TW416982B - Methods for producing a surface active agent fine particle, the surface active agent fine particle and the particle detergent composition - Google Patents

Methods for producing a surface active agent fine particle, the surface active agent fine particle and the particle detergent composition Download PDF

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Publication number
TW416982B
TW416982B TW087100233A TW87100233A TW416982B TW 416982 B TW416982 B TW 416982B TW 087100233 A TW087100233 A TW 087100233A TW 87100233 A TW87100233 A TW 87100233A TW 416982 B TW416982 B TW 416982B
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Taiwan
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weight
surfactant
acid
powder
soap
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TW087100233A
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Chinese (zh)
Inventor
Emiko Watahiki
Shinichi Hashimoto
Tsutomu Ishikawa
Hiroyuki Iwabuchi
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Lion Corp
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    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/16Organic compounds
    • C11D3/37Polymers
    • C11D3/3746Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • C11D3/3757(Co)polymerised carboxylic acids, -anhydrides, -esters in solid and liquid compositions
    • C11D3/3761(Co)polymerised carboxylic acids, -anhydrides, -esters in solid and liquid compositions in solid compositions
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D1/00Detergent compositions based essentially on surface-active compounds; Use of these compounds as a detergent
    • C11D1/02Anionic compounds
    • C11D1/12Sulfonic acids or sulfuric acid esters; Salts thereof
    • C11D1/14Sulfonic acids or sulfuric acid esters; Salts thereof derived from aliphatic hydrocarbons or mono-alcohols
    • C11D1/143Sulfonic acid esters
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D10/00Compositions of detergents, not provided for by one single preceding group
    • C11D10/04Compositions of detergents, not provided for by one single preceding group based on mixtures of surface-active non-soap compounds and soap
    • C11D10/042Compositions of detergents, not provided for by one single preceding group based on mixtures of surface-active non-soap compounds and soap based on anionic surface-active compounds and soap
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D11/00Special methods for preparing compositions containing mixtures of detergents
    • C11D11/0082Special methods for preparing compositions containing mixtures of detergents one or more of the detergent ingredients being in a liquefied state, e.g. slurry, paste or melt, and the process resulting in solid detergent particles such as granules, powders or beads
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D17/00Detergent materials or soaps characterised by their shape or physical properties
    • C11D17/06Powder; Flakes; Free-flowing mixtures; Sheets
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/16Organic compounds
    • C11D3/37Polymers
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D1/00Detergent compositions based essentially on surface-active compounds; Use of these compounds as a detergent
    • C11D1/02Anionic compounds
    • C11D1/12Sulfonic acids or sulfuric acid esters; Salts thereof
    • C11D1/28Sulfonation products derived from fatty acids or their derivatives, e.g. esters, amides

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  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Detergent Compositions (AREA)

Abstract

This invention provided and useful <alpha>-sulfofatty acid alkyl ester as a main ingredient of detergent composition raw material of the surface active agent fine particle and their preparation, these are related to a detergent composition containing said surface active agent fine particle, regulated the sulrry mixture which are containing a <alpha>-sulfofatty acid alkyl ester , soap, water soluble carboxylic acid and/or their salts, concentrated the water content of the sulrry mixture below to the 15 wt%, after the temperature of the concentrates are below to 70 c, particulated, and preparing a surface active agent fine particles which are contained above to 40 wt% of <alpha>-sulfofatty acid alkyl ester,more than 10 wt% of soap, to the total weight of the <alpha>-sulfofatty acid alkyl ester and the soap containing a 0.01-5 wt% of water soluble polycarboxylic acid and/or their salts, in order to make the particle detergent composition containing a surfgace active agent fine particles, it can be obtained an excellence solubility of a surface activity fine particle in the alkali aqueous solution and exhibited the cleanliness level of the surface active agent fine particle throughly.

Description

A7 B7 __416932 五、發明説明(1 ) 〔技術領域〕 (請先閱讀背面之注_項再填寫本頁) 本發明係關於一種有用之《-硫代脂肪酸烷酯為洗劑 組成物原料之主要成分的界面活性劑粉體舆其製法,含 有此界面活性劑粉體之粒狀洗劑組成物。 〔技術背景〕 可供衣物洗劑使用之陰離子界面活性劑,業已摻混在 市面上公開出售之為數槿多之已開發洗劑使用,其中已 知之一種為Of-硫代脂肪酸烷酯。硫代脂肪酸烷酯有 優異之洗渾力,靥於高性能之洗劑材料。又,因有良好 之生物分解性,而鮮少有對琛境産生不利影逛之待點β 然而,or-硫代脂肪酸烷酷,雖有上述之髙洗潔力, 相反者,如單獨將cr-硫代脂肪酸烷酯粉體化時,卽在 低溫之溶解性即稍為變差β又,製造前後之結晶性薄弱 ,呈容易凝集,固化之液晶狀態,而有結晶化時需耗用 長畤間(1〜2星期)之問題。再者,由於不易結晶化,因 而在粉體化過程中有難以操控之情形。 其中陰離子界面活性劑,通常_經由中和而獲得水性淤 漿,如欲使之成為粒狀洗劑組成物,邸有必要不拘手段 施予濃缩化或粉體化,而有以下一般之報告。 經濟部中央標準局員工消費合作社印製 〔界面活性劑粉體之製法〕 U)特開昭54-10642 8號公報(日本特許公開公報):由 噴貉乾燥法製造高级烷基硫酸鹽之粒狀物之方法.惟利 用噴费乾燥法對能源之負荷很大。 (2)待開昭55-69698號公報(日本特許公開公報):偽 本紙張尺度適用中國國家標率(CNS &gt; Α4規格U10X297公釐) 經濟部中央標隼局貝工消費合作社印製 416382 a? Β7 五、發明説明(2 ) 一撞利用噴蓀乾燥法製造陰離子活性劑舆非離子界面活 性劑之混合粒狀物之方法*同樣利用噴费乾燥法所箱用 能源的負荷很大· (3)待開平2-222498號公報(日本待許公開公報):係 一種使用薄膜蒸發機以製迪髙密度洗剤用撕歎原料之方 法,惟尚未到達活性剤之粉體化。 (〇特開平5-331496號公報(日本待許公開公報&gt;:一 種利用薄膜蒸發機以製造陰離子活性之粒狀物方法,因 需將活性劑單掲造粒在以上之髙溫下流動性差,且 有溶解性低之掛窳。實際上•在實施例中僅限定硫酸院 酯,聚氧乙烯烷醚碕酸酯,對於不易也體化之硫代 脂肪酸烷酯,在濃缩前後於离溫下則難以粉碎而逹成粉 體化》 又,使用界面活性劑粉體做為粒狀洗_組成物,即有 以下之各種提案。 〔使用界面活性劑粉體之粒狀洗剤組成物之製法〕 (5)特開平4-345700號公報(日.本待許公開公報): α -硫代脂肪酸烷酯在中性之組份(builder)存在下,予 以粉體化,與其他之洗劑粉體一起混合在粉體以製造粒 狀洗剤組成物之方法,並非以提高溶解性為目的》 —方面,關於含有聚羧酸之界面活性劑粉體,在特公 平3-20439號公報(日本特許公開公報),特開昭60-21000 號公報(日本特許公開公報)·特開昭6 3-9 2639號公報(曰 本待許公開公報 &gt;,特開平5-43897號公報(日本待許公開 -4 - 本紙張尺度適用中國國家標準(CNS ) Α4規格(210X297公釐) (請先閲讀背面之注意事項再填寫本頁) 、τ 416982 ^ 經濟部令央標準局貝工消費合作社印裝 五、發明説明( ) 1 1 公 報 ), 特開平7 ™ ] 8 2 9 5 號 公 報 &lt;日本待許公開公報)掲示 1 1 含 有 陰 離 子 界 面 活 性 劑 與 聚 羧 酸 之 界面活性劑 粉 體 〇 1 1 惟 以 上 之 任 一 案 件 並 非 使 用 a -硫代脂肪酸烷酯, 請 1 先 1 在 於 解 決 其 特 有 之 課 題 〇 m 讀 1 基 於 上 述 之 報 告 y 本 發 明 者 等 所 提出之特願 平 6 ^ 329536 背 面 1 I 之 1 號 (日本特許申請编號), 其 百 的 在 於提供一種 在 高 溫下 注 意 .1 不 易 凝 集 X 固 化 之 界 面 活 性 劑 粉 體 ,做成含有 陰 離 子界 事 項 1 I 再 面 活 性 劑 之 水 性 淤 漿 濃 縮 塊 狀 物 後 ,經由冷卻 步 驟 ,再 填 窝 1 本 1 · · · · j 予 以 粉 體 化 之 界 面 活 性 劑 粉 體 之 製 法。 頁 τ 1 又 9 關 於 待 願 平 7 - 1 3 1 1 0 3 號 公 報 (曰本專利申請编號), I 1 其 傣 以 a -硫代脂肪酸烷酯為主要成分之界面活性劑粉體 1 1 中 9 以 提 高 對 水 之 溶 解 性 為 百 的 〇 利用特願平 6- 329536 ψ * 訂 號 所 掲 之 方 法 經 由 拓 展 而 倡 議 一種由or -硫代脂肪 I 酸 烷 酯 與 皂 製 造 界 面 活 性 劑 粉 體 之 方法。 1 記 載 於 待 願 平 7- 1 3 11 03 之 界 面 活性劑粉體 9 確 認在 1 1 中 性 以 下 之 水 中 有 良 好 之 溶 解 性 〇 1 I 本 發 明 者 傜 據 由 特 願 平 7 - 13 11 0 3 號所掲示之 界 面 活性 線' 劑 粉 體 t 除 可 得 上 述 在 中 性 以 下 之 水中有提高 溶 解 性之 i f 效 果 以 外 » 於 製 造 粉 體 化 物 前 後 持 別不拘於應 用 容 易凝 1 1 集 、 固 化 之 a -硫代脂肪酸烷酯, 而發現使用上述界面 t».: 活 性 劑 粉 體 以 及 該 界 面 活 性 劑 粉 體 ns 之粒狀洗劑 組 成 物, I 比 較 以 往 保 存 在 原 料 倉 庫 内 期 間 中 具有不易使 粒 子 凝 i 1 集 及 固 化 之 優 異 效 果 〇 1 I 蓋 此 乃 傺 與 皂 共 存 9 使 a 5 -脂肪酸烷酯迅速結晶化, 1 1 1 1 1 1 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) A7 B7 416082 五、發明説明(4 ) %成不易凝集及固化狀態的緣故。 Τ ^|_ I— n n - ij. I n m I— m n I (請先閲讀背面之注意事項再填寫本頁) 亦即,特願平7-131103號所掲示之界面活性劑粉體以 及便用此粉體之粒狀洗劑組成物,僳包含有高滠度组成 硫代脂肪酸烷酯,因而解決將《-硫代脂肪酸烷酯 粉讎化後所引起之易於凝集及固化舆對水之低溫溶解性 稍差之問題》 其中,鼷於一般之粒狀洗劑組成物*僳添加有硪酸鈉 等鹺性組份。此種鹺性組份,可将洗液變成險性,而可 達成提高粒狀洗劑组成物之洗淨力* 做為睡性組份使用之物質通常有較高之水溶性,將粒 狀洗劑組成物投入於水中時,首先此齡性組份立卽溶解 ,水變成為驗性水溶液,其次陰離子界面活性劑則溶解 於該鹼性水溶液。 然而,關於特願平7-131103號所掲示之界面活性剤粉 體,雖在中性下之水中有很大之改善溶解性效果,然在 齡性水溶液中則有降低改善溶解性效果之傾向β因此, 實際使用含有此種界面活性劑粉.驩之粒狀洗繭組成物時 ,有因其混配組成而稍為降低赛面活性劑粉體之溶解性 ,而無法充分發揮其洗淨性能之情形。 經濟部中央標準局貝工消費合作社印製 〔發明之掲示〕 本發明之目的在於提供一種可維持特願平7-131103號 掲示之由α -硫代脂肪酸烷酯舆皂所形成界面活,性剤粉膣 不易使粒子凝集及固化之優異效果,且在險性水溶劑中 可獲得良好溶解性之界面粉體之製法,以及可充&amp;發揮 -6 -本紙張尺度適用中國國家標準(CNS ) Α4規格(2丨0X297公釐) 416982 A7 B7_____ 五、發明説明(5 ) 此界面活性劑粉體洗淨性能之粒狀洗_組成物。 欲解決相關之課題,在本發明中,阑整所包含《-硫 代脂肪酸烷酯,皂,水溶性聚羧酸及/或其鹽之混合淤 漿,將該混合淤漿水分濃縮至15%重量以下,而濃缩 物之溫度在7 (TC以下後即行粉體化,而製造含有4 0 %重 量以上之硫代脂肪酸烷酯,1D重量%以上之皂,對 it -硫代脂肪酸烷酯與皂之總量含有〇·〇1〜5%重量之水 溶性聚羧酸及/或其鹽之界面活性劑粉體為其特徴者* 又,可組成含有以此製法所獲得之界面活性劑粉體之 粒狀洗劑組成物。 〔實施發明所箱之最佳形態〕 玆對本發明之内容詳細説明如下。 «-硫代脂肪酸烷酯,適宜者僳由以下一般式(1)所代 表者,而以飽和或不飽和脂肪酸殘基之平均破原子數為 10〜20,酯烷基之硪原子數為1〜5者為桂》又,包括此 α-碕代脂肪酸烷酯之抗離子,乃為鹼金屬,齡土類金 屬,及取代或無取代之銨基等—般適合者為押’納等 之鹸金屬《 R1 CHCOOR2 .......⑴A7 B7 __416932 V. Description of the invention (1) [Technical Field] (Please read the Note_ item on the back before filling this page) The present invention is about a useful "-thio fatty acid alkyl ester as the main ingredient of lotion composition The surfactant powder of the ingredients is manufactured by the method, and the granular detergent composition containing the surfactant powder is provided. [Technical Background] Anionic surfactants that can be used in laundry lotions have been blended with several developed lotions that are commercially available in the market, and one of them is known as Of-thio fatty acid alkyl ester. Thio fatty acid alkyl esters have excellent detergency and are good at high-performance lotion materials. In addition, due to its good biodegradability, there are few points that have adverse effects on the environment. However, although the or-thio fatty acid alkane has the aforementioned cleaning power, the opposite, such as When cr-thio fatty acid alkyl ester powder is powdered, the solubility of europium at low temperature is slightly worsened. β, the crystallinity before and after manufacturing is weak, it is in a liquid crystal state that is easy to agglomerate and solidify, and it takes a long time to crystallize. Kama (1 ~ 2 weeks) problems. Furthermore, since it is not easy to crystallize, it may be difficult to handle during the powdering process. Among them, the anionic surfactant is usually _ obtained by neutralization to obtain an aqueous slurry. If it is to be made into a granular lotion composition, it is necessary to apply concentration or powder without any means. There are the following general reports . Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs [Method for producing surfactant powder] U) JP 54-10642 No. 8 (Japanese Patent Publication): Production of granules of advanced alkyl sulfates by spray drying The method of the object. However, the use of spray drying method has a large load on energy. (2) To-Kou Sho 55-69698 (Japanese Patent Laid-Open Gazette): The paper size of the paper is applicable to China's national standard (CNS &gt; A4 specification U10X297 mm) Printed by Shellfish Consumer Cooperative, Central Bureau of Standards, Ministry of Economic Affairs a? Β7 V. Description of the invention (2) A method of manufacturing a mixed granule of anionic active agent and nonionic surfactant by spray drying method. Also, the load of the energy used in the spray drying method is very large. (3) Tokaikai No. 2-222498 (Japanese Tokukai Publication): A method using a thin-film evaporator to wash the raw materials for the washing of dendron densities, but the powder of the active radon has not been reached. (Japanese Patent Application Laid-Open No. 5-331496 (Japanese Laid-Open Publication) &gt;: A method for producing an anion-active granule by using a thin-film evaporator, which requires the active agent to be granulated at a temperature above the above temperature, and has poor fluidity. And has low solubility. In fact, in the examples, only sulfuric acid esters and polyoxyethylene alkyl ether phosphonates are limited. For thio fatty acid alkyl esters that are not easy to form, they are separated before and after concentration. It is difficult to pulverize at room temperature to form powder. "Furthermore, using the surfactant powder as a granular washing composition has the following various proposals. [Using the granular washing composition of the surfactant powder Production method] (5) Japanese Patent Application Publication No. 4-345700 (Japanese. This is a public notice to be published): α-thio fatty acid alkyl ester in the presence of a neutral component (builder), powdered, and washed with other The method of mixing the powder with the powder to produce a granular detergent composition is not for the purpose of improving the solubility. "-Regarding the surfactant powder containing polycarboxylic acid, it is disclosed in Japanese Patent Publication No. 3-20439 ( Japanese Patent Laid-Open Gazette), Japanese Patent Application Laid-Open No. 60-210 00 (Japanese Patent Laid-open Gazette) • Japanese Patent Laid-Open No. 6 3-9 2639 (Japanese to-be-published public bulletin), Japanese Patent Laid-open No. 5-43897 (Japanese to-be-public published-4-This paper is applicable to China National Standard (CNS) Α4 specification (210X297 mm) (Please read the precautions on the back before filling out this page), τ 416982 ^ Printed by the Central Bureau of Standards of the Ministry of Economic Affairs, Shellfish Consumer Cooperatives 5. Description of the invention () 1 1 Gazette ), Japanese Patent Application Laid-Open No. 7 ™] 8 2 9 5 &lt; Japanese Unexamined Publication (KOKAI)) Indication 1 1 Powder containing an anionic surfactant and a polycarboxylic acid surfactant 01 1 However, it is not used in any of the above cases a-Thio fatty acid alkyl esters, please 1st 1st to solve its unique problems 0m read 1 Based on the above report y The inventors proposed by the inventors and others 6 ^ 329536 back 1I No. 1 (Japanese patent application No.), its one of the best is to provide a kind of attention at high temperature. 1 not easy to agglomerate X solid The surfactant powder is made into an aqueous slurry containing concentrated anionic matter 1 I and then re-surfactant is concentrated into agglomerates, and then the cooling step is followed by filling the nest with 1 powder. 1 · · · · j powdered interface Preparation method of active agent powder. Page τ 1 and 9 Regarding Waiting No. 7-1 3 1 1 0 3 (the patent application number), I 1 is a surfactant powder containing a-thio fatty acid alkyl ester as a main component 1 1 in 9 in order to increase the solubility in water by 100. Using the method of Japanese Patent Application No. 6-329536 ψ * The method proposed in the article is to develop a surfactant from or -thio fatty acid I alkyl ester and soap through expansion. Powder method. 1 Surfactant powder described in Tobei Hei 7- 1 3 11 03 9 Good solubility in water below 1 1 neutral was confirmed. 0 I The present inventor according to Tobei Hei 7-13 11 0 The surface active line shown in No. 3 'powder powder t can be obtained in addition to the above if the effect of improving solubility in water below neutral »» Before and after the production of powder compounds, it is easy to coagulate 1 1 set, curing A-thio fatty acid alkyl ester, and it was found that the use of the above interface t ».: active agent powder and the granular detergent composition of the surfactant powder ns, I was less difficult than when it was stored in a raw material warehouse. Excellent effect for particle aggregation i 1 collection and curing 〇1 I Coexistence of soap and soap 9 Rapidly crystallize a 5 -fatty acid alkyl ester, 1 1 1 1 1 1 This paper size applies Chinese National Standard (CNS) A4 Specifications (210X297 mm) A7 B7 416082 V. Description of the invention (4)% is not easy to aggregate and Sake of state. Τ ^ | _ I— nn-ij. I nm I— mn I (please read the precautions on the back before filling this page), that is, the surfactant powder shown in Japanese Patent Application No. 7-131103 The granular lotion composition of this powder contains a high degree of composition of thio fatty acid alkyl esters, so it solves the problem of easy aggregation and solidification of water caused by "-thio fatty acid alkyl ester powders". The problem of slightly poor solubility "Among them, an ordinary granular lotion composition * is added with an alkaline component such as sodium osmium. This kind of alkaline ingredients can change the lotion into dangerous, and can improve the detergency of granular lotion composition. * The substances used as sleeping ingredients usually have higher water solubility. When the lotion composition is put into water, first, the aging component Ritsuya is dissolved, and the water becomes a test aqueous solution, and secondly, the anionic surfactant is dissolved in the alkaline aqueous solution. However, with regard to the interfacial active powder shown in Japanese Patent Application No. 7-131103, although the solubility improvement effect is greatly improved in neutral water, it tends to reduce the solubility improvement effect in aging aqueous solutions. β Therefore, when the granular cocoon washing composition containing such surfactant powder is actually used, the solubility of the surfactant powder is slightly reduced due to its mixing composition, and the cleaning performance cannot be fully exerted. Situation. Printed by the Shellfish Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs [Indications of Invention] The object of the present invention is to provide an interfacial activity formed by α-thio fatty acid alkyl esters as shown in Japanese Patent Application No. 7-131103.剤 Powder 膣 is not easy to make particles agglomerate and solidify the excellent effect, and can obtain good solubility of interfacial powder in dangerous water solvents, and can be charged &amp; play -6-This paper size applies Chinese national standard (CNS ) Α4 specification (2 丨 0X297 mm) 416982 A7 B7_____ V. Description of the invention (5) Granular cleaning composition for the cleaning performance of this surfactant powder. In order to solve the related problems, in the present invention, the sagium contains a mixed slurry of "-thio fatty acid alkyl ester, soap, water-soluble polycarboxylic acid and / or its salt, and the water content of this mixed slurry is concentrated to 15% Weight, and the temperature of the concentrate is below 7 ° C, and then powdered, and the soap containing 40% by weight or more of thio fatty acid alkyl ester, 1D by weight or more of soap is produced. A surfactant powder containing 0.001 to 5% by weight of a water-soluble polycarboxylic acid and / or a salt thereof is a special agent *, and the surfactant may be composed of the surfactant obtained by the production method. Granular lotion composition of powder. [The best form of the box for implementing the invention] The contents of the present invention are described in detail below. «-Thio fatty acid alkyl ester, as appropriate, represented by the following general formula (1) And the average number of broken atoms of saturated or unsaturated fatty acid residues is 10 to 20, and the number of fluorene atoms of ester alkyl groups is 1 to 5, and the anti-ions including this α-fluorinated fatty acid alkyl ester, Alkali metals, age-earth metals, and substituted or unsubstituted ammonium groups-generally suitable "R1 CHCOOR2 ........."

I SO 3 Μ (式中,Ri rCs-as院基或鍵你基, R 2 : C卜s烷基, K :鹼金屬,相當於一價之齢土類金靨,或為取代或無 取代之銨基^ ) 本紙張尺度逍用中國囷家標準(CNS ) A4規格(210X297公釐) ----一——-I.——Ί©------tr------ -* (請先閲讀背面之注意事項再填寫本頁) 經濟部中央標準局貝工消費合作社印裝 416982 A7 B7 經濟部中央標準局員工消費合作社印製 五、發明説明( Sr ) 1 1 此 a -硫代脂肪酸烷酯界面活性劑粉體中之混合量為 1 ί 4C % 重 量 以 上 &gt; 宜 為 4 0 84 % 重 量 〇 i 1 如 未 滿 4 0 % 重 量 時 &gt; 因 在 洗 劑 中 不 能 增加α -硫代脂 請 1 先 1 肪 酸 烷 酯 之 混 量 而 不 能 期 許 有 充 分 之 效果。 又 ♦ 超 出 閲 讀 1 % 重 量 時 則 導 致 降 低 界 面 活 性 劑 粉 體之溶 解 性 〇 背 面 1 之 1 BE 皂 最 好 烷 基 之 平 均 硪 原 子 數 為 10 18之飽 和 或 不 飽 注 意 J 和 之 脂 肪 酸 鹼 金 靥 鹽 t 脂 肪 酸 驗 土 類 金 屬鹽》 事 項 1 I 再 J 在 界 面 活 性 劑 粉 體 中 皂 之 混 合 量 為 1 0 重量% 以 上 ) 宜 填 寫 本 1 p 為 1 0 54 % 重 量 〇 如 未 滿 1 0 % 重 量 時 ♦ 則無法 充 分 發 揮 頁 1 I ΰ: -硫代脂肪酸烷酯與皂之相乘功效β 又,如超過5 4 %重 1 1 量 時 » 則 界 面 活 性 劑 粉 體 中 之 a •硫代脂肪酸烷酯的濃度 1 I 變 小 9 而 有 不 能 發 揮 洗 淨 能 力 之 現 象 〇 訂 據 由 以 上 之 混 量 » a -硫代脂肪酸烷酯與皂之比率, 1 其 重 量 比 為 4 3 : 57 89 : 11 &gt; 而 最 好 為 50 : 50 89 : 11 1 〇 又 9 上 逑 之 a -硫代脂肪酸烷酯及皂, 概具有衍自於 1 I 脂 肪 ΤΤΤ八 酸 部 位 » 此 脂 肪 酸 俗 使 用 由 牛 脂 &gt; 棕榈油 棕 櫚 核 1 1 油 等 所 衍 生 起 始 於 動 植 物 油 脂 或 合 成 脂 肪酸。 pt 水 溶 性 聚 羧 酸 * 例 如 適 用 丙 烯 酸 » 甲 基丙烯 酸 馬 來 Ί.&quot; 1 I 酸 衣 康 酸 之 任 何 一 種 所 生 成 之 均 聚 體 ,或選 串 其 2 種 1 1 以 上 所 生 成 之 共 聚 物 Ο 1 I 又 * 可 使 用 選 白 丙 烯 酸 甲 基 丙 烯 酸 ,馬來 酸 &gt; 衣 康 l 酸 之 1 種 以 上 與 使 用 馬 來 酸 m 與 共 聚 物。 1 1 水 溶 性 聚 羧 酸 之 抗 離 子 宜 用 選 白 m 金屬, 鹼 土 類 金 1 I 類 4 銨 之 1 種 以 上 Ο 其 中 最 具 適 用 者 為 鈉,鉀 等 鹼 金 1 1 8 1 1 1 本紙張尺度適用中國國家標準(CNS &gt; A4規格(2I0X297公釐) Α7 Β7 416382 五、發明説明(7 ) 屬0 又,水溶性聚羧酸之重量平均分子量為ΙΟΟΜ以下, 最好偽在3 00〜1 00 0 0之間β 如超過10000時,則實質上不能充分改善在«ί水溶液 中之溶解性效果,使游漿增粘,而有妨礙操作之情形。 可單獨或使用2種以上水溶性聚羧酸與水溶性聚矮$ 鹽之混合物。 水溶性聚羧酸及/或其鹽之混配量,偽設成為 代脂肪酸烷酯與皂结量(界面活性劑純成分 &gt;之0.01〜 5¾重量,而最好為0. 1〜3 %重量。如未滿0.01%菫橐 時,則對性水溶液中之溶解性無有實質之改善效果* 超過5 %重童時,則會降低界面活性劑粉體中之界面活 性劑濃度(《-硫代脂肪酸烷酷舆皂總量之比例),因此 不宜適用 又,關於此界面活性劑粉髏,除上述之成分外•可使 用沸石,碩酸鈉等無機組份或有機組份做為洗淨改善劑 或製造時之粉碎補肋劑。 更且,在此界面活性劑粉體中,因應其所需亦有可能 混合碕代脂肪酸烷酯以外之硫酸鹽,磺酸馥,辚酸 鹽等之陰離子界面活性劑。 以上碕酸鹽之具體例,可例示有以下之化合物。 (a)平均碩原子數18之烷基或具有鏈烯基之高级醇 硫酸酿鹽β (Μ鉋和或不飽和之酵殘基之平均磺原子數為10〜18在 本紙張尺度適用中國國家揉準(CNS ) Α4規格(210X297公釐) (請先閲读背面之注$項再填寫本f ) 訂 經濟部中央標準局员工消費合作社印製 經濟部中央操準局員工消費合作社印製 416982 a? B7 五、發明说明(8 ) 分子内附加平均0.5〜8莫耳之環氣乙烷之高级醇翔 乙酿。 以上之磺酸鹽,可例示有以下之化合物。 (c)平均碩原子數為10〜18之烷基或具有鏈烯基之直鏟 或分枝鏈之烷苯磺酸鹽。 (d&gt;平均磺原子數為10〜18之α -烯烴礒酸鹽。I SO 3 Μ (in the formula, Ri rCs-as group or bond group, R 2: C s alkyl, K: alkali metal, equivalent to a monovalent earth-type gold hydrazone, or substituted or unsubstituted Ammonium group ^) This paper size is in accordance with Chinese Standard (CNS) A4 (210X297 mm) ---- 一 ——- I .—— Ί © ------ tr ----- --* (Please read the precautions on the back before filling out this page) Printed by the Central Consumers Bureau of the Ministry of Economic Affairs Printed by the Co-operative Consumer Cooperatives 416982 A7 B7 Printed by the Consumers Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs 5. Description of Invention (Sr) 1 1 This The mixing amount of a-thio fatty acid alkyl ester surfactant powder is 1 ί 4C% by weight or more> preferably 4 0 84% by weight 〇i 1 If less than 40% by weight &gt; Because in the lotion Can not increase the amount of α-thiolipid, please add 1 to 1 fatty acid alkyl ester, and can not expect a sufficient effect. And ♦ Exceeding 1% by weight will lead to a decrease in the solubility of the surfactant powder. 1 on the back 1 BE soap The best alkyl group with an average 硪 atomic number of 10 18 is saturated or unsaturated. Note J and the fatty acid base Gold tin salt t Fatty acid soil test metal salt "Item 1 I and J J The amount of soap in the surfactant powder is more than 10% by weight) It is appropriate to fill in this 1 p is 1 0 54% by weight 〇 If less than 1 When the weight is 0%, ♦ the page 1 I cannot be fully used. 相:-the multiplication effect of thio fatty acid alkyl ester and soap β, and if it is more than 5 4% by weight, the amount is 1 »the a in the surfactant powder. The concentration of thio fatty acid alkyl ester 1 I decreases to 9 and there is a phenomenon that the washing ability cannot be exerted. 0 The quantity is based on the above amount »a-The ratio of thio fatty acid alkyl ester to soap, 1 Its weight ratio is 4 3: 57 89: 11 &gt; and preferably 50: 50 89 : 11 1 〇 9 9 a-thio fatty acid alkyl esters and soaps, which are derived from 1 I fatty TTT octanoic acid site »This fatty acid is customarily derived from tallow & palm oil palm kernel 1 1 oil, etc. Start with animal and vegetable fats or synthetic fatty acids. pt Water-soluble polycarboxylic acid * For example, suitable for acrylic acid »maleic acid methacrylate. &quot; 1 I Homopolymer produced by any one of itaconic acid, or selected from 2 kinds of copolymers produced by 1 1 or more 〇 1 I Again * You can use white acrylic acid, methacrylic acid, maleic acid> one or more of itaconic acid, and use maleic acid m and copolymer. 1 1 Water-soluble polycarboxylic acid anti-ion is suitable for white m metal, alkaline earth gold 1 type I 4 ammonium 1 or more 〇 Among them, alkali gold such as sodium and potassium 1 1 8 1 1 1 paper The scale is applicable to Chinese national standards (CNS &gt; A4 specification (2I0X297 mm) A7 B7 416382 V. Description of the invention (7) belongs to 0 In addition, the weight average molecular weight of water-soluble polycarboxylic acid is less than 100M, and it is best to fake it to 300 ~ If β between 1 00 0 0 exceeds 10,000, the solubility effect in the «ί aqueous solution cannot be substantially improved, and the slurry is thickened, which may hinder the operation. It may be used alone or two or more kinds of water-soluble Mixture of polycarboxylic acid and water-soluble polydwarf salt. The compounding amount of water-soluble polycarboxylic acid and / or its salt is presumed to be the fatty acid alkyl ester and the amount of soap (pure component of surfactant> 0.01 ~ 5¾wt, and preferably 0.1 ~ 3% by weight. If less than 0.01% 0.01, there will be no substantial improvement in solubility in aqueous solution * When it exceeds 5% by weight, the interface will be reduced Boundaries in active agent powder The concentration of surfactant ("-the proportion of the total amount of thio fatty acid alkane soap), so it is not suitable for use. Regarding this surfactant powder, in addition to the above-mentioned ingredients • Inorganic components such as zeolite, sodium ferrite can be used Or organic components can be used as cleaning improvers or pulverizers during manufacturing. In addition, in this surfactant powder, it is possible to mix sulfates and Anionic surfactants such as acid sulfonates, phosphonates, and the like. Specific examples of the above phosphonates include the following compounds. (A) Alkyl groups with an average number of 18 atoms or higher alcohol sulfates with alkenyl groups β (The average number of sulfonic atoms of M and unsaturated yeast residues is 10 ~ 18. In this paper, the Chinese National Standard (CNS) A4 specification (210X297 mm) is applicable. Please read the note on the back first.) Fill in this again f) Order Printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economics Printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economics Printed by the Consumers' Cooperatives of the Central Bureau of Economics 416982 a? Ethanol, a premium alcohol. Examples of the above sulfonates include the following compounds: (c) Alkyl sulfonates having an average number of master atoms of 10 to 18 or straight or branched alkenyl groups having alkenyl groups. (D &gt; average Alpha-olefin sulfonate having 10 to 18 sulfonic atoms.

此等陰離子界面活性劑之抗離子,通常適用者為鉀, 納等之齡金靥。 r·. I 此界面活性劑粉髏可經由調整淤漿,濃缩,冷卻, 粉艨化之步驟予以製造,玆對此界面活性劑粉體製法之 -實例具體説明如下。 即,首先混合硫代脂肪酸烷酯,皂舆水溶性聚羧 酸及/或其鹽,諝製水分含置為20 ~ 30%重量之混合淤 漿(游漿調整步驟)》 其次,使用濃縮装置,蒸發淤漿中之水分成為濃縮物 (濃縮步驟)。 此時此糗縮物之水分含量偽設定在15%重量以下,實 質上傺介於0.1〜15%重量之範圍,而最好傜設定在 10%重童以下。如濃縮物的水分含量超過15%重置畤, 嗣後即使將此濃縮物之溫度設在70°C以下,仍然呈塊狀 或淤漿狀,顔難以操作(成形,粉碎等),因而不能予以 粉體化。又,濃缩至未滿0.1%重量在工業上75為掻端 困難之事。接著,將上述濃编物冷卻使溫度降至70-C以 下後,直接予以粉碎,或以壓丸器成為九狀後粉碎,或 -10- 本紙張尺度適用中國國家標率(CNS ) A4規格(210X297公釐) (請先閱讀背面之注意事項再填寫本頁) 訂 416982 A7 經濟部中央標準局員工消費合作社印製 B7五、發明説明(9 ) 經薄Η化後再予以粉碎,粉碎化後成為界面活性劑粉體 (冷卻,粉體化步驟)。 上述冷卻後濃縮物之溫度偽在70 °C以下,通常宜在 0〜70°C,經由筒式冷卻機冷卻時則在20°C以下,而一. 般條在0〜2 fl°C。 上述淤漿之濃縮條件傜如後逑,一般濃縮後濃縮物之 溫度傜在70 °C以上之高溫^依界面活性劑之物性而言, 在此高溫下此濃縮物之附著性很強,如即時以粉碎機等 進行粉碎乃為不可能。但濃縮後經由冷卻步驟,即有可 能充分粉碎而形成低附箸性之塊狀物。 上述濃縮步驟所需之裝置及方法,包括有以大氣開放 型之混合機(縱型捏和機,螺條混合機等),在70〜120°C 之溫度下攪拌1〜10小時予以濃縮之方法,以及 有可能使用薄膜蒸發機〔蒸雷多(製品名Μ櫻製作所 産製);維告澤巴(製品名)(神岡潘的克公司産製控 乾機(製品名)(日立製作所製)等]由真空蒸發進行濃縮 之方法, . 圓筒式濃縮機〔CD乾燥機(製品名)(西村鐵工所産製) 等〕自行洗淨型濃縮機〔SC浦羅車薩(製品名)(栗本鐵 工所産製&gt;等〕,蓋斯速乾燥機(製品名)(大川原製作所 産製)等。 又,在常壓以1 Q 0-C以上加熱淤漿,接著在減壓之蒸發 罐進行沖水蒸發,由於可降低濃縮後之溫度因此頗有效 率。此時可使用SVC濃縮機(製品名)(佐久間製作商産品) -1 1 - (請先聞讀背面之注意事項再填寫本頁) 訂 -線气 本紙張尺度適用中國國家標準(CNS ) A4^格(210X297公釐) 經濟部中央標準局貝工消費合作社印裝 416382 A7 B7 五、發明説明() 等裝置。 上述冷卻步驟所需之裝置及方法,可使用空冷法或輸 帶式真空冷卻機〔貝爾馬庫斯(製品名)(大川原製作所 産製);不銹鋼輸帶式冷卻裝置(山都貝克公司産製)等 進行冷卻。 待別在冷卻後,直接薄Η化所用之裝置,以圓筒式冷 卻機C圓筒薄Η機(製品名)(楠木機械製作所産製;雙圓 筒乾燥機(製品名)(卡因果公司産製)〕等較具有效率。 依此所得薄片之狀態,有可能製成,以α-硫代脂肪 酸烷酯為目的m及含有皂之界面活性劑産品。 關於粉體化步驟,在九狀化之際對1Q0重量扮界面活 性劑如添加1〜30重量份無機粒子時,容易成彤為九狀 同時界面活性劑粉體有良好之流動性。 其中所使用之無機粒子,最好偽選自硫酸鈉,磺酸銷 ,磺酸氫鈉,沸石,撤粒子氣化矽,矽酸鈣群之一種β 粉碎機俗使用非自磨(製品名)(細川米克隆公司産製) ,連磨(製品名)(岡田精工公司庫製)等。 此時,因使用粉碎助劑而有效率地予以粉碎。 粉碎助劑之平均粒徑最好為20;/ m以下之無機粒子, 使用沸石,白灰,白碳等,其用里偽對以上濃縮物100 重量份宜使用1〜20重量份,最好為2〜10重量份。 在薄Η化或粉碎後,欲提髙流動性等物性改良而混合 平均粒徑20# ra以下之無機粒子,亦可以被覆。使用沸 石,白灰,白碩等無機粒子。被覆童傜對100重量份濃 -12- 本紙張尺度適用中國國家標準(CNS ) A4規格(2丨OX297公釐) (請先閲讀背面之注意事項再填寫本頁)The anti-ions of these anionic surfactants are usually potassium, sodium, and the like. r ·. I This surfactant powder can be manufactured through the steps of adjusting the slurry, concentrating, cooling, and powdering. The method of this surfactant powder system is described below as an example. That is, firstly, a thio fatty acid alkyl ester, a soap-soluble polycarboxylic acid and / or a salt thereof are mixed, and a mixed slurry containing 20 to 30% by weight of water is prepared (the slurry adjusting step). Second, a concentration device is used. The water in the slurry is evaporated to become a concentrate (concentration step). At this time, the moisture content of this condensate is pseudo-set to 15% by weight or less. Actually, it is in the range of 0.1 to 15% by weight, and preferably it is set to 10% by weight or less. If the moisture content of the concentrate exceeds 15%, it will be lumpy or sludge even after the temperature of the concentrate is set below 70 ° C. It will be difficult to handle (forming, crushing, etc.), so it cannot be treated. Powder. In addition, industrial concentration of 75% to 0.1% by weight is difficult. Then, after cooling the above-mentioned knitting fabric to reduce the temperature to below 70-C, it can be crushed directly, or crushed by a pellet press, or -10- This paper size applies the Chinese National Standard (CNS) A4 specification (210X297 mm) (Please read the notes on the back before filling this page) Order 416982 A7 Printed by the Consumers Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs B7 V. Invention Description (9) After thinning, shredding and shredding Then it becomes the surfactant powder (cooling, powdering step). The temperature of the above-mentioned cooled concentrate is pseudo below 70 ° C, usually 0 ~ 70 ° C, and below 20 ° C when cooling through a barrel cooler, and the general strip is at 0 ~ 2 fl ° C. The concentration conditions of the above slurry are as follows. Generally, the temperature of the concentrate after concentration is above 70 ° C. ^ According to the physical properties of the surfactant, the concentration of the concentrate at this high temperature is very strong, such as It is impossible to perform pulverization with a pulverizer or the like immediately. However, after condensing, it is possible to sufficiently pulverize and form a low-adhesive mass through a cooling step. The device and method required for the above concentration step include an air-open type mixer (vertical kneader, ribbon mixer, etc.), which is stirred for 1 to 10 hours at a temperature of 70 to 120 ° C to be concentrated. Method, and the possibility of using a thin-film evaporator [Zendredo (manufactured by Makura Seisakusho Co., Ltd.); Verzabba (manufactured by name) (Kamioka Panke's controlled dryer (manufactured name) (Made by Hitachi) ) Etc.] Method of concentration by vacuum evaporation,. Cylindrical thickener [CD dryer (product name) (made by Nishimura Iron Works), etc.] Self-cleaning type thickener [SC Puro Sa (product name) (Made by Kurimoto Iron Works &gt; etc.), gas speed dryer (product name) (made by Ogawara Seisakusho), etc. The slurry is heated at 1 Q 0-C or more at normal pressure, and then evaporated under reduced pressure. The tank is flushed with water to evaporate, which is very efficient because it can reduce the temperature after concentration. At this time, you can use the SVC thickener (product name) (Sakuma manufacturer's product) -1 1-(Please read the precautions on the back before filling (This page) Staple-line paper size China National Standard (CNS) A4 ^ (210X297 mm) Printed by the Central Standards Bureau of the Ministry of Economic Affairs, Shellfish Consumer Cooperative, 416382 A7 B7 5. Description of the invention () and other devices. The devices and methods required for the above cooling steps can be air-cooled Method or conveyor vacuum cooler [Bell Marcus (product name) (made by Ogawara); stainless steel conveyor cooling device (made by Sandubek), etc. for cooling. Don't directly cool after cooling. The equipment used for trioxide is more efficient with a cylindrical cooler C-cylinder thin-header (product name) (made by Nanmu Machinery Manufacturing Co., Ltd .; a double-cylinder dryer (product name) (made by Cainkuo)). Based on the state of the obtained flakes, it is possible to produce a surfactant product containing α-thio fatty acid alkyl esters and a soap-containing surfactant. Regarding the powdering step, the interface is formed on the basis of 1Q0 weight when it is nine-shaped. When the active agent is added with 1 to 30 parts by weight of inorganic particles, it is easy to be formed into nine shapes and the surfactant powder has good fluidity. Among them, the inorganic particles used are preferably selected from sodium sulfate and sulfonic acid. , Sodium hydrogen sulfonate, zeolite, a kind of β-pulverizer which is used to remove particles of vaporized silicon and calcium silicate. Non-self-grinding (product name) (manufactured by Hosokawa Mikron Co., Ltd.), continuous grinding (product name) (Okada Seiko (Manufactured by the company library), etc. At this time, it is effectively pulverized due to the use of a pulverization aid. The average particle size of the pulverization aid is preferably 20 μm or less of inorganic particles, and zeolite, white ash, white carbon, etc. are used. For 100 parts by weight of the above concentrate, it is preferable to use 1 to 20 parts by weight, and preferably 2 to 10 parts by weight. After thinning or pulverizing, to improve physical properties such as fluidity, the average particle size is 20 #. Inorganic particles below ra can also be coated. Inorganic particles such as zeolite, white ash, Bai Shuo are used. Coated Tong Zhi is 100 parts by weight -12- This paper size applies Chinese National Standard (CNS) A4 specification (2 丨 OX297 mm) ) (Please read the notes on the back before filling this page)

416982 A7 B7 五、發明説明(11 ) 縮物使用1〜20重量份無機粒子,最好為1〜5重量份p ' 依此所製造之界面活性劑粉體,使用噴霧乾燥法以習 知方法或攪伴造粒法等其他方法所製造之他種洗劑成分 ,一起迪粒或混合粉髏而可生成為粒狀洗劑組成物。 此時,即將粒狀洗劑組成物中之《-硫代脂肪酸烷酯 之濃度變成為1〜50重量%。如未谋1重量%時,卽無 法發揮《-硫代脂肪酸烷酯之效果,超過50重量%時, 即有做為鹾性組扮或鈣螯合劑组份等洗劑必要組份量有 不足之虔》 在造粒之際,同時將本發明之界面活性劑粉體與其他 之洗劑成分混合,造粒,形成為粒狀洗劑組成物。此造 粒方法包括有,捏和(壓密化}後予以粉碎之方法(壓密 造粒法),及由攪拌加以造粒之方法(提拌造粒法&gt;。 捏和所用裝置,包括有,連缠式捏和機〔KRC捏合機 (製品名)(栗本鐵工所公司製造)等〕,批式捏和機〔设 型捏和機(製品名HDALT0N公司製造}等〕〇粉碎用裝置 邸包括有弗滋磨(製品名 &gt;(細州米克隆公旬製造),速磨 (製品名 &gt;(岡田精工公司製造)等。 經濟部中央標準局員工消費合作社印製 (請先閱讀背面之注意事項再填寫本頁) 又,同上述製造界面活性劑粉體一般,在粉碎之際使 用粉碎助劑,如此得以提高粉碎效率。此粉碎助劑宜為 平均粒徑20# a以下之無機粒子,可用沸石.白灰•白 磺等。粉碎助劑之用量,對捏和後之捏和物重蛋份, 宜使用1〜20重量份,而最好為2〜10重量份。 攪拌造粒機包括有,雷葛混合機(製品名 &gt;(松波公司 &quot;13&quot; 本紙張尺度適用中國國家標準(CMS ) A4規格(210X297公釐) A7 B7 416982 五、發明説明(i2 ) 製造),修凝混合機(製品名)(抛力克公司製造),高速 混合機 &lt; 製品名)(澡江工業公司製造)等。 (請先聞讀背面之注意事項再填寫本頁) 再者,藉混合粉體以製造粒狀洗劑組成物時,最好將 其他洗劑成分之粉體(宜為高容積密度粒子)與界面活性 劑粉體與粉體混合。 上述其他洗劑成分之高容稹密度粒子,可使用將其他 洗劑成分之噴蓀乾燥粒子經壓密化後粉碎所製造者,亦 可使用不經噴耢乾燥法而以攪拌造粒,轉動造粒,流動 雇造粒等其他方法所製造者。 對造粒或混合粉體後之粒狀洗劑組成物,可添加粉徑 m以下之沸石微粉體等無機化合物做為流動性改良 劑β 更且,可混合洗淨改善劑之螯合劑组份,酵素等粉體 。其中所使用之螯合剤組份,則包栝有沸石粉體,層狀 砂酸鹽,馬來酸一丙烯酸鈉之共聚物,沒-胺基丙酸醋酸 鈉等。 又,可施予抑制起塵用非離子.界面活性劑或其水溶液 等之噴霧或陚香所需之噴蓀香料處理。 以上非離子界面活性劑,則包括如下所述》 經濟部中央標準局貝工消費合作社印製 (a)由以下一般式(II)所代表之脂肪酸聚氧烷撐烷醚。 0416982 A7 B7 V. Description of the invention (11) Use 1 ~ 20 parts by weight of inorganic particles for the condensate, preferably 1 ~ 5 parts by weight p 'Surfactant powder manufactured according to this, using spray drying method in a conventional way Or other lotion ingredients made by other methods, such as agitation and granulation, can be disintegrated together or mixed with powder skull to form a granular lotion composition. At this time, the concentration of the "-thio fatty acid alkyl ester" in the granular lotion composition was changed to 1 to 50% by weight. If 1% by weight is not planned, the effect of 卽 -thio fatty acid alkyl ester cannot be exerted. When it exceeds 50% by weight, it is necessary to use a lotion such as an alkaline component or a calcium chelating agent component. Pie "At the same time of granulation, the surfactant powder of the present invention is mixed with other lotion ingredients at the same time, and granulated to form a granular lotion composition. This granulation method includes a method of kneading (compacting) and pulverizing (compacting granulation method), and a method of granulating by stirring (mixing and granulating method). The equipment used for kneading includes Yes, continuous kneader [KRC kneader (product name) (Kurimoto Iron Works Co., Ltd.), etc.], batch kneader [type kneader (product name: HDALTON company), etc.] The facilities include Fuzima (product name &gt; (manufactured by Hosokawa Mikron), speed grinder (product name &gt; (manufactured by Okada Seiko Co., Ltd.), etc .. Printed by the Consumer Cooperative of the Central Standards Bureau, Ministry of Economic Affairs Read the precautions on the reverse side and fill in this page) Also, as with the surfactant powders mentioned above, a pulverization aid is used during pulverization to improve the pulverization efficiency. The pulverization aid should be less than 20 # a average particle size For inorganic particles, zeolite, white ash, white sulfon, etc. can be used. The amount of pulverization aid is 1 to 20 parts by weight, and most preferably 2 to 10 parts by weight for the kneaded product. Granulators include, Regal mixer (product name &gt; ( &Quot; 13 &quot; This paper size is applicable to Chinese National Standard (CMS) A4 specification (210X297 mm) A7 B7 416982 V. Description of invention (manufactured by i2)), repair mixer (product name) (manufactured by Leric) , High-speed mixer &lt; product name) (manufactured by Yujiang Industries Co., Ltd.), etc. (Please read the precautions on the back before filling out this page) Furthermore, when mixing powders to make granular lotion compositions, It is good to mix the powder of other lotion ingredients (preferably high bulk density particles) with surfactant powder and powder. For the high-capacity and high-density particles of the other lotion ingredients mentioned above, spraying other lotion ingredients can be used. The dry granules are crushed after being compacted, and can also be produced by other methods such as stirring granulation, rotary granulation, mobile granulation, etc. without spray drying. After granulating or mixing powder For granular detergent compositions, inorganic compounds such as zeolite fine powder with a powder diameter of m or less can be added as a fluidity improver β. In addition, chelating agent components of detergent improvers, powders such as enzymes can be mixed. Use Chelate The combined components include zeolite powder, layered oxalate, copolymer of sodium maleate-acrylic acid, and sodium-aminopropionic acid acetate, etc. In addition, nonionics for dust suppression can be applied. .Surface active agent or its aqueous solution spray or scented perfume treatment required for fragrant incense. The above nonionic surfactants include the following: "Printed by the Shellfish Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs (a) by the following Fatty acid polyoxyalkylene alkyl ether represented by general formula (II). 0

II R 3 C (AO) nOR 4 .....(II) U3 CO:碩原子數6〜2C之飽和或不飽和之脂肪酸殘基 A0:碩原子數2〜4之氣烷撐基或由其所混合之氣烷 -14&quot; 本紙張Λ度逍用中國國家樣準(CNS ) A4规格(21〇&gt;&lt;297公嫠) 經濟部中央標準局員工消費合作社印裝 416982 A7 B7 五、發明説明(上3 ) 指 η :表示氣烷撐之平均加成莫耳數,3〜3 0 (包含無 規,分段加成者) R 4 : C 1 烷基) (b)飽和或不飽和之直鋪或分枝鏈醇之碩鏈8〜18,氣 乙烯之平均加成莫耳數3〜30之聚氣乙烯烷醚。 &lt;c)飽和或不飽和之直鍵或分枝鏈醇之硪鍵8〜18,氣乙 烯之平均加成奠耳數3〜3Q,氣化丙烯之平均加成莫 耳數2〜30之聚氧乙烯聚氣丙烯烷醚β 又起塵抑制粘合劑,傜在上述非離子界面活性劑之外 ,融點在3 5 Ό以下之聚乙醇或聚丙二醇等亦有效。 更且,在上述所例示界面活性劑粉體以外之其他洗劑 成分當中,無機紐份包括有三聚磷酸鈉,焦磷酸銷等。 又除此之外,關於其他之洗劑成分,可混配以檸様酸鈉 ,乙烯二胺四醋酸鈉,硝基三醋酸鹽,聚丙烯酸納,丙 烯酸鈉-無水馬來酸銷共聚物,聚乙縮醛羧酸鹽,羥亞 胺二琥珀酸納等之鈉離子捕捉組.份;羧甲基缕維素,聚 乙二醇等之再污染防止劑;對甲苯磺酸鹽,甲苯磺酸鹽 ,二甲苯磺酸盏,尿素等之粘度調整劑;第四级銨鹽, 皂土等之柔軟劑;亞硫酸鈉,亞硫酸氳鈉等之還原劑; 過磺酸鈉,過硼酸鈉等之漂白劑;乙烯二胺四醋酸鹽, 辛醯氣苯磺酸等之漂白活性劑;螢光增白劑;香料;酵 素;色素;白磺等。 至於酵素,可添加以加水分解酵素,還原酵素,轉移 -15- 本紙張尺度適用中國國家標準(CNS ) A4g ( 210X297公釐) (請先閲讀背面之注意事項再填寫本頁)II R 3 C (AO) nOR 4 ..... (II) U3 CO: saturated or unsaturated fatty acid residues with 6 ~ 2C master atoms A0: gas alkylene groups with 2 ~ 4 master atoms or by The mixed gas alkane-14 &quot; this paper Λ degree free use Chinese National Standard (CNS) A4 specifications (21〇 &gt; &lt; 297 gongsong) Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs 416982 A7 B7 V. Description of the invention (above 3) means η: represents the average addition mole number of gas alkylene, 3 ~ 3 0 (including random, segmented addition) R 4: C 1 alkyl) (b) saturated or not Saturated straight-chain or branched chain alcohols with a master chain of 8-18, and the average addition of gaseous ethylene with a mole number of 3-30 is a polyalkylene oxide ether. &lt; c) Saturated or unsaturated straight or branched chain alcohols 8 to 18, the average addition mole number of gas ethylene is 3 to 3Q, the average addition mole number of gasified propylene is 2 to 30 Polyoxyethylene polypropene ether beta also has a dust suppression adhesive. In addition to the above non-ionic surfactants, polyethanol or polypropylene glycol with a melting point of 3 5 Ό or less is also effective. Furthermore, among the lotion ingredients other than the surfactant powders exemplified above, the inorganic linker includes sodium tripolyphosphate, pyrophosphate, and the like. In addition, for other lotion ingredients, sodium citrate, sodium ethylenediamine tetraacetate, nitrotriacetate, sodium polyacrylate, sodium acrylate-anhydrous maleic acid copolymer can be blended, Polyacetal carboxylate, sodium hydroxyimide disuccinate and other sodium ion capture components. Component; Carboxymethyl avidin, polyethylene glycol and other recontamination preventive agents; p-toluenesulfonate, toluenesulfonate Viscosity modifiers of acid salts, calylene xylene sulfonate, urea, etc .; softeners such as fourth-grade ammonium salts, bentonite, etc .; reducing agents such as sodium sulfite, sodium sulfite, etc .; sodium persulfonate, sodium perborate, etc. Bleaching agents; bleaching activators of ethylene diamine tetraacetate, octane benzene sulfonic acid, etc .; fluorescent whitening agents; perfumes; enzymes; pigments; white sulphur. As for enzymes, you can add water-decomposing enzymes, reducing enzymes, and transfer -15- This paper size applies Chinese National Standard (CNS) A4g (210X297 mm) (Please read the precautions on the back before filling this page)

A7 B7 416982 五、發明説明(j·4 ) 酶,裂解酶,異構酶,連接酶,合成酶等β較好者為, 蛋白酶,角蛋白酶,脂酶,酯酶,纖維素酶,澱粉酶, 支鏈澱粉_,果膠分解酶,角質酶,配糖酶,葡聚糖酶 ,磨固酵氣化酶,過氧化酶等ο 含有本發明之界面活性剤粉體以及其界面活性劑粉醱 之粒狀組成物的水分含量為1〜15重量%,而最好為3〜 10重童%。如未滿1重量%時則無法獲得充分溶解性, 超15重量96時,則不但難以製造,而且會增大界面活性 剤粉體或粒狀洗劑組成物本身之荷重在保存時因吸濕而 使粒子凝集,容易發生珠狀〇 此等界面活性劑粉體及粒狀洗劑組成物之平均粒徑宜 為200〜1500;« bu如未滿200# a時則會增加微粉,而降 低粉雔流動性,投入於水中時則會凝集而形成國珠化, 致減低溶解性。如超過ISOO^bi畤,則因表面積減少而 減低溶解性β 又此等界面活性劑粉體及粒狀洗剤組成物之容積密度 ,通常為〇.4g/cn3以上,惟最好係在0.5〜1.2g/cn3 之間。 由本發明所獲得之界面活性劑粉體,則因水溶性聚羧 酸及/或其鹽之作用,使硫代脂肪酸烷酯輿皂具有 高濃度,而改良鹼性水溶液中之溶解性。 由於少量之水溶性聚羧酸及/或其鹽則能獲得相當之 效果,故成本之增加槿為有限。 更且,由皂之作用,即使《-硫代脂肪酸烷酯之濃度 —1 6 — 本紙張尺度適用中SH家揉準(CNS ) A4現格(210X297公釐) (請先閲讀背面之注意事項再填寫本頁) 訂 經濟部中央標準局負工消費合作社印製 416982 A7 B7 五、發明説明(π ) 很高,亦有難以凝集.固化之效果。 由於此界面活性劑粉體之製法,不用噴耪乾燥法來製 造,而因不會有噴霧乾燥法能量之損失,無有使粒子在 空氣中浮遊而使作業環境惡化之情形。更且,濃縮物之 溫度在70°C以下容易使之粉體化,因而可以有效率地以 低成本製造界面活性劑粉體。特別是此界面活性劑粉體 之製法,傺藉上逑終止濃縮步驟時濃縮物之水分含量, 以及粉體化前濃縮物最適宜之溫度,縱然α-硫代脂. 肪酸烷酯之濃度很高,亦能容易使之粉體化,誠為一 種極有效率之製造方法。 又,將此界面活性劑粉體與其他成分一起造粒,或與 其他洗劑成分之粉體(宜為高容積密度粒子)混合,卽可 在鹼性水溶液中良好之低溫溶解性獲得不易凝集.固化 之粒狀洗劑組成物。 玆將本發明之實施樣態棄逑如下。 又關於本發明傜全部包含有以下所成構成之組合。 (i)由本發明所獲得之界面活性劑粉體,宜含有4 0重量% 以上之硫代脂肪酸烷酯,最佳傺40〜84重童96, 10 經濟部中央標準局貝工消費合作社印製 (請先閲讀背面之注意事項再填寫本頁) 重量%以上之皂,最佳為0〜5 4重量%,對α -硫代脂肪 酸烷酯與皂的總屋俗含有0.01〜5重量%之水溶性羧酸 及/或其鹽。 由以上之混合量,《-硫代脂肪酸烷酯與皂之比率, 以重里比為計為43: 57~89: 11,而最好為50: 50〜 89: 11〇 本紙張尺度適用中國國家標準(CNS ) Α4規格(210X297公釐) 鯉濟部中央標準局另工消費合作社印装 416982 A7 B7 五、發明説明(16 ) UU關於水溶性羧酸及/或其鹽,宜適用丙烯酸,甲基 丙烯酸,馬來酸,衣康酸所選取之1種所形成之均聚物 ,或從其中選取2種以上所形成之共聚物。 亦可使用由丙烯酸,甲基丙烯酸,馬來酸,衣康酸所 選取之1種以上與馬來酸酐所形成之共聚物。 水溶性聚羧酸之抗離子,宜使用由齡金屬,鹺土類金 屬,銨所選取之1種以上β其中最宜適用者為納,鉀 等之驗金屬。 水溶性聚羧酸之重量平均分子量為lflOdO以下,而最 好為300〜10G00。 水溶性聚羧酸及/或其鹽之界面活性劑粉體中之混配 量偽對α -硫代脂肪酸烷酯與皂總量(界面活性劑純分&gt; 之0.01〜5重量%,而最好為fl.l〜3重量%。 (iii)本發明界面活性劑粉體之製法,傜将水分含量20 〜30重量%之包含硫代脂肪酸烷酯輿皂和水溶性聚 羧酸及/或其强之混合淤漿原料予以濃缩,生成水分含 量在15重量%以下•朗在(ί·1〜15重量%之範圍,而最 好為10重量%以下之濃缩物•其次,此濃縮物之溫度在 7〇°〇以下,通常在〇〜7B«C之後,將此濃縮物直接粉碎 ,或由壓丸器形成九狀後予以粉碎,或粉碎薄片,使之 粉體化,生成界面活性劑粉體之方法。 上述濃縮物粉體化前之溫度,如由圓筒式冷卻機予以 冷卻時最好在20°C以下,通常為0〜20°Ce Uv&gt;可製備含有由本發明所獲得界面活性劑粉體之粒狀 -18- 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) !| : I ί- ii ^ ^^1 ^1 (請先閲讀背面之注意事項再填寫本頁) 訂 A7 B7 416982 五、發明説明(l7 ) 洗劑組成物〇可將此界面活性劑粉體與其他之洗剤成分 一起造粒或潺合粉體而生成粒狀洗劑組成物。 Γ 1 I— ^—^1 ϋϋ —mu (請先閲讀背面之注意事項再填寫本買) 此時粒狀洗劑組成物中之《-硫代脂肪酸烷酯之濃度 最好為1〜50重量%。 造粒方法包括有,捏和(騸密化&gt; 後粉碎之方法(壓密 造粒法 &gt; 輿攙拌造粒之方法(摄拌造粒法 又,混合粉體製造粒狀洗剤組成物時,則有宜將其他 洗劑成分之噴霧乾燥粒子壓密後予以粉碎形成高容積密 度(粉體 &gt; 後,將此粉體與本發明之界面活性剤粉體混合 ,或將噴霧乾燥法以外之由攪拌造粒,轉動造粒,流動 層造粒等方法所製造之其他洗劑成分之高容積密度粒子 (粉體)與本發明之界面活性劑粉醱形成粉體混合之方法。 (V)由本發明所獲得之界面活性劑粉體以及含有此界面 活性劑粉體之粒狀洗劑组成物,其水分含量宜為1〜15 重量%,最好為3〜10重量%,其平均粒徑為2 0 0〜1500 Αβ,容積密度一般為〇.4g/cB3以上,而最好為0.5~ 1 . 2 g/ cb 3 0 . 〔實施例〕 經濟部中央摞準局貝工消費合作社印裝 以下,玆由賁施例詳細說明本發明,如無特別記述或 表明所指%偽表示重量%。 * 首先,針對實施例所採用鹾性水溶液中之低溫(5-C) 溶解性試驗之評估方法(溶解殘渣測定法)説明之。 (溶解殘渣澜定法) 在1公升燒杯中置入1公升之5&quot;C水,投入3克之一 -1 9- 本紙張尺度適用中國國家標準(CNS ) Α4規格(210Χ297公釐) A7 B7 416982 五、發明説明(β ) (請先閱讀背面之注意事項再填寫本頁) 定粒徑之碳酸鈉與5克試料,在25Qrpm之定速下攪拌8 分鐘。經由預計重量之耐倫針織物布(以下稱做耐倫布) 加以過濾,此耐倫布在1 0 5 °C乾燥6小時後加以計量。 由過濾乾燥後耐倫布之重量,扣除最初之耐倫布重量 所示之重量做為供試料之溶解殘渣重量,算出對最初試 料重量之溶解殘渣之tb例(重量% &gt;。 〔I]界面活性劑粉體之製造 (實施例1〜6 ) 依照表1所示之組成,混合α-硫代脂肪酸甲酯銷, 肥皂 &lt; 平均碩原子數12〜18之鈉鹽),聚丙烯酸鈉(水溶 性聚羧酸鹽)諝整成為游漿。將此淤漿,使用縱型攪拌 混合機(道而頓公司製造),在套管溫度90 °C之條件下蒸 發水分,製造 然後,除實施例4以外,將上述濃縮物使用筒式薄片 I»--------- .....- 機(製品名)(楠木機械製作所製)進行冷卻至表1所示冷 .----------------- 卻步驟後之溫度為止,同時加以薄片化。實施例4即將 ^--- . 經濟部中央標準局員工消費合作社印製 上述濃縮物放置於室溫,冷卻至.表1所示冷卻步驟後之 溫度,將此濃縮物與表1所示用量之沸石(記載於表1 中丸狀成形時之添加物)混合後,所獲得之塊狀物使用 雙重式壓丸器(製品名)(不二粉公司産製,型式:EXDFJS -6 0 )做成直徑約1 0 til η ,長度約1 5 m m之九狀。 其次,將實施例1〜6之薄Η或壓九,與對100重量份 界面活性劑純分,將此純分與表1所示用量之沸石(粉 碎肋劑)一起,使用裝設有孔徑2ΒΒ1篩網之斐滋磨機(製 品名)(細川米克隆公司製造,型式:ΡΚΑ-3),通過以 -20&quot; 本紙張尺度適用中國國家標準(CNS ) Α4说格(210X297公釐) 416982 A7 B7 __ 五、發明説明(19 ) 15&quot;C之冷風予以粉碎使之粉體化,得界面活性劑粉體。 (請先閲讀背面之注意事項再填寫本頁} 所得界面活性劑粉醴之性狀,組成及溶解殘渣測定結 果則併合如表1所示。 (比較例1〜3 ) 依照表2所示之組成,混合α-硫代脂肪酸甲酯鈉, 肥皂 &lt; 平均碳原子數12〜18之鈉鹽),並因應其所需加入 聚丙烯酸納調製成淤漿。此淤漿仿上述實施例1〜6之操 作方式,製成濃编物。 然後,將比較例2以外之上述濃縮物,使用筒式薄Η 機(製品名 &gt;(楠木機械製作所製造),將其冷卻至表2所 示冷卻步驟後之溫度,同時使之薄片化。至於比較例2 ,則仿實施例4之方法,經由冷卻作成直徑約·»,長 度約1 5m«之壓丸ρ 其次,將上述比較例1〜3之壓九式薄Η,依照上逑 實施例1〜6相同方法予以粉體化而得界面活性劑粉體。 所得界面活性劑粉體之性狀,組成以及溶解殘渣測定 結果則併合如表2所示》 鼸於比較例2由於冷卻溫度高因此無法成形為丸狀, 至於比較例3則因澳縮物水分高而不能粉碎。 經濟部中央標準局貝工消費合作社印裝 由以上實施例1〜6以及比較例1〜3之結果,如與使用 水溶性聚羧酸及/或其鹽時比較,則以不使用水溶性聚 羧酸及/或其鹽之比較例1之界面活性劑粉體有較多之 溶解殘渣,結果其溶解性變成低劣β 又,冷卻溫度較高之比較例2,輿濃縮物水分較高之 -2 1-本紙乐尺度逍用中國囷家標準(CNS ) Α4規格(210X297公釐) A7 B7 416982 五、發明説明(2〇 ) 比較例3,均無法加以粉體化。因此可知在製造界面活 性劑粉體當中,重量者俗將濃縮物之水分與粉體化前濃 縮物溫度設定在最適宜之條件。 —方面,關於本發明實施例1〜6之界面活性劑粉體, 其中之任何實例較之比較例1有良好之低溫溶解性,容 易粉體化,含有高濃度之硫代脂肪酸烷酯與肥皂, 可知俗屬一種在鹼性水溶液中有良好低溫溶解性之界面 活性劑粉體。 (請先閱讀背面之注意事項再填寫本頁) -=β 經濟部中央標準局貝工消費合作社印裝 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 416982 A7 B7 五、發明説明() 〔表1〕 表1 :界面活性劑粉體之製造搽件及性狀與 組成(實施例) 經濟部中央標举局貝工消費合作社印製 實施例编號 1 2 3 4 5 6 淤漿 α-SF 濃度(%)β1 33.7 44.7 58.7 44.7 45.3 42.2 肥皂濃度 33.7 22.0 8.0 22.0 22.3 20.8 (cr-SF/皂比率) 50/50 67/33 88/12 67/33 67/33 67/33 聚丙烯酸納 平均分子量 10000 3000 300 3000 3000 3000 抗活性劑濃度(%〉*2 0.1 1 1 1 0.01 5 水分(%) 29.1 28.2 26.8 28*2 27*8 29.7 義縮物水分(%) 10.0 5.0 3.0 5.0 5.0 5.0 濃縮後之溫度(eC&gt; 90 冷卻步驟後之溫度&lt;°C&gt; 30 15 15 50 15 15 壓丸成形時之添加物*3 沸石 抗活性劑獏度(%)·2 - - - 10 — - 破碎肋劑 沸石 抗活性_澳度(%)*2 5 界面活性劑粉體之性狀 容積密度(g/cc) 0.4〜fl.5 平均粒徑(/*»〇 400〜500 溶解殘渣(%) 9 7 9 5 9 9 界面活性劑:粉成· a -SFjggF (%^·1 40.6 55.9 73.6 50.7 56.5 54.1 肥皂濃度(%) 40.6 27.6 10.0 25.0 27.8 26.6 永分 (¾) 10.0 5.3 3.4 5.7 5.3 5.3 * 1)α,SF:脂肪酸殘基之硪數為Η〜16之α -硫代脂 防酸烷酯納 &quot;2)抗活性劑獲度:對硫代脂肪酸烷酯與肥舂總量 之tb例 * 3)躔九成形時添加物:實施例4以外由筒式薄Η機 (楠木機械製作所製造)將濃縮物冷卻後,因係直 接薄Η化而不使用添加物。 -23- 本紙今^度適用中國圃家標準((:阳)/14規格(21〇\297公釐) (請先閲讀背面之注意事項再填寫本頁) 訂 1, ! 416982 A7 B7 % /{ 度 量濃 納子劑 酸一分性 烯均活 丙/平抗 聚, 五、芦|月2呼明(22 ) 表2:界面活性劑粉體之製造條件及性狀與組成(比 較例) 實施例编號 1 2 3 游發 α-SF 嬝度(96)*1 4 5.3 4 4 . 7 4 4 .7 肥皂濃度 22.3 2 2 . 0 2 2 .0 (or-SF/皂比率) 6 7 / 3 3 6 7 / 3 3 6 7 / 3 3 水分(%) 27.8 28.2 28.2 濃縮物水分(%) 10.0 5.0 16.0 濃縮後之溫度(°C ) 90 冷卻步驟後之溫度(°C) 1 5 8 0 1 5 壓九成形時之添加物s3 沸石 抗活性劑濃度(%)*2 - 20 破碎肋劑 沸石 抗活性劑濃度5 成形不可 20 (請先閲讀背面之注意事項再填寫本頁) 粉 劑度徑渣 性密粒殘 活積均解 面容平溶 界A7 B7 416982 V. Description of the invention (j · 4) Enzymes, lyases, isomerases, ligases, synthetases, etc. β is preferably protease, keratinase, lipase, esterase, cellulase, amylase , Amylopectin, pectinolytic enzyme, cutinase, glycosylase, glucanase, glutenase gasification enzyme, peroxidase, etc. ο Contains the interfacial active powder and the interfacial active agent powder of the present invention The moisture content of the granular composition of osmium is 1 to 15% by weight, and preferably 3 to 10% by weight. If it is less than 1% by weight, sufficient solubility cannot be obtained. If it exceeds 15% by weight, it will not only be difficult to manufacture, but also increase the interfacial activity. The load of the powder or granular detergent composition itself will be hygroscopic during storage. When the particles are agglomerated, beads tend to occur. The average particle size of these surfactant powders and granular lotion compositions should be 200 ~ 1500; if bu is less than 200 # a, fine powder will increase and decrease. The powder is fluid, and when it is put into water, it will aggregate and form a national pearl, which will reduce the solubility. If it exceeds ISOO ^ bi 畤, the solubility β is reduced due to the decrease in surface area. The bulk density of these surfactant powders and granular washing compositions is usually 0.4 g / cn3 or more, but it is preferably 0.5 ~ 1.2g / cn3. The surfactant powder obtained by the present invention, because of the action of water-soluble polycarboxylic acid and / or its salt, allows the thio fatty acid alkyl ester soap to have a high concentration, thereby improving the solubility in an alkaline aqueous solution. Since a small amount of water-soluble polycarboxylic acid and / or its salt can obtain equivalent effects, the increase in cost is limited. In addition, due to the action of soap, even if the concentration of -thio fatty acid alkyl esters—16—this paper size is applicable, SH home standard (CNS) A4 (210X297 mm) (please read the precautions on the back first) (Fill in this page again.) Order printed by the Central Bureau of Standards, Ministry of Economic Affairs, Consumer Cooperatives. 416982 A7 B7 5. The description of the invention (π) is very high, and it is difficult to agglomerate and solidify. Due to the preparation method of the surfactant powder, the spray drying method is not used for the production, and there is no loss of energy from the spray drying method, and there is no case where the particles are floating in the air and the working environment is deteriorated. In addition, the concentration of the concentrate at a temperature of 70 ° C or less makes it easy to powderize it, so that the surfactant powder can be efficiently produced at a low cost. In particular, the preparation method of this surfactant powder, the concentration of the moisture content of the concentrate at the time of terminating the concentration step, and the optimum temperature of the concentrate before the powderization, even though the concentration of α-thiolipid. It is very high and can be easily powdered, which is an extremely efficient manufacturing method. In addition, this surfactant powder is granulated together with other ingredients, or mixed with powders of other lotion ingredients (preferably high bulk density particles), so that it has good low-temperature solubility in alkaline aqueous solutions and is not easy to aggregate. . Cured granular lotion composition. The implementation of the present invention is as follows. The present invention also includes a combination of the following constitutions. (i) The surfactant powder obtained by the present invention should preferably contain more than 40% by weight of thio fatty acid alkyl esters, preferably 40 ~ 84 weight children 96, 10 Printed by the Shellfish Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs (Please read the precautions on the back before filling this page) Soap with a weight of more than 0%, the best is 0 ~ 54% by weight. The total house custom of α-thio fatty acid alkyl ester and soap contains 0.01 ~ 5% by weight. Water-soluble carboxylic acid and / or its salt. From the above mixing amount, the ratio of "-thio fatty acid alkyl ester to soap" is 43: 57 ~ 89: 11 based on weight-to-weight ratio, and preferably 50: 50 ~ 89: 11. This paper size is applicable to China Standard (CNS) A4 specification (210X297 mm) Printed by the Central Standards Bureau of the Ministry of Finance and Economics, printed by another industrial consumer cooperative 416982 A7 B7 V. Description of the invention (16) UU regarding water-soluble carboxylic acid and / or its salt, acrylic acid, methyl ester, A homopolymer formed from one selected from acrylic acid, maleic acid, and itaconic acid, or a copolymer formed from two or more selected from them. Copolymers of one or more selected from acrylic acid, methacrylic acid, maleic acid, and itaconic acid, and maleic anhydride may also be used. As the anti-ion of water-soluble polycarboxylic acid, it is suitable to use one or more kinds of β selected from aging metals, bentonite metals, and ammonium. Among them, the most suitable ones are sodium, potassium and other testing metals. The weight average molecular weight of the water-soluble polycarboxylic acid is lflOdO or less, and preferably 300 to 10 G00. The compounding amount of the water-soluble polycarboxylic acid and / or its salt in the surfactant powder is pseudo-p-α-thio fatty acid alkyl ester and the total amount of the soap (surfactant pure fraction> 0.01 to 5% by weight, and Preferably, it is fl.l ~ 3% by weight. (Iii) In the method for preparing the surfactant powder of the present invention, a water content of 20 ~ 30% by weight containing a thio fatty acid alkyl ester soap and a water-soluble polycarboxylic acid and / Or its strong mixed slurry raw material is concentrated to produce a concentrate with a moisture content of 15% by weight or less. (L. in the range of 1 to 15% by weight, and preferably a concentration of 10% by weight or less.) Second, this, The temperature of the concentrate is below 70 ° 〇, usually after 0 ~ 7B «C, this concentrate is directly crushed, or formed into a nine shape by a pelletizer, and then crushed, or the flakes are crushed to make the powder into a powder. Method for preparing surfactant powder. The temperature of the above-mentioned concentrate powder before being powdered, if cooled by a cylindrical cooler, is preferably below 20 ° C, usually 0 ~ 20 ° C. Uv &gt; Granularity of the obtained surfactant powder -18- This paper size applies to Chinese National Standard (CNS) A4 (210X297mm)! |: I ί- ii ^ ^^ 1 ^ 1 (Please read the precautions on the back before filling in this page) Order A7 B7 416982 V. Description of the invention (l7) The lotion composition This surfactant powder is granulated or mixed with other washing ingredients to form a granular lotion composition. Γ 1 I— ^ — ^ 1 ϋϋ —mu (Please read the precautions on the back before filling in this Buy) At this time, the concentration of "-thio fatty acid alkyl ester in the granular lotion composition is preferably 1 to 50% by weight. The granulation method includes, kneading (densification &gt; post-crushing method (pressing) Dense granulation method &gt; Method for mixing granulation (photo-mixing granulation method, when mixing powder to make granular detergent composition, it is appropriate to compact the spray-dried particles of other lotion ingredients and pulverize to form After high bulk density (powder), this powder is mixed with the interfacial active rhenium powder of the present invention, or manufactured by methods other than spray-drying by stirring granulation, rotary granulation, fluid layer granulation, etc. High bulk density particles (powder) of other lotion ingredients and the surfactant powder of the present invention Method for powder mixing (V) The moisture content of the surfactant powder obtained by the present invention and the granular lotion composition containing the surfactant powder is preferably 1 to 15% by weight, and most preferably 3 to 10% by weight, with an average particle size of 200 to 1500 Αβ, and a bulk density of generally 0.4 g / cB3 or more, and preferably 0.5 to 1.2 g / cb 3 0. [Example] Ministry of Economic Affairs The Central Government Bureau of Standards, Shellfish Consumer Cooperative, prints the following, and the present invention will be described in detail in the following examples. If there is no special description or indication, the indicated% is a pseudo-weight%. * First, the low temperature in the alkaline aqueous solution used in the examples is described. (5-C) The evaluation method of the solubility test (dissolved residue measurement method) is explained. (Residual residue method) Put 1 liter of 5 &quot; C water in a 1 liter beaker and put in one of 3 grams-1 9- This paper size applies Chinese National Standard (CNS) A4 specification (210 × 297 mm) A7 B7 416982 5 Explanation of the invention (β) (Please read the precautions on the back before filling in this page) Sodium carbonate with a fixed particle size and 5 grams of sample, stir at 25Qrpm for 8 minutes. Filter through the expected weight of Nylon knitted fabric (hereinafter referred to as Nylon). This Nylon is dried at 105 ° C for 6 hours and then measured. From the weight of the filter-dried Nylon cloth, subtract the weight shown in the initial Nylen cloth weight as the dissolved residue weight of the sample, and calculate the tb example of the dissolved residue to the initial sample weight (% by weight &gt;. [I] Production of surfactant powder (Examples 1 to 6) According to the composition shown in Table 1, mixed α-thio fatty acid methyl ester pins, soap (sodium salt with an average number of master atoms of 12 to 18), sodium polyacrylate (Water-soluble polycarboxylate) is tempered into a slurry. This slurry was produced by using a vertical mixer (manufactured by Dowton Co., Ltd.) to evaporate moisture at a jacket temperature of 90 ° C. Then, except for Example 4, the above-mentioned concentrate was used as a cylindrical sheet I »--------- .....- Machine (product name) (made by Nanmu Machinery Manufacturing Co., Ltd.) is cooled to the temperature shown in Table 1 .-------------- --- At the same time as the temperature after the step, thinning. Example 4 is coming ^ ---. The above-mentioned concentrate is printed by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs, placed at room temperature, and cooled to the temperature after the cooling step shown in Table 1. The concentration and the amount shown in Table 1 After mixing the zeolite (additives described in Table 1 in the form of pellets in Table 1), the obtained lumps were made using a double-type pellet press (product name) (manufactured by Fuji Co., Ltd., type: EXDFJS-6 0). Nine shapes with a diameter of about 10 til η and a length of about 15 mm. Next, the thin slabs or pressed noodles of Examples 1 to 6 were purified with 100 parts by weight of the surfactant, and this pure was used together with the zeolite (pulverizing agent) in the amount shown in Table 1. 2ΒΒ1 sieve of Fizi mill (product name) (manufactured by Hosokawa Mikron Co., Ltd., type: ΚΑ-3), by -20 &quot; This paper size applies Chinese National Standard (CNS) Α4 grid (210X297 mm) 416982 A7 B7 __ V. Description of the invention (19) 15 &quot; C The cold wind is pulverized to powderize it to obtain a surfactant powder. (Please read the precautions on the back before filling in this page} The properties, composition, and measurement results of the obtained surfactant powder powder are combined as shown in Table 1. (Comparative Examples 1 to 3) According to the composition shown in Table 2 , Sodium α-thio fatty acid methyl ester, soap (sodium salt with an average carbon number of 12 to 18), and polyacrylic acid sodium is added to prepare a slurry as required. This slurry was prepared in a manner similar to the operation of the above-mentioned embodiments 1 to 6 to form a thick knit. Then, the above-mentioned concentrates other than Comparative Example 2 were thinned using a drum-type thin heading machine (product name &gt; (Nanmu Machinery Manufacturing Co., Ltd.)) to the temperature after the cooling step shown in Table 2 while being thinned. As for Comparative Example 2, the method of Example 4 was followed by cooling to make pellets ρ with a diameter of about »» and a length of about 15 m. Next, the nine types of thin sheets of Comparative Examples 1 to 3 described above were implemented in accordance with the above. Examples 1 to 6 were powdered in the same manner to obtain a surfactant powder. The properties, composition, and measurement results of the obtained surfactant powder were combined as shown in Table 2. "Comparative Example 2 due to the high cooling temperature Therefore, it cannot be formed into a pellet. As for Comparative Example 3, it cannot be crushed because of the high moisture content of the Australian condensate. The Central Standards Bureau of the Ministry of Economic Affairs, Shellfish Consumer Cooperative, printed the results from the above Examples 1 to 6 and Comparative Examples 1 to 3, such as Compared with the case where a water-soluble polycarboxylic acid and / or a salt thereof is used, the surfactant powder of Comparative Example 1 without using a water-soluble polycarboxylic acid and / or a salt thereof has more dissolved residues, and as a result, the solubility is higher. Becomes inferior β and the cooling temperature Higher Comparative Example 2, Higher Moisture Content of Concentrated -2 1-Paper Scale Standard Chinese Standard (CNS) A4 Specification (210X297 mm) A7 B7 416982 V. Description of Invention (20) Comparative Example 3. Neither can be powdered. Therefore, it is known that in the manufacture of surfactant powders, the weight of the concentrate and the temperature of the concentrate before powdering are set to the most suitable conditions.-Regarding the implementation of the present invention, The surfactant powders of Examples 1 to 6, any of them has better low temperature solubility than Comparative Example 1 and is easy to be powdered. It contains a high concentration of thio fatty acid alkyl ester and soap. Surfactant powder with good low temperature solubility in aqueous solution. (Please read the precautions on the back before filling this page)-= β Printed by the Central Standards Bureau of the Ministry of Economic Affairs, Shellfish Consumer Cooperatives. CNS) A4 specification (210X297 mm) 416982 A7 B7 V. Description of the invention () [Table 1] Table 1: Manufacturing parts, properties and composition of surfactant powder (Example) Eliminate Cooperative printed example number 1 2 3 4 5 6 Slurry α-SF concentration (%) β1 33.7 44.7 58.7 44.7 45.3 42.2 Soap concentration 33.7 22.0 8.0 22.0 22.3 20.8 (cr-SF / soap ratio) 50/50 67 / 33 88/12 67/33 67/33 67/33 Average molecular weight of sodium polyacrylic acid 10000 3000 300 3000 3000 3000 Anti-active agent concentration (%> * 2 0.1 1 1 1 0.01 5 Moisture (%) 29.1 28.2 26.8 28 * 2 27 * 8 29.7 Moisture content (%) of condensate 10.0 5.0 3.0 5.0 5.0 5.0 Temperature after concentration (eC) 90 Temperature after cooling step &lt; ° C &gt; 30 15 15 50 15 15 Additives for pelletizing * 3 Zeolite Antioxidant degree (%) · 2---10 —-Broken rib agent zeolite resistance_Ao degree (%) * 2 5 Bulk density (g / cc) of surfactant powder 0.4 ~ fl.5 Average particle size (/ * »〇400 ~ 500 Dissolved residue (%) 9 7 9 5 9 9 Surfactant: powder into a -SFjggF (% ^ · 1 40.6 55.9 73.6 50.7 56.5 54.1 Soap concentration (%) 40.6 27.6 10.0 25.0 27.8 26.6 Percent (¾) 10.0 5.3 3.4 5.7 5.3 5.3 * 1) α, SF: Fat The number of acid residues is 硫 ~ 16 α-thiolipid anti-acid alkyl esters &quot; 2) Anti-Availability: tb case of total thio fatty acid alkyl esters and fats * 3) Nine Additives during molding: After the concentrate was cooled by a barrel type thinner (manufactured by Nanki Machinery Co., Ltd.) other than Example 4, the additive was directly thinned without using additives. -23- This paper is compliant with Chinese garden standards ((: Yang) / 14 specifications (21〇 \ 297 mm) (Please read the precautions on the back before filling this page) Order 1, 416982 A7 B7% / {Measure the concentration of narcotic acid, isopropylidene, isopropylidene / flat anti-polymerization, Wu, Lu | Yue 2 Huming (22) Table 2: Manufacturing conditions, properties and composition of surfactant powder (comparative example) Implementation Example No. 1 2 3 Effervescent α-SF Degree (96) * 1 4 5.3 4 4. 7 4 4 .7 Soap concentration 22.3 2 2. 0 2 2 .0 (or-SF / soap ratio) 6 7 / 3 3 6 7/3 3 6 7/3 3 Moisture (%) 27.8 28.2 28.2 Concentrate moisture (%) 10.0 5.0 16.0 Temperature after concentration (° C) 90 Temperature after cooling step (° C) 1 5 8 0 1 5 Additives s3 during compressive molding. Zeolite anti-active agent concentration (%) * 2-20 Broken rib agent zeolite anti-active agent concentration. 5 Impossible to form (please read the precautions on the back before filling this page). Residual dense granules of slag-like particles all solve the face and the melting boundary

狀 性 之C) 體/C 粉碎不可 0 經濟部中夬標準局貝工消費合作社印裝 度 I農 性Fii濃 活-s皂分 面α肥水 ητ R7 粉 度 成 組*1 之} 體% % % 一 活tb丸 a 抗之壓 \/ \/ \/ 12 3 為 數 碩 之 基鈉 殘酯 .酸烷 肪酸 脂肪 α 對 度 濃 劑 sIg加:㈣添 Λ用 Λ使 /,不 形S化 性例成1片 旨 ΗΠ 代 硫 a 之 最 總 皂 肥 與 酯 烷 酸 防 脂 代 硫 機直 片俗 .薄因 式, 筒後 由卻 外冷 以物 4縮 例濃C 施將物 本紙張尺度適用中國國家標準(CNS ) A4現格(2丨0 X 297公釐) 經濟部中央標準局貝工消費合作社印«. 416982 五、發明説明(23) 〔2〕粒狀洗淨劑組成物之製造 (實施例7:壓密造粒法) 將依照表3所示組成調製水性淤漿,由表3所示條件 經噴蓀乾燥法製成乾燥粒子(表中,係記載乾燥粒子(A))。 將此乾燥粒子與上述實施例2之界面活性劑粉體,以 及非離子界面活性劑以表3所示比較在KRC捏和機(製品 名)(栗本鐵工所公司産製,型式:S-2)中予以壓密混合。 由此所獲得之塊狀物,使用雙重式壓丸器(製品名)( 不二粉公司製造,型式:EXDFJS-60)作成直徑約l〇mn, 長度約15mm之壓九。此壓九與對lflO重量份粒狀洗淨劑 組成物含有6重童扮純分量之硝酸銷一起,使用安裝有 孔徑2ββ篩網之斐滋磨機(製品名 &gt;(細川米克隆公司製造 ,型式:KDA-3),通過以15°C之冷風予以粉碎製作成粉 體化產品。然後,將此粉體化産品,與對100重量份粒 狀洗淨劑組成物含有3重量份沸石及1重量份酵素(蛋 白酶}純份在旋轉筒内混合,再噴霧以0.5重量份香料與 1重量份靥於起塵防止粘合爾之.非離子界面活性劑(Cu 酵聚氧羥乙酷(ΕΟρ =2〇)(純分84%)),得粒狀洗淨劑 組成物。 此粒狀洗淨劑組成物之性狀及溶解殘渣測定結果併合 如表3所示。 (實施例8 :攪拌造粒法) 依照表3所示组成讕製水性淤漿,由表3所示條件經 由噴蓀乾燥法予以乾燥而獲得乾燥粒子(表中,記載為 -25- 本紙張尺度適用中國國家標準(CNS ) Α4規格(210X297公釐) (請先閲讀背面之注意事項再填寫本頁)Status C) Body / C Crushing is not possible 0 Printing degree of the Ministry of Economic Affairs of the China Standards Bureau Shellfish Consumer Cooperative I Agricultural Fii Concentration-s soap facet α fertilizer water ητ R7 Powder group * 1 of the body}%% % Yihuo tb pill a anti-pressure \ / \ / \ / 12 3 is a number of sodium based sodium esters. Acid alkanoic acid fat α Contrast concentration agent sIg plus: add Λ with Λ to make /, not shape S The performance example is 1 tablet, which is the most total soap fertilizer of thiosulfate a and ester alkanoic acid anti-lipid sulfide machine. The film is thin, and the tube is cooled by the outside, and the material is concentrated. The scale is applicable to Chinese National Standard (CNS) A4 (2 丨 0 X 297 mm). Printed by the Sheller Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs. 416982 V. Description of the Invention (23) [2] Granular detergent composition Production (Example 7: Compaction granulation method) An aqueous slurry was prepared in accordance with the composition shown in Table 3, and dried particles were prepared by a spray drying method under the conditions shown in Table 3 (In the table, dry particles (A )). The dried particles were compared with the surfactant powder and the non-ionic surfactant of Example 2 in a KRC kneader (product name) as shown in Table 3 (made by Kurimoto Iron Works Co., Ltd., type: S- 2) Compression and mixing. The obtained pellets were made into a pellet press with a diameter of about 10 mn and a length of about 15 mm using a double-type pellet press (product name) (manufactured by Fuji Powder Co., Ltd .: EXDFJS-60). This pressure was used together with a nitric acid pin containing 6 weights of pure detergent for lflO parts by weight of a granular detergent composition, using a Fischer mill (product name &gt; (manufactured by Hosokawa Mikron Co., Ltd.) equipped with a 2ββ screen. , Type: KDA-3), pulverized with cold air at 15 ° C to produce a powdered product. Then, the powdered product contains 3 parts by weight of zeolite with 100 parts by weight of the granular detergent composition. And 1 part by weight of enzyme (protease) pure parts are mixed in a rotating cylinder, and then 0.5 parts by weight of perfume and 1 part by weight are dusted to prevent dust adhesion. Non-ionic surfactant (Cu fermented polyoxyhydroxyethyl) (E0ρ = 20) (purity 84%)) to obtain a granular detergent composition. The measurement results of the properties and dissolved residues of this granular detergent composition are shown in Table 3. (Example 8: Agitation granulation method) An aqueous slurry was prepared in accordance with the composition shown in Table 3, and dried particles were obtained by spray drying method under the conditions shown in Table 3 (in the table, it is described as -25- This paper size applies to Chinese national standards. (CNS) Α4 specification (210X297 mm) (Please read the precautions on the back first Write this page)

經濟部中央操準局貝工消費合作社印製 416982 A7 B7 五、發明説明(24) 乾燥粒子(A))。 將此乾燥粒子舆實施例2之界面活性劑粉涯,以及非 離子界面活性劑以表3所示tb例在雷葛混合機(製品名) (松波公司産製,型式:H~20&gt;中予以横拌造粒,彷實施 例10相同之後處理得粒狀洗淨劑組成物。此粒狀洗淨劑 組成物之性狀及殘渣測定結果併合如表3所示β (實施例9 :粉體混合) 依照表3所示組成調製水性淤漿,以表3所示條件由 噴藕乾燥法經乾燥而獲得乾燥粒子(在表中卽記載以乾 燥粒子(Α))。 此乾燥粒子與非離子界面活性劑即以表3所示比例在 KRC捏和機(製品名)(栗本鐵工所公司製品,型式:S-2) 中壓密混合。所獲得之塊狀物使用雙重式壓九器(製品名) (不二粉公司製造,型式:SXDFJS-60)做成直徑約lOntt, 長度約15mm之鼷九。此壓九對100重fi份粒狀洗劑組成物 與6重量份之純分量硪酸鈉一起,使用裝設有孔徑2nB 篩網之斐滋磨機(製品名)(細川米克隆公司製造,型式: DKA-3),通過以15=〇之冷風經由粉碎予以粉體化獲得 高容積密度粒體(表中係記載高容積密度粒體(B))。 將此高容稹密度粒體舆實施例2所得之界面活性劑粉 體,由表3所示比例,在旋轉筒醴中混合對100重量份 粒狀洗淨劑組成物含有3重量份沸右及1重量份酵素 (蛋白酶)純分粉體,噴猱以0.5重量份香料及1重董份 起塵防止拈合劑之非離子界面活性劑(Cu醇聚氧羥乙醱 -2 6- 本紙張尺度適财咖家樣_ ( CNS )从胁.(21Q χ 297公楚) --------J-11Θ------、訂------線(i - . (讀先閱讀背面之注意事項再填寫本買) 五、 416982 A7 B7 發明説明( 25 數 耳 莫 成 加 均 平。 烷物 乙成 氣組 環劑 ;淨 Θ 2 洗 I 一 狀 Ρ ο 粒 Ε {得 % 4 8 分 純 合 併 0&lt; 結 定 測 渣 殘 解 溶 及 狀 性 之 物 成 組 劑 淨 〇 洗示 狀所 粒3 此表 如 \y 4 例 較 fcb yl\ 表 照 依 漿 淤 性 水 製 成 組 示 所 操 同 相 9 例 施 實 仿 例 較 比 與 子 粒 燥 乾 用 使 體 粉 劑 性 活 面 界 之 得 所 成 組 劑 0 淨示 洗所 狀 3 粒表 此如 β 合 物併 成果 組結 剤定 淨測 洗渣 狀殘 粒解 得溶 而及 體以 粉狀 合性 混之 由物 關溶 有水 用性 使皤 因在 ,知 果得 結然 之顯 4 , 例體 較粉 比_ 及性 V 7 面 例界 施之 實例 之施 3 實 表明 從發 本 獲(£ 可納 中酸 液磺 其存 尤渣 ❶殘 物解 成溶 組有 劑無 淨幾 洗8 狀例 粒施 之實 好之 良多 性置 解含 溶丨 溫 低 得 份 組 性 (請先閲讀背面之注意事項再填寫本頁) 訂 在例 9 施 實 之 件 條 同 相 之 外 以 體 粉 劑 性 活 面 界 3J f 月 4 使例 較較 fcbfcb 又與 性 解 溶 其 善 改 顯 明 有 知 已 9 例 施 實 在 -β. 經濟部中央標準局員工消費合作社印製 本紙張尺度適用中國國家標準(CNS ) A4规格(210X297公釐) A7 B7 416982 五、發明説明(26 ) [表3〕 表3:粒狀洗劑組成物之製造(實施例,比較例) 實施例及 實施例 比較例 比較例编號 789 4 乾燥粒天(A) 組成&amp;(%&gt; LAS-K*2 沸石 磺酸鉀 亞硫酸鈉 蒂諾帕爾CBS . (Tinopal CBS)*J 15 硪酸鈉 0 6 0 2 5 1ί · 7Printed by the Shellfish Consumer Cooperative of the Central Guiding Bureau of the Ministry of Economic Affairs 416982 A7 B7 V. Description of the invention (24) Dry particles (A)). The dried particles of Fanya, the surfactant in Example 2, and the non-ionic surfactant were shown in Table 3 as tb in a Regal mixer (product name) (manufactured by Songbo Co., Ltd., type: H ~ 20). It was granulated by horizontal mixing, and then treated in the same manner as in Example 10 to obtain a granular detergent composition. The measurement results of the properties and residues of this granular detergent composition are shown in Table 3 β (Example 9: Powder Mixing) An aqueous slurry was prepared in accordance with the composition shown in Table 3, and dried particles were obtained by spray drying under the conditions shown in Table 3 (the dry particles (A) are described in Table 卽). The surfactant was compacted and mixed in a KRC kneader (product name) (product of Kurimoto Iron Works Co., Ltd., type: S-2) in the proportion shown in Table 3. The obtained block was a double-type compactor. (Product name) (Made by Fuji Powder Co., Ltd., Type: SXDFJS-60) Made of 鼷 9 with a diameter of about ltt and a length of about 15mm. This pressure is about 100 parts by weight of fi parts of granular lotion composition and 6 parts by weight of pure Using a portion of sodium gallate, use a Fischer mill (product name) equipped with a 2nB mesh screen Manufactured by Hosokawa Mikron Co., Ltd., type: DKA-3). High bulk density granules are obtained by pulverizing with cold wind of 15 = 0 (high bulk density granules (B) are listed in the table). The surfactant powder obtained in Example 2 was prepared in the ratio shown in Table 3. The content of the surfactant powder was mixed in a rotating cylinder with 100 parts by weight of the granular detergent composition. Parts of enzyme (protease) pure powder, sprayed with 0.5 parts by weight of perfume and 1 part by weight of non-ionic surfactant (Cu alcohol polyoxyethylen-2-2) Café-like _ (CNS) Congxiu. (21Q χ 297 Gongchu) -------- J-11Θ ------, order ------ line (i-. (Read first Read the notes on the reverse side and fill in this purchase) V. 416982 A7 B7 Invention description (25 numerous molybdenum plus average level. Alkane B gas forming ring agent; net Θ 2 wash I shape P ο grain Ε {得% 4 8 points pure and combined 0 &lt; final measurement of residual slag dissolution and properties of the grouping agent 〇 wash and show the granules 3 This table is like \ y 4 cases compared with fcb yl 9 groups are shown in the same phase, and the examples are compared with those used to dry the granules. The powder is used to make the body powder active. The composition is 0. The cleansing is like 3 tablets. The result is that the slag-like residues are dissolved and dissolved in powder form, and the powder is mixed with water. The water is used to make the cause, and the results are obvious. 4 The ratio of body to powder is _ and The properties of the V 7 example of the application of Example 3 show that it can be obtained from the hair (£ can be dissolved in the acid solution and its residues, and the residues can be dissolved into a solution. Extensive solution of solubilities 丨 low temperature composition (please read the precautions on the back before filling out this page). Set it in Example 9 and apply it in the same phase as body powder. 3J f Compared with fcbfcb, it has been dissolved with sex and its good change has shown that 9 cases have been implemented in -β. Printed by the Consumers Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs This paper is printed in accordance with Chinese National Standards (CNS) A4 specifications (210X297 mm) A7 B7 416982 five Description of the invention (26) [Table 3] Table 3: Production of granular lotion compositions (Examples, Comparative Examples) Examples and Comparative Examples of Examples Comparative Example No. 789 4 Dry Granular Day (A) Composition & ( % &gt; LAS-K * 2 Zeolite Potassium Sodium Sulfite Tinopal CBS. (Tinopal CBS) * J 15 Sodium osmate 0 6 0 2 5 1ί · 7

T 1X 乾燥條件 淤漿水分(%) 40 熱風溫度(°C) 300 (請先閱讀背面之注意事項再填寫本頁) 性狀 容稹密度(g/ce) 0.35 水分 (%) 6 成--μλ- 之)-) Β 外%cc ^IA( / 子m劑(g 粒(A性度 度子活密 密粒子積 積燥離狀容 容乾非性 高 3 3 訂 粒狀洗劑組成物 混合(造粒)方法壓密混合攪拌造粒粉體混合粉體混合 混配量(%Γ5 乾燥粒子(A) 59.0 高容積密度粒子(fi)-界面活性劑粉體;25.3 非離子活性劑β4 3 66.5 -- 69.8 25.0 24.7 3 - 69.8 24.7 性狀 容積密度(g/cc) 0.80 平均粒徑(ΛίΒ) 550 溶解殘渣(%) 〇 0 0 10 &quot;1)組成:以對粒狀洗劑組成物全量之重量%表示。 • 2 ) US_K: Cu—b烷苯磺酸鉀 3 )蒂諾帕爾CBS:汽巴嘉基公司製造之螢光增白劑 β 4 )非離子活性劑:C13醇聚氣羥乙酯(E0p=20)( 純分84%),對粒狀洗劑組成物總量以重量% 袅示。 &quot;5)混配量:對粒狀洗剤組成物總量以重量%表示。 * 6)界面活性劑粉體:實施例7〜g為實施例2之界 面活性劑粉體,比較例4為比較例1之界面活 性劑粉體〇 -28- 本紙張尺度適用中國國家標準(CNS ) A4規格(210X29&quot;?公釐&gt; 線 經濟部中央標準局貝工消費合作社印製 416982 A7 B7 五、發明説明(27 ) 〔産業上之可利用性〕 關於本發明可得以下之效果。 (請先閱讀背面之注意事項再填寫本頁) 亦即,本發明之界面活性劑粉體,傜藉水溶性聚羧酸 及/或其鹽之作用,因各含有高濃度之α-硫代脂肪酸院 酯舆肥皂,故可提高鹼水溶液中之低溫溶解性。更且由 肥皂之作用而加速進行硫代脂肪酸烷酯之結晶化, 形成不易凝集,固化之界面活性劑粉體。 含有少置之水溶性聚羧酸及/或其鹽,亦能獲得充分 之效果,因此所引起之成本增加非常有限。 更且,本發明由於不使用噴蓀乾燥法而可以製造界面 活性劑粉末,故無有因噴霧乾燥而有能量損失之情形, 且無有粒子在空氣中漂浮致環境有惡化之現象β 又,關於界面活性劑粉體之製造,濃縮物之溫度設定 在70°C以下後即能粉體化,因容易粉體化,故有可能以 高效率低成本製造界面活性劑粉體^ 更且,由於使用本發明方法所獲得之界面活性劑粉體 ,因此在鹾性水溶液中有良好之.低溫溶解性,可生成不 易凝集•固化之粒狀洗劑組成物。 經濟部中央標準局員工消費合作社印製 • 2 9 _ 本紙張尺度適用中國國家標準(CNS ) A4规格(210X 297公釐)T 1X Drying condition Slurry moisture (%) 40 Hot air temperature (° C) 300 (Please read the precautions on the back before filling in this page) Properties Capacity Density (g / ce) 0.35 Moisture (%) 6%-μλ -Of)-) Β outside% cc ^ IA (/ 子 m agent (g particles (A degree of degree, liveness, dense particles, accumulation, dryness, dryness, capacity, dryness, non-sexuality, high 3, 3) (Granulation) method compaction mixing and stirring granulation powder mixing powder mixing compounding amount (% Γ5 dry particles (A) 59.0 high bulk density particles (fi) -surfactant powder; 25.3 nonionic active agent β4 3 66.5-69.8 25.0 24.7 3-69.8 24.7 Characteristic Bulk Density (g / cc) 0.80 Average Particle Size (ΛίΒ) 550 Dissolved Residue (%) 〇 0 0 10 &quot; 1) Composition: To the total amount of granular detergent composition It is expressed by weight%. • 2) US_K: Cu—b potassium potassium alkane sulfonate 3) Tinopar CBS: Fluorescent whitening agent β 4 manufactured by Ciba Jiaji Company) Non-ionic active agent: C13 alcohol polymerization gas Hydroxyethyl ester (E0p = 20) (84% pure) is shown as weight percent of the total amount of the granular lotion composition. &quot; 5) Compounding amount: The total amount of granular washing composition is expressed by weight%. * 6) Surfactant powder: Examples 7 to g are the surfactant powders of Example 2, and Comparative Example 4 is the surfactant powder of Comparative Example 0-28- This paper size applies Chinese national standards ( CNS) A4 specification (210X29 &quot;? Mm &gt; Printed by the Central Bureau of Standards of the Ministry of Economics and Printing Co., Ltd. Shellfish Consumer Cooperative 416982 A7 B7 V. Description of the invention (27) [Industrial availability] The following effects can be obtained with the present invention (Please read the notes on the back before filling this page) That is, the surfactant powder of the present invention, by virtue of the action of water-soluble polycarboxylic acid and / or its salt, each contains a high concentration of α-sulfur Substituted fatty acid esters and soaps can improve the low-temperature solubility in alkaline aqueous solutions. It also accelerates the crystallization of thio fatty acid alkyl esters by the action of soaps, forming surfactant powders that are not easy to aggregate and solidify. The water-soluble polycarboxylic acid and / or its salt can also obtain sufficient effects, so the cost increase caused is very limited. Furthermore, because the surfactant powder can be produced in the present invention without using the spray drying method, None In the case of spray drying and energy loss, and no particles floating in the air and causing deterioration of the environment β In addition, regarding the manufacture of surfactant powders, the concentration of the concentrate can be set below 70 ° C, and the powder can be powdered. Of, because it is easy to powder, it is possible to produce surfactant powder with high efficiency and low cost ^ Moreover, because the surfactant powder obtained using the method of the present invention, it is good in alkaline aqueous solution. Low temperature solubility, it can produce granular lotion composition that is not easy to agglomerate and solidify. Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs • 2 9 _ This paper size applies to China National Standard (CNS) A4 (210X 297 mm)

Claims (1)

Α8 Β8 C8 DSΑ8 Β8 C8 DS 經濟部智慧財產局員工消費合作社印製 第8710023 3號「界面活性劑粉體之製法及界面活性劑粉體 與粒狀淸潔.劑組成物·」専利案 (88年1 1月19日修正) 六、申請專利範圍: 1. 一種淸潔界面活性劑粉體之製造方法,其特徵爲調製 含有α -硫代脂肪酸烷酯,肥皂,水溶性聚羧酸及/或 鹽之混合淤漿,將此混合淤漿水分濃縮至1 5重量%以 下,此濃縮物之溫度在7 〇 °C以下後即予以粉體化,用 以製造含有.40~84重量%.之α -硫代脂肪酸烷酯,1 0~54 重量%之肥皂,相對於α -硫代脂肪酸烷酯與肥皂之總 量,係含有0.01〜5重量%之水溶性羧酸及/或其鹽 而上述界面活性劑粉體中之α -硫代脂肪酸烷酯與肥皂 • · . 之比率,依重量比計爲43: 57〜89: 11’且係直接粉 碎濃縮物予以粉體化’或將濃縮物壓九後粉碎使之粉 體化,或將濃縮物片狀化後粉碎予以粉體化。 2. 如申請專利範圔第1項之界面活性劑粉體之製法’其 中上述界面活性劑粉體中之水溶性聚羧酸及/或其鹽 之含量,係對α -硫代脂肪酸烷酯與肥皂總量之0 ·1〜3 重量%者。 3. 如申請專利範圍第1項之界面活性劑粉體之製法’其 中水溶性聚羧酸係選自丙烯酸,甲基丙烯酸’馬來酸’ 衣康酸之1種所生成之均聚物’或選自其中之2種 .以上所生.成之共聚物,或爲選自丙嫌酸,.甲基两嫌酸’ 馬來酸,衣康酸之1種以上’與馬來酸酐之共聚物1 (請先閲讀背面之注$項再填寫本頁) 本紙張尺度逋用中國國家標準(CNS &gt; Α4规格(210X297公兼) AS _416982_1_:_ 六、申請專利範圍 上述水溶性聚羧酸鹽之對應基陽離子係選自鹼金 屬,鹼土類金靨,銨之1種以上者。 {請先閱绩背面之注意事項再填寫本頁) 4. 如申請專利範圍第1項之界面活性劑粉體之製法,其 中水溶性聚羧酸之重量平均分子量爲10000以上者。 5. 如申請專利範圍第1項之界面活性劑粉體之製法,其 中混合淤漿之水分含量爲2〇〜30重量%者。 6. —種淸潔界面活性劑,其特徵爲: 調製含有α -硫代脂肪酸烷酯,肥皂,水溶性聚羧酸 及/或其鹽之混合淤漿, 濃縮此混合淤«之水分在1 5重量%以下, 此濃縮物之溫度在7 〇 °C以下後經由粉體化而予以製 造成含有40〜84重量%之^硫代脂肪酸烷酯,10〜5 4 重量%之肥皂,相對於α -硫代脂肪酸烷酯與肥皂之總 量,係含有〇.〇 1〜5重量%之水溶性聚羧酸及/或其 鹽, 而其中界面活性劑中之α -硫代脂肪酸烷酯與肥皂之 比率,以重量比計乃爲43 : 5 7〜89 : 1 1。 經濟部智慧財產局員工消費合作社印製 7. 如申請專利範圍第6項之界面活性劑,其中對α -硫代 脂肪酸烷酯與肥皂之總量係含有〇. 1〜3重量%之水 溶性聚羧酸及/或其鹽者。 a如申請專利範圍第6項之界面活性劑,其中水溶性聚 羧酸係選自丙烯酸,甲基丙烯酸,馬來酸,衣康酸之 1種所形成之均聚物,或選自其中之2.種以上所形 -2- 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) Αδ Β8 _416982_g_·_ 六、申請專利範圍 成之共聚物,或爲選自丙烯酸,甲基丙烯酸’馬來酸, 衣康酸之1種以上,與馬來酸酐之共聚物, 而水溶性聚羧酸鹽之對應基陽離子,係選自鹼金 屬,鹼土類金屬,銨之1種以上者。 9. 如申請專利範圍第6項之界面活性劑 &gt; 其中水溶性聚 羧酸之重量平均分子量爲10000者。 10. 如申請專利範圍第6項之界面活性劑'其中混合淤漿 之水分含量20〜30重量%者。 11. 一種粒狀冼劑組成物,其特徵爲使如申請專利範圍第 6項之界面活性劑與其他之洗劑成分共同經造粒或粉體 混合。 12. 如申請專利範圍第1 1項之粒狀洗劑組成物,其中水 分含量爲1〜15重量%,平均粒徑爲200〜15〇〇/zm’ 容積密度爲0.4 g/cm3以上者。 (請先聞讀背面之注意事項再填寫本頁) 經濟部智慧財產局員工消費合作社印製 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐)Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs No. 8710023 3 "Methods of Making Surfactant Powders and Surfactant Powders and Granular Cleansing Agent Compositions" Case (Amended on January 19, 88 ) 6. Scope of patent application: 1. A method for manufacturing cleansing surfactant powder, which is characterized by preparing a mixed slurry containing α-thio fatty acid alkyl ester, soap, water-soluble polycarboxylic acid and / or salt, The water content of this mixed slurry is concentrated to 15% by weight or less, and the temperature of the concentrate is reduced to 70 ° C or less, and then powdered to produce α-thio fatty acid alkane containing 40 to 84% by weight. Ester, 10 to 54% by weight of soap, 0.01 to 5% by weight of water-soluble carboxylic acid and / or its salt relative to the total amount of α-thio fatty acid alkyl ester and soap, and the above surfactant powder The ratio of α-thio fatty acid alkyl ester to soap • ·. Is 43: 57 ~ 89: 11 'by weight ratio, and the concentrate is directly pulverized and powdered; Powder, or pulverize the concentrate into powder. 2. For example, the method for preparing a surfactant powder according to item 1 of the patent application 'wherein the content of the water-soluble polycarboxylic acid and / or its salt in the surfactant powder is the α-thio fatty acid alkyl ester With the total amount of soap · 0 ~ 1-3% by weight. 3. The method for preparing surfactant powder according to item 1 of the patent application, wherein the water-soluble polycarboxylic acid is selected from acrylic acid, methacrylic acid, maleic acid, and itaconic acid. Or a copolymer selected from two kinds of the above, or a copolymer produced by the above, or a copolymer selected from the group consisting of propionic acid, methyl amphoteric acid, 'maleic acid, more than one type of itaconic acid', and maleic anhydride Object 1 (Please read the note on the back before filling this page) This paper uses the Chinese national standard (CNS &gt; A4 size (210X297)) AS _416982_1 _: _ VI. Application scope of the patent The corresponding base cation of the salt is selected from the group consisting of alkali metals, alkaline earth metals, and ammonium. {Please read the notes on the back of the report before filling this page.) 4. If the surfactant is the first in the scope of patent application A method for producing a powder, wherein the weight average molecular weight of the water-soluble polycarboxylic acid is 10,000 or more. 5. For the method for preparing surfactant powder according to item 1 of the patent application, wherein the moisture content of the mixed slurry is 20-30% by weight. 6. —A kind of cleansing surfactant, which is characterized by: preparing a mixed slurry containing α-thio fatty acid alkyl ester, soap, water-soluble polycarboxylic acid and / or its salt, and concentrating the water content of the mixed slurry in 1 5% by weight or less, and the temperature of the concentrate is 70 ° C or less, and powdered to produce 40 to 84% by weight of ^ thio fatty acid alkyl ester and 10 to 54% by weight of soap. The total amount of the α-thio fatty acid alkyl ester and soap contains 0.01 to 5% by weight of a water-soluble polycarboxylic acid and / or a salt thereof, and the α-thio fatty acid alkyl ester in the surfactant and the The ratio of soap is 43: 5 7 ~ 89: 11 in weight ratio. Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs 7. If the surfactant of the scope of patent application is No. 6, the total amount of α-thio fatty acid alkyl ester and soap contains 0.1 to 3% by weight of water-soluble Polycarboxylic acids and / or their salts. a The surfactant according to item 6 of the application, wherein the water-soluble polycarboxylic acid is selected from the group consisting of acrylic acid, methacrylic acid, maleic acid, and itaconic acid, or a homopolymer thereof. 2. A variety of shapes described above-2- This paper size applies to Chinese National Standard (CNS) A4 specification (210X297 mm) Αδ B8 _416982_g_ · _ VI. Copolymers in the scope of patent application, or selected from acrylic acid, methacrylic acid 'Maleic acid, one or more of itaconic acid, a copolymer with maleic anhydride, and the corresponding cation of a water-soluble polycarboxylate are selected from one or more of alkali metals, alkaline earth metals, and ammonium. 9. The surfactant according to item 6 of the patent application &gt; wherein the weight average molecular weight of the water-soluble polycarboxylic acid is 10,000. 10. For example, the surfactant of item 6 of the patent application, wherein the moisture content of the mixed slurry is 20-30% by weight. 11. A granular tincture composition, characterized in that the surfactant such as item 6 of the patent application is mixed with other lotion ingredients through granulation or powder mixing. 12. The granular lotion composition according to item 11 of the scope of patent application, wherein the water content is 1 to 15% by weight, and the average particle size is 200 to 150,000 / zm ', and the bulk density is 0.4 g / cm3 or more. (Please read the precautions on the back before filling out this page) Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs This paper applies the Chinese National Standard (CNS) A4 specification (210X297 mm) Α8 Β8 C8 DSΑ8 Β8 C8 DS 經濟部智慧財產局員工消費合作社印製 第8710023 3號「界面活性劑粉體之製法及界面活性劑粉體 與粒狀淸潔.劑組成物·」専利案 (88年1 1月19日修正) 六、申請專利範圍: 1. 一種淸潔界面活性劑粉體之製造方法,其特徵爲調製 含有α -硫代脂肪酸烷酯,肥皂,水溶性聚羧酸及/或 鹽之混合淤漿,將此混合淤漿水分濃縮至1 5重量%以 下,此濃縮物之溫度在7 〇 °C以下後即予以粉體化,用 以製造含有.40~84重量%.之α -硫代脂肪酸烷酯,1 0~54 重量%之肥皂,相對於α -硫代脂肪酸烷酯與肥皂之總 量,係含有0.01〜5重量%之水溶性羧酸及/或其鹽 而上述界面活性劑粉體中之α -硫代脂肪酸烷酯與肥皂 • · . 之比率,依重量比計爲43: 57〜89: 11’且係直接粉 碎濃縮物予以粉體化’或將濃縮物壓九後粉碎使之粉 體化,或將濃縮物片狀化後粉碎予以粉體化。 2. 如申請專利範圔第1項之界面活性劑粉體之製法’其 中上述界面活性劑粉體中之水溶性聚羧酸及/或其鹽 之含量,係對α -硫代脂肪酸烷酯與肥皂總量之0 ·1〜3 重量%者。 3. 如申請專利範圍第1項之界面活性劑粉體之製法’其 中水溶性聚羧酸係選自丙烯酸,甲基丙烯酸’馬來酸’ 衣康酸之1種所生成之均聚物’或選自其中之2種 .以上所生.成之共聚物,或爲選自丙嫌酸,.甲基两嫌酸’ 馬來酸,衣康酸之1種以上’與馬來酸酐之共聚物1 (請先閲讀背面之注$項再填寫本頁) 本紙張尺度逋用中國國家標準(CNS &gt; Α4规格(210X297公兼)Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs No. 8710023 3 "Methods of Making Surfactant Powders and Surfactant Powders and Granular Cleansing Agent Compositions" Case (Amended on January 19, 88 ) 6. Scope of patent application: 1. A method for manufacturing cleansing surfactant powder, which is characterized by preparing a mixed slurry containing α-thio fatty acid alkyl ester, soap, water-soluble polycarboxylic acid and / or salt, The water content of this mixed slurry is concentrated to 15% by weight or less, and the temperature of the concentrate is reduced to 70 ° C or less, and then powdered to produce α-thio fatty acid alkane containing 40 to 84% by weight. Ester, 10 to 54% by weight of soap, 0.01 to 5% by weight of water-soluble carboxylic acid and / or its salt relative to the total amount of α-thio fatty acid alkyl ester and soap, and the above surfactant powder The ratio of α-thio fatty acid alkyl ester to soap • ·. Is 43: 57 ~ 89: 11 'by weight ratio, and the concentrate is directly pulverized and powdered; Powder, or pulverize the concentrate into powder. 2. For example, the method for preparing a surfactant powder according to item 1 of the patent application 'wherein the content of the water-soluble polycarboxylic acid and / or its salt in the surfactant powder is the α-thio fatty acid alkyl ester With the total amount of soap · 0 ~ 1-3% by weight. 3. The method for preparing surfactant powder according to item 1 of the patent application, wherein the water-soluble polycarboxylic acid is selected from acrylic acid, methacrylic acid, maleic acid, and itaconic acid. Or a copolymer selected from two kinds of the above, or a copolymer produced by the above, or a copolymer selected from the group consisting of propionic acid, methyl amphoteric acid, 'maleic acid, more than one type of itaconic acid', and maleic anhydride Object 1 (Please read the note on the back before filling in this page) This paper uses the Chinese national standard (CNS &gt; Α4 specification (210X297))
TW087100233A 1997-01-16 1998-01-09 Methods for producing a surface active agent fine particle, the surface active agent fine particle and the particle detergent composition TW416982B (en)

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