
薄 栄司
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.)
Nippon Peroxide Co Ltd
Original Assignee
Nippon Peroxide 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 Nippon Peroxide Co Ltd filed Critical Nippon Peroxide Co Ltd
Priority to JP16415183A priority Critical patent/JPS6060905A/en
Publication of JPS6060905A publication Critical patent/JPS6060905A/en
Publication of JPS6319441B2 publication Critical patent/JPS6319441B2/ja
Granted legal-status Critical Current

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  • Detergent Compositions (AREA)
  • Agricultural Chemicals And Associated Chemicals (AREA)

Abstract

PURPOSE:To obtain a granular peroxide having superior disintegrability in water by adding a water soluble polymer contg. acylic acid (deriv.) as a monomer component and having a specified average degree of polymn. to a powdery peroxide when the peroxide is granulated. CONSTITUTION:A water-soluble polymer contg. acrylic acid (deriv.) as a monomer component and having <=10,000 average degree of polymn., e.g., sodium polyacrylate is added to powder of a peroxide such as sodium percarbonate or sodium perborate by about 0.1-1% of the amount of the peroxide. An adequate amount of water is added to the mixture, and they are kneaded, extruded with an extrusion granulator, and dried with a fluidized drying machine to obtain the desired granular peroxide having superior disintegrability in water. The granular peroxide is suitable for use as a bleaching agent, a disinfectant or the like.

Description

【発明の詳細な説明】 本発明は、水中における崩壊拡展性のすぐれた顆粒状過
酸化物の製造方法に関するものでちる。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing granular peroxide having excellent disintegration and spreading properties in water.

本発明における過酸化物とは、過炭酸ソーダ。The peroxide in the present invention is soda percarbonate.

過炭酸ソーダ、硫酸ナトリウム塩化ナトリウム過酸化水
素付加物等の過酸化水素誘導体を言う。
Refers to hydrogen peroxide derivatives such as sodium percarbonate, sodium sulfate, sodium chloride, and hydrogen peroxide adducts.

これら過酸化物は、酸素系漂白剤、あるいは殺菌剤とし
て工業的に有用な物質であるが、これらの用途面におい
て優れた効果を発揮するためには、水中において速かに
溶解する必要があり、そのた非分 めに数体状過酸化物を造粒して顆粒状とするのが好まし
い。
These peroxides are industrially useful substances as oxygen bleaches or disinfectants, but in order to be effective in these applications, they must dissolve quickly in water. In addition, it is preferable to granulate the several-dimensional peroxide without dividing it into granules.

過酸化物の造粒に用いられる造粒機としては、適当なバ
インダー及び水の存在下に、ニーグーで混線後、多孔板
から押出す押出造粒機、あるいはヘンシエルミキザー、
グラニユレータ−等の混合造粒機が一般的に用いられて
いる。
The granulator used for granulating peroxide is an extrusion granulator that mixes the mixture with a niegu in the presence of a suitable binder and water and then extrudes it from a perforated plate, or a Henschel mixer.
Mixing granulators such as granulators are commonly used.

また、適当な圧力のかかるニーターを用いて混練、混和
して一度ある程度の大きさに成形した後、破砕機で破砕
造粒するような造粒方法も提案されている。
Furthermore, a granulation method has also been proposed in which the mixture is kneaded and mixed using a kneader that applies appropriate pressure, is once formed into a certain size, and is then crushed and granulated using a crusher.

しかしながら、これらの造粒方法で単に造粒した過酸化
物は、水中に投じた時の崩壊性が悪く溶解速度も遅い。
However, peroxide simply granulated by these granulation methods has poor disintegration properties and slow dissolution rate when thrown into water.

低温水において溶解速度の速い過酸化物を得るためには
、優れた崩壊剤を添加する事が不可決である。
In order to obtain a peroxide with a high dissolution rate in low temperature water, it is essential to add a good disintegrant.

本発明者らは、顆粒状過酸化物を水中に投じた時に、速
かに崩壊2分散し、もって速かに溶解せしめる事が出来
る添加剤を種々検討した結果、本発明を完成するに至っ
た。
The present inventors have completed the present invention after studying various additives that can quickly disintegrate and disperse granular peroxide when it is thrown into water, thereby quickly dissolving it. Ta.

すなわち、本発明は、粉体状過酸化物を造粒するに際し
、アクリル酸あるいはアクリル酸誘導体?単量体とする
水溶性重合体で、平均重合度が1oooo以下のものを
添加する事を特徴とする水中崩壊性の優れた過酸化物の
製造方法である。
That is, the present invention uses acrylic acid or acrylic acid derivatives when granulating powdered peroxide. This is a method for producing a peroxide having excellent disintegration in water, which is characterized by adding a water-soluble polymer as a monomer having an average degree of polymerization of 1oooo or less.

本発明の方法において用られる重合体の代表例としては
、比較的低分子量のポリアクリル酸ンーグでアシ、商品
名「トキサノン」(三洋化成工業)として市販されてい
る。添加量としては、原体である過炭酸ソーダに対して
0.01〜5.0%の範囲で使用可能であるが、好まし
くは、11〜1.0俤が良い。
A typical example of the polymer used in the method of the present invention is polyacrylic acid having a relatively low molecular weight and is commercially available under the trade name "Toxanone" (Sanyo Chemical Industries, Ltd.). The amount added can range from 0.01 to 5.0% based on the raw material, sodium percarbonate, but preferably 11 to 1.0%.

本発明の方法において用いられる重合体は、崩壊剤とし
てばかりでなく、結合剤としても優れており、従来造粒
する際に添加していたCMC,あるいは水ガラス等を特
に添加しなくても十分の強度を有する粒剤を作る事がで
きる。もちろんこれら結合剤と並用する事も可能である
The polymer used in the method of the present invention is excellent not only as a disintegrating agent but also as a binder, and can be used without the need for CMC or water glass, which were conventionally added during granulation. It is possible to make granules with a strength of Of course, it is also possible to use these binders together.

従来、造粒物の崩壊剤としては、繊維素グリコール酸ナ
トリウム(CMC)、繊維素グリコール酸カルシウム、
デンプン等が知られている。これら従来の崩壊剤の崩壊
機構としては、水中において、崩壊剤が膨潤するため顆
粒が分裂するためであろうと考えられている。
Conventionally, disintegrants for granules include cellulose sodium glycolate (CMC), cellulose calcium glycolate,
Starch etc. are known. It is thought that the disintegration mechanism of these conventional disintegrants is that the disintegrants swell in water, causing the granules to split.

本発明の方法によって得た顆粒状過酸化物はこれら従来
の添加物を使用したものに比べ、一段と水中における崩
壊性、溶解性にすぐれ、顆粒を水中に投じた時、極めて
速かに粒の分裂が起るのが見られる。この機構について
は良く解っていないが、おそらく添加重合体によるイオ
ン釣力反撥によるものと思われ、従来の崩壊剤が膨潤す
るのに必要な時間に比べ、極めて速かに現象が進むもの
と考えられる。
The granular peroxide obtained by the method of the present invention has better disintegration and solubility in water than those using these conventional additives, and when the granules are thrown into water, the granules disintegrate very quickly. You can see a split occur. The mechanism of this is not well understood, but it is probably due to ion tension repulsion by the added polymer, and it is thought that the phenomenon progresses extremely quickly compared to the time required for conventional disintegrants to swell. It will be done.

以下に、実施例と比較例をもって、本発明の具体的方法
を説明する。
The specific method of the present invention will be explained below with reference to Examples and Comparative Examples.

以下で述べる「崩壊深度」とは、直径15crn。The "collapse depth" described below is a diameter of 15 crn.

状 高さ60鋼の円筒ホのガラス容器に、高さ50crnま
で20℃の純水を入れ、水面上高さ5crnの所から検
体−粒を自然落下させて水中に投じ、水中において、検
体が分裂するのを肉眼で観測し、その時の水面からの深
さを副単位で表現したものであり、30回の測定をくフ
返した平均値を用いている。
Fill a cylindrical glass container with a height of 60 steel with pure water at 20°C to a height of 50 crn, and let the sample particles fall naturally from a height of 5 crn above the water surface and drop them into the water. The splitting is observed with the naked eye, and the depth from the water surface at that time is expressed in subunits, and the average value of 30 measurements is used.

実施例 造粒は、次の3種類の方法A、B、Cで行い、添加剤は
、各々過酸化物に対して1%用い、第1表の結果を得た
Example granulation was carried out using the following three methods A, B, and C, and each additive was used in an amount of 1% based on the peroxide, and the results shown in Table 1 were obtained.

方法A 過酸化物の粉体に添加剤を加え、含水率が14襲となる
ように水分を調節し、混線機によって十分混合した後、
直径0.5 tan 96のスクリーンを取シ付けた押
出し造粒機によシ押出し、流動乾燥機によって乾燥し、
過酸化物の造粒物を得た。標準ふるいで篩分し、24メ
ツシユpass〜60メツシユONのもの全試料とした
Method A: Add additives to peroxide powder, adjust the moisture content so that the moisture content is 14%, mix thoroughly with a mixer, and then
It was extruded through an extrusion granulator equipped with a screen with a diameter of 0.5 tan 96, and dried using a fluidized fluid dryer.
Granules of peroxide were obtained. It was sieved using a standard sieve, and all samples with 24 mesh pass to 60 mesh ON were used.

方法B 過酸化物の粉体に対し、含水率が18チとなるような水
に、添加剤を溶解しておく。
Method B: Dissolve the additive in water such that the peroxide powder has a water content of 18%.

混合攪拌造粒機に過酸化物の粉体を入れ、攪拌しながら
上記添加剤水溶液を噴霧し、20分間攪拌を続けて造粒
物を得る。その後は、方法Aと同様に処理した。
The peroxide powder is put into a mixing agitation granulator, and the above additive aqueous solution is sprayed while stirring, and stirring is continued for 20 minutes to obtain a granulated product. Thereafter, the same treatment as method A was performed.

方法C 過酸化物の粉体に対して、含水率が18%となるような
水に添加剤を溶解しておく。
Method C: Dissolve the additive in water such that the moisture content of the peroxide powder is 18%.

原体過酸化物と上記水溶液を、加圧型ニーダ−に投入し
て、良く混練し、た後、直径20画、高さ30crnの
破砕室を有する破砕室に8枚の十字型カッターを取シ付
けたもので300゜rpmの回転数にて破砕した。以後
は、方法人と同様に処理した。
The raw peroxide and the above aqueous solution were put into a pressurized kneader and kneaded well. After that, eight cross-shaped cutters were installed in a crushing chamber having a diameter of 20 cm and a height of 30 crn. The material was crushed at a rotation speed of 300° rpm. Thereafter, the process was carried out in the same manner as the method.

比較例 添加剤を変えた他は、実施例と同様にして第2表の結果
を得だ。
Comparative Example The results shown in Table 2 were obtained in the same manner as in the Examples except that the additives were changed.

Claims (1)

【特許請求の範囲】[Claims] 1、粉体状過酸化物を造粒して、顆粒状過酸化物を製造
する際、アクリル酸あるいはアクリル酸誘導体を単量体
とする水溶性重合体で平均重合度
1. When producing granular peroxide by granulating powdered peroxide, the average degree of polymerization is
JP16415183A 1983-09-08 1983-09-08 Manufacture of peroxide having superior disintegrability in water Granted JPS6060905A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16415183A JPS6060905A (en) 1983-09-08 1983-09-08 Manufacture of peroxide having superior disintegrability in water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16415183A JPS6060905A (en) 1983-09-08 1983-09-08 Manufacture of peroxide having superior disintegrability in water

Publications (2)

Publication Number Publication Date
JPS6060905A true JPS6060905A (en) 1985-04-08
JPS6319441B2 JPS6319441B2 (en) 1988-04-22

Family

ID=15787706

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16415183A Granted JPS6060905A (en) 1983-09-08 1983-09-08 Manufacture of peroxide having superior disintegrability in water

Country Status (1)

Country Link
JP (1) JPS6060905A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0200163A2 (en) * 1985-05-02 1986-11-05 Henkel Kommanditgesellschaft auf Aktien Bleaching agent, its preparation and its use
JPS63215502A (en) * 1987-03-03 1988-09-08 Nippon Peroxide Co Ltd Production of stabilized sodium percarbonate
JPH01153510A (en) * 1987-12-11 1989-06-15 Nippon Peroxide Co Ltd Production of stabilized sodium percarbonate
US9775402B2 (en) 2012-05-10 2017-10-03 Asics Corporation Shoe sole having outsole and midsole

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5315716A (en) * 1976-07-28 1978-02-14 Gen Corp System for indicating layout data of newspaper or the like
DE2652488A1 (en) * 1976-11-18 1978-05-24 Kali Chemie Ag Granulate builders for cleansing and detergent compsns. - prepd. from zeolite and oxygen-generating cpd. in presence of water
JPS5771891A (en) * 1980-10-16 1982-05-04 Toho Chem Ind Co Ltd Manufacture of granular fertilizer
JPS58132093A (en) * 1981-11-16 1983-08-06 ザ・プロクタ−・エンド・ギヤンブル・カンパニ− Granular detergent composition containing tightly mixed anionic surfactant and anionic polymer

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5315716A (en) * 1976-07-28 1978-02-14 Gen Corp System for indicating layout data of newspaper or the like
DE2652488A1 (en) * 1976-11-18 1978-05-24 Kali Chemie Ag Granulate builders for cleansing and detergent compsns. - prepd. from zeolite and oxygen-generating cpd. in presence of water
JPS5771891A (en) * 1980-10-16 1982-05-04 Toho Chem Ind Co Ltd Manufacture of granular fertilizer
JPS58132093A (en) * 1981-11-16 1983-08-06 ザ・プロクタ−・エンド・ギヤンブル・カンパニ− Granular detergent composition containing tightly mixed anionic surfactant and anionic polymer

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0200163A2 (en) * 1985-05-02 1986-11-05 Henkel Kommanditgesellschaft auf Aktien Bleaching agent, its preparation and its use
EP0200163B1 (en) * 1985-05-02 1989-10-04 Henkel Kommanditgesellschaft auf Aktien Bleaching agent, its preparation and its use
JPS63215502A (en) * 1987-03-03 1988-09-08 Nippon Peroxide Co Ltd Production of stabilized sodium percarbonate
JPH051205B2 (en) * 1987-03-03 1993-01-07 Nippon Peroxide Co Ltd
JPH01153510A (en) * 1987-12-11 1989-06-15 Nippon Peroxide Co Ltd Production of stabilized sodium percarbonate
JPH0524848B2 (en) * 1987-12-11 1993-04-09 Nippon Peroxide Co Ltd
US9775402B2 (en) 2012-05-10 2017-10-03 Asics Corporation Shoe sole having outsole and midsole

Also Published As

Publication number Publication date
JPS6319441B2 (en) 1988-04-22

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