JPH0710507A - Method for granulating sodium percarbonate - Google Patents

Method for granulating sodium percarbonate

Info

Publication number
JPH0710507A
JPH0710507A JP14921893A JP14921893A JPH0710507A JP H0710507 A JPH0710507 A JP H0710507A JP 14921893 A JP14921893 A JP 14921893A JP 14921893 A JP14921893 A JP 14921893A JP H0710507 A JPH0710507 A JP H0710507A
Authority
JP
Japan
Prior art keywords
water
sodium carbonate
granulation
sodium percarbonate
sodium
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
Application number
JP14921893A
Other languages
Japanese (ja)
Inventor
Hiromi Sasaki
広美 佐々木
Yoji Ueda
洋史 上田
Yasushi Muneno
靖 宗野
Sunao Yamamoto
素直 山本
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.)
Central Glass Co Ltd
Original Assignee
Central Glass 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 Central Glass Co Ltd filed Critical Central Glass Co Ltd
Priority to JP14921893A priority Critical patent/JPH0710507A/en
Publication of JPH0710507A publication Critical patent/JPH0710507A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To efficiently granulate sodium percarbonate by mixing sodium carbonate being a diluent and water for granulation with sodium percarbonate and granulating them while heating to and keeping at a specific temp. CONSTITUTION:A mixer, a granulator, a transporter and the like are heat- insulated or heated and sodium percarbonate, sodium carbonate being the diluent and water required for granulation are mixed at 36-80 deg.C. Next, the mixture is supplied to and granulated by the granulator while keeping the temp. range. Thus, the mixing and granulation are executed while keeping temp. at 36-80 deg.C, Na2CO3.7H2O or Na2CO3.10H2O does not produced by the hydration of sodium carbonate at the time of adding sodium carbonate and water into sodium percarbonate, therefore the added water is not absorbed into sodium carbonate as crystllization water. As a result, the granulation is executed by adding the absolute minimum amounts of water necessitated for granulation so that granulation is efficiently executed without evaporating and drying unnecessary water at the time of 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、過炭酸ソーダの造粒方
法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for granulating sodium percarbonate.

【0002】[0002]

【従来技術】過炭酸ソーダは過ホウ酸ソーダとならび代
表的な酸素系漂白剤であり、塩素系漂白剤に比較して漂
白効果は若干劣るが、その漂白作用は温和であり、合成
繊維や動植物繊維さらには染色された繊維に対しても布
地を損ねたり、色落ちがない、さらに、塩素の急激な発
生による危険性も全く無いなどの特徴を持つため家庭
用、業務用の漂白剤として非常に有用である。
BACKGROUND OF THE INVENTION Sodium percarbonate is a typical oxygen-based bleaching agent as well as sodium perborate, and its bleaching effect is slightly inferior to that of chlorine-based bleaching agents, but its bleaching effect is mild and synthetic fibers and As a bleaching agent for household and business use, it has the characteristics that it does not damage the fabric of animal and plant fibers or dyed fibers, does not lose color, and has no danger due to the rapid generation of chlorine. Very useful.

【0003】過炭酸ソーダ自体は可然物ではなく単独で
安全な化合物であるが、可然物と混合された場合になん
らかの影響により急激に酸素を発生し、燃焼を促進する
ことがある。このため、通常種々の化合物を添加・希釈
し、有効酸素含量を低下させて危険性を低減させるとい
う方法が行われている。希釈剤としては炭酸水素ナトリ
ウム、炭酸ナトリウム、硫酸ナトリウム等の水溶性の無
機塩類が通常よく用いられる。ところが、これらの無機
塩類の内、危険性の低減効果が大きくしかも比較的安価
であり希釈剤として有用性の高い炭酸ナトリウムを用い
た場合において、過炭酸ソーダと炭酸ナトリウムを混合
し、造粒する場合に、水を添加して混合・造粒しようと
すると、希釈剤の炭酸ナトリウムが水和し、Na2 CO
3 ・7H 2 OもしくはNa2 CO3 ・10H2 Oという
形になって炭酸ナトリウム1Kgあたり1.2〜1.7
Kgもの水分を吸収してしまう。この状態で造粒するた
めにはさらに過剰量の水を添加して造粒し、乾燥時には
逆に大量の水を蒸発・乾燥する必要があり非常に効率の
悪い造粒方法となるのが欠点であった。特に外気温が低
下する冬季においては効率の低下が顕著であった。
Sodium percarbonate itself is not inevitable
It's a safe compound, but what if it's mixed with intangibles?
Oxygen is suddenly generated due to some influence to accelerate combustion
Sometimes. For this reason, various compounds are usually added and diluted.
However, it is said that the effective oxygen content is reduced to reduce the risk.
The method is done. Natricarbonate as a diluent
Water-soluble substances such as sodium, sodium carbonate, and sodium sulfate
Machine salts are usually used. However, these inorganic
Greater risk reduction effect among salts, and relatively inexpensive
Sodium carbonate, which is highly useful as a diluent,
Mix sodium carbonate and sodium carbonate
When granulating, try adding water to mix and granulate.
Then, the diluent sodium carbonate is hydrated and Na2CO
3・ 7H 2O or Na2CO3・ 10H2Called O
Formed into 1.2-1.7 per 1 kg of sodium carbonate
It absorbs as much as Kg of water. Granulate in this state
For this purpose, add an excess amount of water and granulate.
On the contrary, it is necessary to evaporate and dry a large amount of water, which is very efficient.
The disadvantage is that it is a poor granulation method. Especially low outside temperature
The decrease in efficiency was remarkable in the winter.

【0004】[0004]

【問題点を解決するための具体的手段】本発明者らはか
かる問題を解決すべく鋭意研究した結果、本発明を完成
するに至った。すなわち、本発明は該混合物を造粒する
に際して該混合物の温度を炭酸ナトリウムが大量の結晶
水を吸収する温度以上に常時保ち、混合・造粒すること
によって必要最小限の水を添加し造粒出来、乾燥時にも
不必要な水を蒸発・乾燥することなく効率のよい造粒を
行なうことが可能となった。
[Means for Solving the Problems] The present inventors have completed the present invention as a result of intensive studies to solve the above problems. That is, in the present invention, when granulating the mixture, the temperature of the mixture is constantly maintained at a temperature higher than the temperature at which sodium carbonate absorbs a large amount of water of crystallization, and by mixing and granulating, a minimum amount of water is added to granulate the mixture. As a result, it is possible to perform efficient granulation without evaporating and drying unnecessary water during drying.

【0005】炭酸ナトリウムは表1に示す様に35.1
℃を境として1水塩から7水塩に転移し、さらに、3
2.0℃以下で10水塩となり大量の水を吸収すること
が知られている。
Sodium carbonate is 35.1 as shown in Table 1.
The transition from monohydrate to heptahydrate occurs at ℃, and further 3
It is known that it becomes a 10-hydrate salt at 2.0 ° C or lower and absorbs a large amount of water.

【0006】[0006]

【表1】 [Table 1]

【0007】造粒のために混合された過炭酸ソーダと炭
酸ナトリウムと水がこの35.1℃以下に冷却されると
急激に水分が炭酸ナトリウムに吸収され見かけ状の水分
が低下する。このため、造粒するためにはさらに水を添
加して見かけ状の水分を造粒に適した水分、通常10〜
15%であるが、に調整しなければならない。しかし、
本発明の方法すなわち該混合物の温度が36℃以下に低
下しない様に、造粒のための混合機、造粒機、輸送機等
を保温あるいは加温することによって該混合物の温度を
36℃以上、好ましくは40℃以上に保つことによって
炭酸ナトリウムが水和して10水塩になることを防ぎ、
効率のよい造粒方法を提供することが可能となった。こ
こで、該混合物の温度を80℃以上の高温にすると含ま
れる過炭酸ソーダが分解し有効酸素含量の低下を引き起
こすため、該混合物の温度は80℃以下が好ましい。
When the sodium percarbonate, sodium carbonate and water mixed for granulation are cooled to below 35.1 ° C., the water content is rapidly absorbed by the sodium carbonate and the apparent water content is lowered. Therefore, for granulation, water is further added to give an apparent water content, which is usually 10 to 10.
It is 15%, but it must be adjusted to. But,
In order to prevent the temperature of the mixture of the present invention from falling below 36 ° C., the temperature of the mixture is kept above 36 ° C. by keeping or warming the mixing machine for granulation, granulating machine, transporting machine, etc. , It is preferable to prevent the sodium carbonate from hydrating to decahydrate by keeping it at 40 ° C or higher,
It has become possible to provide an efficient granulation method. Here, the temperature of the mixture is preferably 80 ° C. or lower because the sodium percarbonate contained therein is decomposed when the temperature of the mixture is raised to a high temperature of 80 ° C. or higher and the effective oxygen content is lowered.

【0008】過炭酸ソーダと炭酸ナトリウムの混合物に
造粒のための水を添加すると、まず、炭酸ナトリウムが
水和してNa2 CO3 ・H2 Oとなり、その時炭酸ナト
リウム1Kg当たり30Kcalの熱量が発生する。こ
の熱量は、炭酸ナトリウムの添加割合にも影響される
が、夏期であれば混合物の温度を35.1℃以上に引き
上げることは可能である。しかし、秋から春にかけて気
温の低い時期には出発物の温度が低く、また、外気温が
低いために混合物が冷却されて混合・造粒を行なう最中
に水和が進行し、造粒が困難となり、造粒水の追加が必
要となる場合がある。しかし、本発明の方法により混合
機、造粒機の外壁を2重のジャケット構造とするなどし
て、電熱、温水、蒸気等の方法により保温もしくは加温
することにより炭酸ナトリウムの水和を阻止し、造粒水
の追加を必要とすることなく造粒が可能となった。本発
明において使用する混合機、造粒機の方式については制
限されることなく実施可能である。また、保温、加温の
方法や熱媒についても該混合物の温度を36〜70℃に
保つことが出来るならば何れの方法および熱媒を用いて
も構わない。
When water for granulation is added to the mixture of sodium percarbonate and sodium carbonate, first, sodium carbonate is hydrated to Na 2 CO 3 .H 2 O, at which time the heat of 30 Kcal per 1 kg of sodium carbonate is obtained. appear. This amount of heat is affected by the addition ratio of sodium carbonate, but it is possible to raise the temperature of the mixture to 35.1 ° C. or higher in the summer. However, the temperature of the starting materials is low during the low temperature period from autumn to spring, and because the outside air temperature is low, the mixture is cooled and hydration proceeds during mixing and granulation, resulting in granulation. It may be difficult and additional granulation water may be required. However, hydration of sodium carbonate is prevented by keeping the temperature of the mixer or granulator by a double jacket structure by the method of the present invention, or by heating or warming it by a method such as electric heat, hot water or steam. However, it became possible to granulate without the need to add granulating water. The system of the mixer and the granulator used in the present invention can be practiced without any limitation. As for the method of heat retention and heating and the heat medium, any method and heat medium may be used as long as the temperature of the mixture can be maintained at 36 to 70 ° C.

【0009】本発明において使用される過炭酸ソーダは
晶出法、流動層法等何れの方法によって得られたもので
も構わない。また、希釈剤として使用される炭酸ナトリ
ウムは造粒するという目的ためには粒子径の小さな粉体
状のものが好ましいがこれに限定されない。さらに、通
常過炭酸ソーダの保存安定性能や漂白性能等の改善のた
めに添加される添加物についても同様に使用できる。
The sodium percarbonate used in the present invention may be obtained by any method such as a crystallization method and a fluidized bed method. Further, sodium carbonate used as a diluent is preferably in the form of powder having a small particle diameter for the purpose of granulating, but is not limited to this. Further, the additives which are usually added to improve the storage stability and bleaching performance of sodium percarbonate can also be used.

【0010】[0010]

【実施例】以下、実施例により本発明を説明する。 実施例1 粉末状過炭酸ソーダ4Kgと粉末状炭酸ナトリウム1K
gおよび水0.9Kgを1軸撹拌式混合機を用いて15
分間混合し、該混合物を2軸押し出し式造粒機(不二パ
ウダル(株))を用いて造粒した。乾燥前の造粒物の温
度は41℃であった。引続き、該造粒物を流動層式乾燥
機を用いて乾燥した。乾燥に要した時間は12分であっ
た。全ての工程において各機器は問題なく動作し、得ら
れた造粒物は漂白剤として良好に使用可能であった。
EXAMPLES The present invention will be described below with reference to examples. Example 1 4 kg of powdered sodium percarbonate and 1 K of powdered sodium carbonate
15 g of water and 0.9 kg of water using a uniaxial stirring mixer
After mixing for a minute, the mixture was granulated using a twin-screw extrusion type granulator (Fuji Paudal Co., Ltd.). The temperature of the granulated product before drying was 41 ° C. Subsequently, the granulated product was dried using a fluidized bed dryer. The time required for drying was 12 minutes. Each device worked without any problem in all steps, and the obtained granules were successfully used as a bleaching agent.

【0011】なお、この時の気温は10℃で、用いた過
炭酸ソーダ、炭酸ナトリウム、水の温度は何れも10℃
であった。さらに、用いた混合機、造粒機はジャケット
式の加温装置を装備してあり、ジャケットには50℃の
温水を循環して加温した。
At this time, the temperature is 10 ° C., and the temperatures of the sodium percarbonate, sodium carbonate and water used are all 10 ° C.
Met. Furthermore, the mixer and granulator used were equipped with a jacket-type heating device, and warm water of 50 ° C. was circulated in the jacket for heating.

【0012】比較例1 実施例1と同様に、粉末状過炭酸ソーダ4Kgと粉末状
炭酸ナトリウム1Kgおよび水0.9Kgを1軸撹拌式
混合機を用いて15分間混合した。混合途中から混合物
の見かけの水分が少なくなり、サラサラの粉体状となっ
た。該混合物を2軸押し出し式造粒機(不二パウダル
(株))を用いて造粒しようとしたが、造粒機から押し
出すことが困難であった。造粒前の混合物の温度は28
℃であった。
Comparative Example 1 As in Example 1, 4 kg of powdered sodium percarbonate, 1 kg of powdered sodium carbonate and 0.9 kg of water were mixed for 15 minutes using a uniaxial stirring mixer. From the middle of mixing, the apparent water content of the mixture decreased, and it became a dry powder. The mixture was tried to be granulated using a twin-screw extrusion type granulator (Fuji Paudal Co., Ltd.), but it was difficult to extrude the mixture from the granulator. The temperature of the mixture before granulation is 28
It was ℃.

【0013】なお、この時の気温は10℃であり用いた
過炭酸ソーダ、炭酸ナトリウム、水の温度は何れも10
℃であった。さらに、用いた混合機、造粒機には保温装
置および加温装置を装備していなかった。
The temperature at this time was 10 ° C., and the temperatures of the sodium percarbonate, sodium carbonate and water used were all 10
It was ℃. Furthermore, the mixer and granulator used were not equipped with a heat retention device and a heating device.

【0014】比較例2 粉末状過炭酸ソーダ4Kgと粉末状炭酸ナトリウム1K
gおよび水0.9Kgを1軸撹拌式混合機を用いて混合
した。混合開始後徐々に見かけの水分が低下してきたた
め、さらに、1.5Kgの水を徐々に追加し引続き混合
した。15分間の混合を行なった後、該混合物を2軸押
し出し式造粒機(不二パウダル(株))を用いて造粒し
た。乾燥前の造粒物の温度は26℃であった。引続き、
該造粒物を流動層式乾燥機を用いて乾燥した。乾燥に要
した時間は28分であった。得られた造粒物は漂白剤と
して良好に使用可能であった。 なお、この時の気温は
10℃であり用いた過炭酸ソーダ、炭酸ナトリウム、水
の温度は何れも10℃であった。さらに、用いた混合
機、造粒機には保温装置および加温装置を装備していな
かった。
Comparative Example 2 4 Kg of powdered sodium percarbonate and 1 K of powdered sodium carbonate
g and 0.9 Kg of water were mixed using a uniaxial stirring mixer. Since the apparent water content gradually decreased after the mixing was started, 1.5 kg of water was gradually added and the mixing was continued. After mixing for 15 minutes, the mixture was granulated using a twin-screw extrusion type granulator (Fuji Paudal Co., Ltd.). The temperature of the granulated product before drying was 26 ° C. Continued,
The granulated product was dried using a fluidized bed dryer. The time required for drying was 28 minutes. The obtained granulated product was successfully used as a bleaching agent. The temperature at this time was 10 ° C, and the temperatures of sodium percarbonate, sodium carbonate and water used were all 10 ° C. Furthermore, the mixer and granulator used were not equipped with a heat retention device and a heating device.

【0015】[0015]

【発明の効果】本発明により過炭酸ソーダの造粒に際
し、添加する水分量を大幅に減少させることを可能に
し、経済的効果は大きいものである。
INDUSTRIAL APPLICABILITY According to the present invention, it is possible to significantly reduce the amount of water added when granulating sodium percarbonate, and the economic effect is great.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 山本 素直 山口県宇部市大字沖宇部5253番地 セント ラル硝子株式会社宇部研究所内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Moto Naoyama, Inoue Yamaguchi Prefecture, Ube City 5253 Oki Ube Central Glass Co., Ltd. Ube Laboratory

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 過炭酸ソーダに炭酸ナトリウムを添加
し、造粒・乾燥する際に、過炭酸ソーダと炭酸ナトリウ
ムおよび造粒のための添加水との混合物を保温もしくは
加温し、36〜80℃に保つことを特徴とする過炭酸ソ
ーダの造粒方法。
1. When sodium carbonate is added to sodium percarbonate and the mixture is granulated and dried, a mixture of sodium percarbonate, sodium carbonate and added water for granulation is kept warm or heated to 36-80. A method for granulating sodium percarbonate, which is characterized by maintaining at ℃.
JP14921893A 1993-06-21 1993-06-21 Method for granulating sodium percarbonate Pending JPH0710507A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14921893A JPH0710507A (en) 1993-06-21 1993-06-21 Method for granulating sodium percarbonate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14921893A JPH0710507A (en) 1993-06-21 1993-06-21 Method for granulating sodium percarbonate

Publications (1)

Publication Number Publication Date
JPH0710507A true JPH0710507A (en) 1995-01-13

Family

ID=15470439

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14921893A Pending JPH0710507A (en) 1993-06-21 1993-06-21 Method for granulating sodium percarbonate

Country Status (1)

Country Link
JP (1) JPH0710507A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003523915A (en) * 2000-02-21 2003-08-12 ソルヴェイ Process for the preparation of coated alkali metal percarbonates, coated alkali metal percarbonates obtained by this process, their use in detergent formulations and detergent formulations containing them

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003523915A (en) * 2000-02-21 2003-08-12 ソルヴェイ Process for the preparation of coated alkali metal percarbonates, coated alkali metal percarbonates obtained by this process, their use in detergent formulations and detergent formulations containing them

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