JPS5983912A - Production of stable sodium percarbonate - Google Patents

Production of stable sodium percarbonate

Info

Publication number
JPS5983912A
JPS5983912A JP19361482A JP19361482A JPS5983912A JP S5983912 A JPS5983912 A JP S5983912A JP 19361482 A JP19361482 A JP 19361482A JP 19361482 A JP19361482 A JP 19361482A JP S5983912 A JPS5983912 A JP S5983912A
Authority
JP
Japan
Prior art keywords
borate
water
percarbonate
sodium
powder
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
JP19361482A
Other languages
Japanese (ja)
Other versions
JPS621563B2 (en
Inventor
Mutsumi Kuroda
睦 黒田
Junichi Tamura
順一 田村
Masahiro Saito
斉藤 正博
Kenzo Togashi
富樫 健三
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.)
Kao Corp
Nippon Peroxide Co Ltd
Original Assignee
Kao Corp
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 Kao Corp, Nippon Peroxide Co Ltd filed Critical Kao Corp
Priority to JP19361482A priority Critical patent/JPS5983912A/en
Priority to CA000430062A priority patent/CA1202854A/en
Priority to GB08315801A priority patent/GB2123044B/en
Priority to ES523135A priority patent/ES8503626A1/en
Priority to DE19833321082 priority patent/DE3321082C2/en
Priority to DE3348394A priority patent/DE3348394C2/en
Priority to FR8309698A priority patent/FR2528447B1/en
Publication of JPS5983912A publication Critical patent/JPS5983912A/en
Publication of JPS621563B2 publication Critical patent/JPS621563B2/ja
Priority to SG63687A priority patent/SG63687G/en
Priority to MY8700570A priority patent/MY8700570A/en
Priority to HK46888A priority patent/HK46888A/en
Granted legal-status Critical Current

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Abstract

PURPOSE:To form sodium percarbonate having improved stability and shelf stability, by treating sodium percarbonate powder with a coating agent containing a borate. CONSTITUTION:Sodium percarbonate powder wetted with water is smeared with about 0.04-10wt%, based on the dry sodium percarbonate expressed in terms of boron, borate, e.g. sodium tetraborate decahydrate having about 50-300mu particle diameter, and the resultant treated sodium percarbonate powder is dried at the melting point of the borate or above to give the aimed sodium percarbonate powder coated with the borate on the surface thereof. Preferably, a sequestering agent, e.g. an ethylenediaminetetraacetate, is used together with the borate.

Description

【発明の詳細な説明】 本発明は安定性、保存性に優れた過炭酸ソーダの、fI
!造法に関するものである。更に肝1.<(は、過炭酸
ソーダ粉末をホウ酸塩を含む被覆剤により処理!〜で表
面を#!覆すること罠より、安定な過炭酸ソーダを製造
する方法に閂する。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides fI
! It is related to the method of construction. Furthermore, liver 1. <( treatment of soda percarbonate powder with a borate-containing coating agent!~) turns into a method for producing stable soda percarbonate rather than coating the surface with #!~.

過炭酸ソーダは漂白剤又は酸化剤として周知のものであ
り、一般的にtri炭醪ソータ゛と過酸化水素を作用さ
せて製造されるもので、一般式:2NF12Co、・、
!5H,,02で表わされるように炭酸ソーダに過酸化
水素が付加したものである。過炭酸ソーダは塩素系漂白
剤に比べ常温で漂白刃tよややおちろものの、色柄物の
漂白にも使用できること、生地を損うことがないことお
よび芦変することがないこ、!:等のため広く家庭用あ
るいは業務用の酸素系77白剤として単独で或V1洗剤
と配合して使用されている。
Sodium percarbonate is well known as a bleaching agent or oxidizing agent, and is generally produced by reacting a tricarbonate sorter with hydrogen peroxide, and has the general formula: 2NF12Co,...
! Hydrogen peroxide is added to soda carbonate as shown by 5H,,02. Soda percarbonate has a slightly slower bleaching effect than chlorine bleach at room temperature, but it can also be used to bleach colored and patterned fabrics, and it does not damage fabrics or cause them to change color! : etc., it is widely used as an oxygen-based 77 whitening agent for household or commercial use, either alone or in combination with V1 detergent.

過炭酸ソータ゛が一般洗剤や家庭用漂白剤に注目される
理由1−J2、千の分解生成物が無公害性である表とも
に、如何なる使用方法においても、何ら問題なく実用化
できる点にある0 しかしながら、過炭酸ソーダd、過#I酸ソーダ忙比べ
、保存安定性がかなり悪く、貯蔵中にかなり速−ヤかに
有効酸素を失うという大き外欠点を有する。過炭酸ソー
ダtま水に対して親、和のが強いため、微縫の湿分によ
っても表面が湿分吸着状態となり、分解が起り、この系
に鉄、銅。
The reason why percarbonate sorter is attracting attention as a general detergent and household bleach is that it can be put to practical use in any way without any problem, both in 1-J2 and 1,000 decomposition products that are non-polluting. However, compared to sodium percarbonate and sodium peroxide, it has a major disadvantage in that it has considerably poor storage stability and loses effective oxygen quite quickly during storage. Sodium percarbonate has a strong affinity for water, so even slight moisture from the stitches causes the surface to absorb moisture, decomposition occurs, and iron and copper are added to this system.

マンガン、コバルトなどのイメンが存在する場合Kij
、さらに分解が促進され、その安定性において禍?1I
lfl酸ソーダより劣る。過炭酸ソーダを単独で密閉容
器に保存した場合は、その貯蔵安定性に訃いて過硼酸ソ
ーダと変らないが、洗剤と混合したり、開封で放置した
場合には、過炭酸ソーダは溶解性が良いにもかかわらず
、吸湿性が高く、その貯蔵安定性において劣る。
If elements such as manganese and cobalt are present, Kij
, further decomposition is promoted and its stability is a disaster? 1I
Inferior to sodium fluoride. If sodium percarbonate is stored alone in a sealed container, its storage stability will be the same as that of sodium perborate, but if it is mixed with detergent or left unopened, sodium percarbonate will become less soluble. Despite its good properties, it has high hygroscopicity and poor storage stability.

従って、開す↑したネま放置しても分解が促進されるこ
となく、如何なる洗剤″!たは漂白組成物と配合されて
も、貯蔵安定性において、実用上、伺らの問題を生じな
い過炭mソーダを提供することが望まれる。
Therefore, decomposition will not be accelerated even if left unopened, and even when mixed with any detergent or bleaching composition, practical problems regarding storage stability will not occur. It is desirable to provide supercarbonated soda.

従来より過炭酸ソーダの安定化方法として数多くの研究
がなされて卦り、種々の方法が提案されている。特に過
炭酸ソーダを有機物、熱櫟物で被覆する方法の提案が多
数なされているが、本発明者等は過炭酸ソーダ粉末をホ
ウ酸塩を含む被覆剤により処理して表面を被覆するとと
により安定な過炭酸ソーダが得られ、貯蔵安定性が極め
て優れていることを見出した。特に本発明に従いホウ酸
塩によって表面を被覆された過炭酸ソーダは洗浄剤と配
合した場合その貯蔵安定性が極めて優れていることがわ
かったが、過炭酸ソーダ粉末の表面をホウ酸塩で被覆す
るに当っては、被覆過炭酸ソーダリ、ナルのホウ酸塩で
完全に被覆されていることが望ましく、被覆にむらがあ
るとその安定性が低下する恐れがある。本発明者等はホ
ウ酸塩被覆過炭酸ソーダ製造に当り工業的にその実施が
簡−雫で且つエネルギー消費が少ない方法でホウ酸塩の
被覆が完全に釘々、創る方法について惨劇[7た結果、
被覆処理に際17て十つm均の特性を利用することによ
り、所望の被覆過炭酸ソーダ7)り得られることを一鼠
出した。
Many studies have been conducted on methods for stabilizing soda percarbonate, and various methods have been proposed. In particular, many proposals have been made for methods of coating soda percarbonate with organic substances or heated substances. It has been found that stable sodium percarbonate can be obtained and has extremely excellent storage stability. In particular, it has been found that the sodium percarbonate powder whose surface is coated with a borate according to the present invention has extremely excellent storage stability when combined with a detergent. In doing so, it is desirable that the coating be completely coated with the sodium percarbonate or nal borate; uneven coating may reduce its stability. The present inventors have discovered a method for producing borate-coated soda percarbonate that is industrially easy to implement and consumes little energy, with a complete coating of borate. result,
It was demonstrated that a desired coating of sodium percarbonate7) could be obtained by utilizing the characteristics of the 17 m average during the coating process.

即ち本発明により過炭酸ソーダ粉末をホウ酸塩を含む被
覆剤によりIJn4N711.て表面を被覆した過炭酸
ソータをイクるための最も有利か方法は、ホウり塩を含
む被覆剤粉末を水で湿尚させた湿n状卯の過炭酸ソータ
に混合吸着させた後、こh−をホウ酸jバが溶融し1、
しめる温度以上の温度で乾燥する処理を行なう方法であ
る。
That is, according to the present invention, sodium percarbonate powder is coated with a borate-containing coating agent to form IJn4N711. The most advantageous method for coating the surface of a percarbonate sorter is to mix and adsorb the coating powder containing borosalt onto a wet n-shaped percarbonate sorter moistened with water; When h- is melted with boric acid, 1,
This method involves drying at a temperature higher than the cooling temperature.

この場合ホウ酸塩としては結晶水をもつホウ酸塩である
ことが望ましく、本発明に使用し得Z)結晶水をもつホ
ウ酸塩とし、でけ、四ホウ酸ソーダ10水焦(ポウ砂回
、0・2B、、O,・1120 ) 。
In this case, the borate is desirably a borate having water of crystallization, and can be used in the present invention. times, 0.2B,,O,.1120).

四ホウ酸ソーダ5水填(>ra2o−2B、、o、・5
n2o 3 。
5 liters of sodium tetraborate (>ra2o-2B,,o,・5
n2o3.

四ホray M 7− p−4水塩r Ha、、0・2
.[’+20.・4FT20 )。
Tetrahoray M 7- p-4 hydrate r Ha, 0.2
.. ['+20.・4FT20).

オクタホウ酸ソーダ4水+x、 c r■p、、、o−
4p、2a、・4H2o > 。
Sodium octaborate 4 water + x, cr p, , o-
4p, 2a, 4H2o>.

ペンタホウ酸ソーダ5水JI C)la、、0’ 5B
20. ・10H,、O) 。
Sodium pentaborate 5 water JI C) la,, 0' 5B
20.・10H,,O).

メ、J * ウ/!9 ソーブ4水塩(uFl、no2
・4H2o )、メクホウ酸ソーダ2水塩(N a B
o 2・2H20)等があげらり、  これらの中1時
に好ましいものe」メタホウ酸ソーダ2水塩並に4水塩
、及び四ホウ酸ソーダ10水塩である。
Me, J * U/! 9 Sorb tetrahydrate salt (uFl, no2
・4H2o), sodium meborate dihydrate (N a B
o 2.2H20), etc., and among these, the most preferred are sodium metaborate dihydrate, tetrahydrate, and sodium tetraborate decahydrate.

上記本発明の有利な被覆方法に於ては結晶水をもつホウ
m塩の粉末を湿潤状態の過炭酸ソーダにまぶし、これを
ホウ酸塩の融点(例えばNa2B、07’10H,、O
: 75℃、  Na、B02’4H20: 57℃。
In the advantageous coating method of the invention described above, a powder of boron salt with water of crystallization is sprinkled on wet sodium percarbonate, and this is applied to the melting point of the borate (e.g. Na2B, 07'10H, O
: 75°C, Na, B02'4H20: 57°C.

NeBo ・2HO: 90℃、  NaBO,−4H
20: 63℃)又は2 それ以上の温度で乾燥すると、ホウ酸塩は自らの結晶水
に溶は込み溶融状態となり、過炭酸ソーダを完全に包み
込むものと考えられる。
NeBo ・2HO: 90℃, NaBO, -4H
It is thought that when dried at a temperature of 20:63°C) or 2 or higher, the borate dissolves in its own water of crystallization and becomes molten, completely enveloping the sodium percarbonate.

この工程中に過炭酸ソーダ中の水分およびホウ酸塩中の
結晶水が蒸発し乾燥作業が完了する。
During this step, the water in the sodium percarbonate and the water of crystallization in the borate evaporate, completing the drying operation.

即ち、均一な被膜形成と乾燥工程が同時に行なわれる。That is, uniform coating formation and drying steps are performed simultaneously.

尚、過炭酸ソーダVi通常40〜160℃で乾燥される
。40℃以下でも乾燥できるが、乾燥時間がかかりすぎ
、160℃以上では過炭酸ソーダの無効分解が起り、有
効酸素の消失が激しくなる。本発明に於いてはホウ酸塩
の溶融点以上、160℃以下で乾燥ずみことが好ましい
Note that sodium percarbonate Vi is usually dried at 40 to 160°C. Although drying can be performed at temperatures below 40°C, the drying time is too long, and at temperatures above 160°C, ineffective decomposition of sodium percarbonate occurs and effective oxygen is rapidly lost. In the present invention, it is preferable to dry at a temperature above the melting point of the borate and below 160°C.

ホウ酸塩の無水塩は、千の有水塩に比べて融点は高いが
(例えばNへ、B、O7: 741℃)、湿潤な過炭酸
ソータ゛中の水分により結晶水を持った場合と同じよう
になり溶融点が下がるため、本発明に卦いて使用できる
が、好ましくけ結晶水を持つホウ酸塩である。ホウ酸塩
被覆過炭酸ソーダ中のホウ酸塩の間t」1、ホウ素とし
て乾燥過炭酸ソーダに対し0.04− I ET % 
Cv+/w)であり、好ましくtよ0.1〜5%(w/
w)である。又、ホウrp!塩の粒径C」−微細なほど
良いが、作業性から50〜300μであり、好−りしく
に100〜150μである。
Anhydrous borate salts have a higher melting point than hydrated salts (e.g., N, B, O7: 741°C), but the melting point is the same as that with water of crystallization due to moisture in a humid percarbonate sorter. This lowers the melting point, so it can be used in the present invention, but borates with water of crystallization are preferred. Borate in borate-coated soda percarbonate between t'1, boron as 0.04-I ET % to dry soda percarbonate
Cv+/w), preferably 0.1 to 5% (w/
w). Also, Hourp! Particle size C of salt - The finer the better, but from the viewpoint of workability, it is 50 to 300μ, preferably 100 to 150μ.

本発明の安定な過炭酸ソー!−の製造に用いる湿潤な過
P、酸ソーダとしてt」1、炭酸ソーダと過酸化水素と
を通常の方法で反応させ、通常の方法で脱水した過炭酸
ソーダをそのまま使用し得る。即ちこの混血状態の過炭
酸ソーダは水分を7〜1日係含んでおり、この水分が必
要とする湿淵水として作用するため、−tのまま使用出
来るが、好オしくけ含水率10〜16係のものである。
Stable percarbonate saw of the present invention! - Wet perphosphorous acid used in the production of t''1 as acid soda, sodium carbonate and hydrogen peroxide are reacted in a conventional manner, and sodium percarbonate, which is dehydrated in a conventional manner, can be used as it is. In other words, this mixed sodium percarbonate contains water for 7 to 1 day, and this water acts as the necessary wet water, so it can be used as is, but it is preferable to use a water content of 10 to 1. This is from Section 16.

場合により含水率の低い過炭酸ソーダを用いる時にけ、
ホウ酸塩の粉末が均一にまぶされるように水で適当に湿
1)化することが好まし2い0木発明の実施に際してホ
ウrP塩が溶融して被膜を形成する際に悪影響を及ぼ式
ない様な過炭酸ソーダの公知の安定剤、例えばエチレン
ジアミン四酢酸塩又&、に) IJ口三酢酸塩等の全日
イオン封鎖剤を被覆剤に含有させることは、有利な方法
である。
In some cases, when using soda percarbonate with a low water content,
It is preferable to moisten the borate powder appropriately with water so that it is evenly sprinkled (1). It is an advantageous method to include in the coating a permanent ion sequestrant, such as the known stabilizers of sodium percarbonate, such as ethylenediaminetetraacetate or IJ-triacetate.

本発明のホウ酸基被覆過炭酸ソータ゛の製造に当って、
ホウr¥9.塩水溶液を用い、これを過炭酸ソーダ粉末
に対しlTi″を輯混合した後、乾燥する処理を行かう
ことにより過炭酸ソーダを被ぐすするととも出来為が、
この場合は軟骨過炭酸ソーダを用いtrければならない
ため、乾ヅ・■を二重に行なうことが必要となる。
In producing the boric acid group-coated percarbonate sorter of the present invention,
Hou r¥9. Using a salt aqueous solution, mixing lTi'' with the sodium percarbonate powder and drying it covers the sodium percarbonate and the resulting product is as follows:
In this case, since it is necessary to use cartilage sodium percarbonate, it is necessary to perform the drying process twice.

これに対し上記の如く、過炭酸ソーダとして水で湿閂六
れた過炭酸ソーダ粉末、特に過酸化水素と炭酸ソーダを
水溶液中で反応食せ脱水[7て得られた湿潤状態の過P
、酸ソーダを用い、ホウ重塔粉末をこhに対し?l?、
合吸着させた後、こhを乾燥する#L理を行かう、ホウ
酸塩の特性を利用した方法は、ホウ酸基を溶解−する操
作も必要なく、エネルギー消費が少なく、実施が簡単で
あるだめ本発明の実施に当り工業的に極めて有利な方法
である。
On the other hand, as mentioned above, sodium percarbonate powder, which has been moistened with water as sodium percarbonate, in particular hydrogen peroxide and soda carbonate, is reacted in an aqueous solution and dehydrated [7].
, using acid soda and adding powder to the powder? l? ,
The method that takes advantage of the properties of borates, which performs the #L process of drying the material after adsorption, does not require an operation to dissolve boric acid groups, consumes less energy, and is easy to implement. This is an industrially extremely advantageous method for carrying out the present invention.

本発明の方法により得られたホウ酸塩被覆過炭酸ソーダ
e」1、添付するp P6g写真に示される如くホウ酸
塩が被覆状態で均一に過炭酸ソーダ粒子表面を被ってい
ることが観察される。被覆した過炭酸ソーダは平均粒子
径が100〜2000μ、女J、tL<iよ250〜1
000μの粉末とするのが好ましい。
As shown in the attached photo of borate-coated soda percarbonate e'1 obtained by the method of the present invention, it was observed that the borate was uniformly coated on the surface of the soda percarbonate particles. Ru. The coated soda percarbonate has an average particle size of 100 to 2000μ, tL<i>250 to 1
000μ powder is preferable.

第1図は被覆前の過炭酸ソーダ粒子、第2図は被覆過炭
酸ソーダ粒子の走査型電子顕微鏡写真で夫々100倍に
拡大したもの、第3図は第2図の被覆過炭酸ソーダ粒子
の断面拡大写7!、(440倍)であり、第3図は表面
のホウ酸m被(友層を示している。尚第2〜3図のもの
はメタホウ酸ンーダ2水塩3.7チでネ皮覆されでいる
Figure 1 is a scanning electron micrograph of the uncoated sodium percarbonate particles, Figure 2 is a scanning electron micrograph of the coated soda percarbonate particles, each magnified 100 times, and Figure 3 is a photo of the coated soda percarbonate particles of Figure 2. Enlarged cross-section photo 7! , (440 times), and Figure 3 shows the boric acid layer on the surface.The ones in Figures 2 and 3 were coated with 3.7 chloride of metaborate dihydrate. I'm here.

以下に本発明を実施例例ついて説、明するが、本発明は
これらの実施例により限定さhるものではない。
EXAMPLES The present invention will be described and explained below with reference to Examples, but the present invention is not limited to these Examples.

実施例 1 過酸化水素と炭酸ソーダを水溶液中で反応させて得られ
た温湯な過炭酸ソルダ(水分10%。
Example 1 Warm percarbonate solder (moisture 10%) obtained by reacting hydrogen peroxide and soda carbonate in an aqueous solution.

乾燥時平均粒子径480μ)を連続フィダーにて5.3
kgZ分の割合で連続混合機に供給し、一方、メタホウ
酸ソーダ2水堪(平均粒子径150μ)を連続フィダー
にて0.178kf/lI+ の割合で先の連続混合機
に供給した。連続混合機での滞留時間を5分になるよう
に調節L %  この混合物を連続的に流動乾燥機に供
給し、130℃で乾燥した。
The average particle diameter when dry is 480μ) is 5.3 in a continuous feeder.
kgZ was supplied to the continuous mixer at a rate of 0.178 kf/lI+, and on the other hand, two water bottles of sodium metaborate (average particle size 150μ) were supplied to the continuous mixer at a rate of 0.178 kf/lI+. The residence time in the continuous mixer was adjusted to 5 minutes L % This mixture was continuously fed to a fluidized fluid dryer and dried at 130°C.

この被伊過炭酔ソーダのホウ素を定□□□したところ0
.42 % (ホウ素として)であった。この被覆処理
した過炭酸ソーダと各種第2成分とを混合した時の安定
性を第1表に示す。尚、安定度はピンホール付樹脂容器
にサンプルを所要量入れ、50℃、80%RHに24時
間放置後の有効第  1  岩 実  施  例   2 湿曹状に5弓の過炭酸ソーダ(水分12チ、乾燥時平均
粒子径400μ)3.4吟およびホウ酸ソーダ゛10水
塩0.jkfをバッヂ式混f¥機に入り、、  1分間
混合し、この混合物を流動乾燥枦にC140℃で乾燥し
た。この被覆過炭酸ソーダのホウ素を定員したところ0
.404 (ホウ素として)であった0 尚比較の目的でホウ酸ソーダ10水塩の代りに、被覆剤
としてそれぞれ炭酸ソーダ、コロイダルシリカ(S10
220チ品)および3号ケイ酸ソーダを選択し、それぞ
れ0.16し9 * 0.78 kg および0.31
kg添加した以外は前記した条件に従った。このように
して得られた被覆過炭酸ソーダと市販洗剤AC無リン洗
剤、ゼオライト配合)をピンホール付樹脂容器に9:1
の割合で混合し、40 T: 、 80%RHに2週間
放置後の有効酸素残存率(安定度)を測定し、その結果
を第2表に示す。
The boron content of this carbonated soda was determined to be 0.
.. 42% (as boron). Table 1 shows the stability when the coated soda percarbonate and various second components were mixed. The stability was determined by putting the required amount of sample into a resin container with a pinhole and leaving it at 50℃ and 80% RH for 24 hours. , dry average particle size 400 μ) 3.4 gin and sodium borate decahydrate 0. JKF was placed in a badge type mixer and mixed for 1 minute, and the mixture was dried at 140° C. in a fluidized drying cage. When the boron content of this coated soda percarbonate was set to 0
.. 404 (as boron) 0 For comparison purposes, sodium carbonate and colloidal silica (S10
Select No. 220 product) and No. 3 sodium silicate and weigh 0.16 * 0.78 kg and 0.31, respectively.
The conditions described above were followed except that kg was added. The thus obtained coated soda percarbonate and commercially available detergent AC phosphorus-free detergent (combined with zeolite) were placed in a resin container with a pinhole at a ratio of 9:1.
After mixing at a ratio of 40 T: and 80% RH for two weeks, the effective oxygen residual rate (stability) was measured, and the results are shown in Table 2.

第  2  表 実施例 3 実施例1及び2で隼1(造l−た被覆poについてハム
下の条件で保存安定性を試験した。
Table 2 Example 3 The coated po coated in Examples 1 and 2 was tested for storage stability under humid conditions.

(1)市販洗剤B(無リン洗剤・ゼオライト配合)に被
覆POを10重目、チ湿合 (2)  市販洗剤O(含リン洗剤・トリボIJ IJ
ン酸ソーダ配合)を被覆pcを10重風q6混合これら
をそれぞれ10fずつ50 (’、C容プラプラスチッ
ク容器れ蓋をして40℃、80%RHの条件に14日間
放置した後、有効酸素残存率を次式により求めた。
(1) Commercially available detergent B (phosphorus-free detergent, zeolite combination) coated with PO coated with 10 layers of moisture (2) Commercially available detergent O (phosphorus-containing detergent, Tribo IJ IJ
Coated PC with 10 heavy air (mixed with sodium chloride) and mixed with 10 f of each of these 50 ('). The residual rate was calculated using the following formula.

有効酸素の測定Ic+よ0.1N過マンガン酸カリウム
測定法を用いた。
Measurement of available oxygen Ic+ 0.1N potassium permanganate measurement method was used.

また比較のため本発明による被覆POの他に(1)被覆
をほどこさずに湿y4 p cをそのま寸乾燥し九PO
,(2)過ホウ酸ソーダ(FB)を同様に試験した。
For comparison, in addition to the coated PO according to the present invention, (1) 9PO was prepared by drying the wet Y4PC as it was without applying any coating.
, (2) Sodium perborate (FB) was similarly tested.

【図面の簡単な説明】[Brief explanation of the drawing]

第1〜3図は走査電子顕P鏡写^で、第1図は被覆前の
過炭乍ソーダ粒子の写真、第2図は被覆過炭酸ソーダ粒
子の写真、第3図Cj、第2図の断面拡大写真である。
Figures 1 to 3 are scanning electron micrographs, Figure 1 is a photo of percarbonate soda particles before coating, Figure 2 is a photo of coated soda percarbonate particles, Figure 3 Cj, Figure 2 This is an enlarged cross-sectional photograph.

Claims (1)

【特許請求の範囲】 1、 過炭酸ソーダ粉末をホウ酸塩を含む被覆剤により
処理して表面を被覆することを特徴とする安定な過炭酸
ソーダの製造法。 2、過炭酸ソーダ粉末が水で湿憫された粉末であり、ホ
ウ酸塩を含む被覆剤粉末を湿■状態の過炭酸ソーダに混
合吸着させた後、これをポウ酸塩が溶融しはじめる温度
以上の温度で乾燥する処理を行なう特許請求の範囲第1
項記載の製造法。 3、 水で湿間された過炭酸ソーダ粉末が過酸化水素と
炭酸ソーダを水溶液中で反応させ脱水して得られた水分
7〜18重量%のものである0¥[請求の範囲第2項記
載の製造法。 4、過炭酸ソーダに対するホウ酸塩のitがホウ素とし
て0.04〜10重景チである特WrR古木の範囲第1
項〜第5項の何れか1項に記載の製造法。 5、 被覆剤が金パイオン封1911剤を含む特許請求
の範囲第1項〜第4項の伺)1か1項に記載の製造法。 6、 金朽イオン月釧剤がエヂレンジアミン四酢酸塙又
eよニトリロ三酢酸塩である特許請求の範囲第5項記載
の9!造法。 7、 被覆過炭酸ソーダ粉末の平均粒・子径が100〜
2nooμである特#′r請求の範囲第1項〜第6項の
何れか1項に記載の製造法。 8、 ホウrN塩が結晶水をもつホウ酸塩である特許請
求の範VJ1第1!N−M7項の何れが1項に記載の製
造法。 9、 結晶水をもつホウ酸塩がメクポウ酸ソーダ2水信
又tit 4水堪である特許請求の範囲第8項記載の製
造法。 10、  結晶水をもつホウ酸塩がホウ酸ソーダ1゜水
塩である’I? Fl’r請求の範囲第8項記載の製造
法。 11、  ホウ酸塩粉末の粒径が5o〜300μである
特許請求の範囲第2項〜第10項の何れか1項に記載の
9■造法。
[Claims] 1. A method for producing stable soda percarbonate, which comprises treating the surface of sodium percarbonate powder with a coating agent containing a borate. 2. Sodium percarbonate powder is a powder moistened with water, and after coating powder containing borate is mixed and adsorbed to wet sodium percarbonate, it is heated to a temperature at which the borate starts to melt. Claim 1 which performs a drying process at a temperature above
Manufacturing method described in section. 3. Soda percarbonate powder moistened with water has a water content of 7 to 18% by weight obtained by dehydrating hydrogen peroxide and soda carbonate in an aqueous solution [Claim 2] Manufacturing method described. 4. The first range of special WrR old wood where the it of borate relative to sodium percarbonate is 0.04 to 10 times as boron.
The manufacturing method according to any one of Items 1 to 5. 5. The manufacturing method according to claim 1 or 1 of claims 1 to 4, wherein the coating material includes a gold pion sealant 1911 agent. 6. 9 according to claim 5, wherein the Kinkuku Ion Tsukisen agent is ethylenediaminetetraacetic acid Hanamata e or nitrilotriacetate. Construction method. 7. The average particle diameter of the coated soda percarbonate powder is 100~
2nooμ. The manufacturing method according to any one of claims 1 to 6. 8. Claim VJ1 No. 1 in which the boron salt is a borate having water of crystallization! Any of N-M7 is the manufacturing method according to Item 1. 9. The production method according to claim 8, wherein the borate having water of crystallization is sodium mekporate 2 water or tit 4 water. 10. The borate with water of crystallization is sodium borate 1° hydrate 'I? Fl'r manufacturing method according to claim 8. 11. The manufacturing method according to any one of claims 2 to 10, wherein the borate powder has a particle size of 5o to 300μ.
JP19361482A 1982-06-10 1982-11-04 Production of stable sodium percarbonate Granted JPS5983912A (en)

Priority Applications (10)

Application Number Priority Date Filing Date Title
JP19361482A JPS5983912A (en) 1982-11-04 1982-11-04 Production of stable sodium percarbonate
CA000430062A CA1202854A (en) 1982-06-10 1983-06-09 Bleaching detergent composition
GB08315801A GB2123044B (en) 1982-06-10 1983-06-09 Bleaching detergent composition
ES523135A ES8503626A1 (en) 1982-06-10 1983-06-09 Bleaching detergent composition
DE3348394A DE3348394C2 (en) 1982-06-10 1983-06-10 Sodium percarbonate bleaching agents
DE19833321082 DE3321082C2 (en) 1982-06-10 1983-06-10 Bleach Cleaner
FR8309698A FR2528447B1 (en) 1982-06-10 1983-06-10 DETERGENT AND WHITENING COMPOSITION AND PROCESS FOR PREPARING THE SAME
SG63687A SG63687G (en) 1982-06-10 1987-08-07 Bleaching detergent composition
MY8700570A MY8700570A (en) 1982-06-10 1987-12-30 Bleaching detergent composition
HK46888A HK46888A (en) 1982-06-10 1988-06-23 Bleaching detergent composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19361482A JPS5983912A (en) 1982-11-04 1982-11-04 Production of stable sodium percarbonate

Publications (2)

Publication Number Publication Date
JPS5983912A true JPS5983912A (en) 1984-05-15
JPS621563B2 JPS621563B2 (en) 1987-01-14

Family

ID=16310865

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19361482A Granted JPS5983912A (en) 1982-06-10 1982-11-04 Production of stable sodium percarbonate

Country Status (1)

Country Link
JP (1) JPS5983912A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04187508A (en) * 1990-11-21 1992-07-06 Kao Corp Stable sodium percarbonate granule and production thereof
US5328721A (en) * 1992-07-30 1994-07-12 Fmc Corporation Process for manufacturing sodium carbonate perhydrate particles and coating them with sodium borosilicate
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
JP2008545609A (en) * 2005-06-01 2008-12-18 ソルヴェイ(ソシエテ アノニム) Coated sodium percarbonate particles, methods for their production, their use and detergent compositions containing them
JP2009544554A (en) * 2006-07-27 2009-12-17 エボニック デグサ ゲーエムベーハー Sodium percarbonate particles with shell
JP2009544555A (en) * 2006-07-27 2009-12-17 エボニック デグサ ゲーエムベーハー Sodium percarbonate particles with shell

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04187508A (en) * 1990-11-21 1992-07-06 Kao Corp Stable sodium percarbonate granule and production thereof
US5328721A (en) * 1992-07-30 1994-07-12 Fmc Corporation Process for manufacturing sodium carbonate perhydrate particles and coating them with sodium borosilicate
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
JP2008545609A (en) * 2005-06-01 2008-12-18 ソルヴェイ(ソシエテ アノニム) Coated sodium percarbonate particles, methods for their production, their use and detergent compositions containing them
JP2009544554A (en) * 2006-07-27 2009-12-17 エボニック デグサ ゲーエムベーハー Sodium percarbonate particles with shell
JP2009544555A (en) * 2006-07-27 2009-12-17 エボニック デグサ ゲーエムベーハー Sodium percarbonate particles with shell

Also Published As

Publication number Publication date
JPS621563B2 (en) 1987-01-14

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