JPS5865799A - Continuous floating soap manufacturing apparatus - Google Patents

Continuous floating soap manufacturing apparatus

Info

Publication number
JPS5865799A
JPS5865799A JP16409781A JP16409781A JPS5865799A JP S5865799 A JPS5865799 A JP S5865799A JP 16409781 A JP16409781 A JP 16409781A JP 16409781 A JP16409781 A JP 16409781A JP S5865799 A JPS5865799 A JP S5865799A
Authority
JP
Japan
Prior art keywords
soap
mixing
cylinder
rotating shaft
stirring
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
JP16409781A
Other languages
Japanese (ja)
Other versions
JPS5927796B2 (en
Inventor
吉雄 田中
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.)
Ideal Soap Co
Original Assignee
Ideal Soap Co
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 Ideal Soap Co filed Critical Ideal Soap Co
Priority to JP16409781A priority Critical patent/JPS5927796B2/en
Publication of JPS5865799A publication Critical patent/JPS5865799A/en
Publication of JPS5927796B2 publication Critical patent/JPS5927796B2/en
Expired legal-status Critical Current

Links

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 本発明は空気又は他の気体を抱含して比重を軽くした浮
自石けんの製造装置に関し、特に圧出機よシ連続した石
けん棒を得る連続式浮色石けん製造装置に関するもので
ある。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for producing floating soap that has a reduced specific gravity by incorporating air or other gases, and in particular, a continuous process for producing floating soap that uses an extruder to obtain continuous soap bars. It is related to the device.

浮き石けん製造に関する公知の方法として、常法に依シ
得られたニート石けんを17.5 kg/+++”或い
はそれ以上の圧力の下で高圧蒸気に依って加熱される密
閉タイプの加熱器を通過する可くポンプ送付に依って大
兄200℃に迄加熱し石けんはそれから、スゲレイノズ
ルを通じてフラッシング室内に排出されそし−て夫処で
その水分含量が約20チに減少されるに足りる水分の蒸
発を伴って大気圧中に噴射され、同時に石けん温度は此
の減少された水分パーセントを含有する石けんの沸点に
対応する温度、即ち約106℃迄減少される、所謂7ラ
ツシング乾燥工程に依9、濃縮された熱熔融状態石けん
Ila、/ンlで連続式クラッチ1−に送給され、そし
て、夫処で香料、保存剤、着色料が1− Rovert
 V Burtの米国特許2,024,425及びされ
る、同時に、圧縮空気又は他の気体か、引き続く工程を
経て圧出された石けん棒がカッターに達した時に、その
比重が大兄080に減少するに充分な量で熔融石けん流
れ中に導入され、次いでボーチータフと称せられる特殊
な構造の冷却装置へ圧送され、ボーチーター内で冷却ジ
ャケットの内面で冷却され、スクシンパーに依って急速
に掻き取られ、スクシンA’−に依る攪拌に依って未冷
却上けんと混合され、そして冷却、攪拌された、ペース
ト状粘着性石けん塊が、ボーチーターに接続された絞シ
排出室末端の穴から圧出され、次いでカッターに達し切
断され型打ち成形されて浮き石けんを製造する方法が知
られて居るか、此の方法はフラッシング乾燥装置及びボ
ーチーター冷却装置を必要とし装置設備費が嵩み、操作
も複雑で高度の技術、経験を必要とし、又、濃縮された
高粘度の熔融状態石けん膠を連続式クラッチマー、そし
て−一テーター冷却装置そして絞り排出室へと圧送する
為の目的に適合し九ポングを必要とする等の難点があり
、此の製造方法は、今日迄餘り広く普及されていない。
As a known method for producing floating soap, neat soap obtained by a conventional method is passed through a closed-type heater heated by high-pressure steam under a pressure of 17.5 kg/+++" or higher. The soap is then heated to a temperature of 200 DEG C., preferably by pumping, and discharged through a sedge nozzle into a flushing chamber, with evaporation of sufficient moisture to reduce its moisture content to about 20 degrees centigrade. The soap is concentrated by a so-called 7-lash drying step, in which the soap is injected into atmospheric pressure and at the same time the temperature of the soap is reduced to a temperature corresponding to the boiling point of the soap containing this reduced moisture percentage, i.e. about 106°C. The hot molten soap Ila/l is fed to the continuous clutch 1-, and the perfume, preservatives and colorants are added to the continuous clutch 1- Robert
V. Burt, U.S. Pat. Sufficient quantities are introduced into the molten soap stream, which is then pumped into a specially designed cooling device called a Bocheetah, where it is cooled on the inner surface of a cooling jacket, rapidly scraped off by a scrunchper, and succin The paste-like sticky soap mass, which has been mixed with the uncooled soap by stirring according to A'-, and which has been cooled and stirred, is squeezed out from a hole at the end of the wringer discharge chamber connected to the bow cheater, There is a known method of producing floating soap by cutting it with a cutter and stamping it, but this method requires a flushing dryer and a bow cheetah cooling device, which increases the equipment cost and is complicated to operate. It requires a high degree of skill and experience, and is also suitable for the purpose of pumping concentrated, highly viscous, molten soap glue into a continuous clutch machine, a tater cooling device, and a squeezing discharge chamber. This manufacturing method has not been widely used to date because of the drawbacks such as the need for

又、浮き石けん製造に関して含有水分が30−〜35−
の高含有率である浮き石けんを連続的に注意することを
目的とし良製造方法が開示されて居る(%開開48−2
5706)。
Also, regarding the production of floating soap, the moisture content is 30-35-
A good manufacturing method has been disclosed for the purpose of continuously preventing floating soap with a high content of (% opening 48-2
5706).

ところが、世界的に需要を有していて「アイがリー」の
商品名で知られて居る浮き石けんは、含有水分が20%
近傍である。
However, floating soap, which is in demand worldwide and is known by the product name "Ai Gari", has a water content of 20%.
It's nearby.

此の事は、含有水分が30−〜355Gの浮き石けんは
、使用に際して摩擦溶解性が過大で、減り易く、又、製
造後、水分の蒸発が大で石けんが収縮変形し、商品価値
的に劣る難点を有しているこ、とを示す。
This is because floating soap with a water content of 30-355G has excessive friction solubility during use and is easily reduced, and after production, the water evaporates to a large extent and the soap shrinks and deforms, reducing its commercial value. Indicates that the product has inferior disadvantages.

本発明の目的は、フラッシング乾燥機を新たに必要とし
危いで、従来から石けん製造業に於いて通常使用されて
居る乾燥機、即ち、所謂ノ4ンド乾燥機、或いは真空乾
燥機で得られる、水分的20−から25チの固状の乾燥
石けんペレット、又はリボン或いは、フレークを出発素
材とし、〆−テーターと称せられる特殊な構造の冷却装
置に依る冷却工程を必要としないで、又、濃縮された高
粘度の熔融状態石けんを連続式クララチャーそしてだ一
チーター冷却装置、そして絞り排出室12圧送する為の
目的に適合したポンプをも必要としないで、又、香料、
保存剤、着色材を連続式クララチャー中へ比例供給する
為の比例注入定量ポンプを必要としないで、従来、石け
ん製造業界で汎用されて居る、ミキサーで、固状乾燥面
けんペレット17レーク或いねりがンに対して、香料、
保存剤、又は着色材を添加混合する、簡単な工程で得ら
れた、固状乾燥面けん素地を出発素材とする事が出来る
長所をも有し次、容易に浮き石けんを連続的に製造する
事を可能にした、連続式浮き石けん製造装置を提供する
事におる。
The object of the present invention is to avoid the need for a new flushing dryer, and to obtain a dryer that is conventionally used in the soap manufacturing industry, that is, a so-called 4-nd dryer or a vacuum dryer. Using solid dry soap pellets, ribbons, or flakes with a moisture content of 20 to 25 inches as the starting material, the method does not require a cooling process using a specially constructed cooling device called a tater, and can be concentrated. It also eliminates the need for a continuous clarifier and single-cheater cooler and a pump suitable for pumping the highly viscous molten soap into the squeezing discharge chamber 12;
The solid dry surface soap pellets can be mixed into 17 lakes in a mixer, conventionally used in the soap manufacturing industry, without the need for a proportional dosing metering pump to proportionally feed preservatives and colorants into a continuous clarifier. For inerigan, fragrance,
It has the advantage of being able to use a solid dry soap base as a starting material, which is obtained through a simple process of adding and mixing preservatives or colorants, and then easily producing floating soap continuously. To provide a continuous floating soap manufacturing device that makes it possible to do this.

常法により、得られた脂肪酸のアルカリ金属塩、一般的
には、脂肪酸のす) IJウム塩又は脂肪酸のナトリウ
ム塩と脂肪酸のカリウム塩よ構成る混合物よ構成る、含
有水分3091g近傍の石けん膠を周知の乾燥方法に依
シ乾燥して得られた含有水分20嗟近傍の、固状乾燥石
けんのペレット又はリボン、或いは、フレークを田発素
材とし、此れに必要とあれば、酸化チタン、着色料、保
存料、査料及び他の添加剤を添加混合した後、円胴内で
回転する写スクリーウを装備し、石けんを圧搾、圧出す
る、所謂ブレゾロツメ−素材供給口であるホッパーに送
付する。
Soap glue with a water content of around 3091 g, consisting of an alkali metal salt of a fatty acid (generally a fatty acid salt) or a mixture of a sodium salt of a fatty acid and a potassium salt of a fatty acid, obtained by a conventional method. Solid dried soap pellets, ribbons, or flakes with a moisture content of around 20 oz obtained by drying using a well-known drying method are used as the Tahatsu material, and if necessary, titanium oxide, titanium oxide, After colorants, preservatives, test materials and other additives are added and mixed, the soap is sent to a hopper, which is a so-called Bresolotme material supply port, which is equipped with a scroll that rotates inside the cylinder and presses and squeezes out the soap. do.

ブレプロラダー出口端には、間隔を距てて、同一中心軸
を有して垂直に配置された、同一ピッチの多孔円板よ構
成る2枚の管板の対面する穴同志を管材でそれぞれ連結
し、プレ10ツメ−円胴内を、スクリユウの回転によシ
圧縮移送される石けんが、管内を通過するようにし、管
内を通過する石けんを管外より、蒸気又は他の加熱媒体
で加熱す石所謂、多管群よ構成る熱交換器を接続し、次
いで熱交換器を出た、半熔融状類似状態の石けんを温度
差を減らす為に1均一に攪拌混和する為の、円胴内にて
回転軸によシ、攪拌羽根又は、石けんの流わに対し抵抗
を与える混和攪拌機能を有した邪魔板が回転する、混和
攪拌室を接続する。かかる通過石けんに対する加熱の為
の熱交換器及び混和攪拌室の工程を少く共、−組以上を
経て半熔融状類似状態に斉らせられた石けんは、連絡管
路を経て、プレプロラダースクリュウ回転軸と4別個の
回転軸を有した、シリンダー内壁面に櫛溢に半月形横断
面形状の固定ビンが装着され、回転軸には、やはシ半月
形の横断面形状を有し、固定ピンの直面部と回転の際に
、半月形横断面形状よ構成るニーダ−ビンの直面部が向
い合う方向で配置されたニーダ−ビンがらせん状に装着
されて居シ、回転軸の回転により=−ダービンは固定ビ
ン同志の間隙を通過する事に依り剪断の作用をも伴った
混和、分散、熟成が行なわれる、剪断、混和、分散、熟
成シリンダー中に入来する。
At the exit end of the Brepro ladder, the facing holes of two tube plates made up of perforated disks with the same pitch and arranged vertically at a distance from each other with the same center axis are connected by pipe materials. , Pre-10 claws - The soap that is compressed and transferred by the rotation of the screw passes through the tube, and the soap that passes through the tube is heated from outside the tube with steam or other heating medium. A heat exchanger consisting of a so-called multi-tube group is connected, and then the soap, which is in a similar state to a semi-molten state, exiting the heat exchanger is stirred and mixed uniformly in order to reduce the temperature difference. A mixing and stirring chamber in which a stirring blade or a baffle plate having a mixing and stirring function that provides resistance to the flow of soap rotates is connected to the rotating shaft. The soap that has been brought to a state similar to a semi-molten state through a heat exchanger for heating and a mixing and stirring chamber for heating the passed soap passes through a connecting pipe and is heated by a rotating pre-pro ladder screw. A fixed pin with a half-moon cross section is attached to the inner wall of the cylinder, which has a shaft and four separate rotating shafts. When the face part of the kneader bin and the face part of the rotating shaft are rotated, the kneader bin, which has a half-moon cross-sectional shape and is arranged in such a direction that the face part of the kneader bin faces each other, is mounted in a spiral shape. - The durbin enters the shearing, mixing, dispersing and maturing cylinder, where mixing, dispersing and maturing with the effect of shearing takes place by passing through the gaps between the fixed bottles.

連絡管路内には外部よf)ノ+イノ路を経て圧縮空気又
は他の圧縮気体が、半熔融状類似状態の石けんの流れ中
に、最終製品が比重0.8から0.95の範域で得られ
る様な割シ合いで圧入される。
In the communication pipe, compressed air or other compressed gas is passed from the outside through the flow line to the flow of semi-molten soap, and the final product has a specific gravity in the range of 0.8 to 0.95. It is press-fitted at a ratio that can be obtained in the area.

剪断、混和、分散、熟成シリンダー出口側には、回転軸
の一端を支える軸受けがあり、軸受けはシリンダー内壁
面から支持部材で支えられて居る。
On the exit side of the shearing, mixing, dispersing, and maturing cylinder, there is a bearing that supports one end of the rotating shaft, and the bearing is supported by a support member from the inner wall of the cylinder.

此の回転軸、軸受は支持部材を通過した石けんに、更に
攪拌、混和を作用させる攪拌羽根又は他の回転抵抗体が
、回転軸の軸受けよシ、出口側延長軸に装着されて居る
A stirring blade or other rotational resistor for further stirring and mixing the soap that has passed through the support member is attached to the bearing of the rotating shaft and the extension shaft on the outlet side.

次いで、先端に圧出石けん棒の横断面形状を定める、所
謂口金と称せられる開口部材を装着した絞り室が連結さ
れて居る。
Next, a squeezing chamber is connected to the tip, which is equipped with an opening member called a mouthpiece, which defines the cross-sectional shape of the pressed soap bar.

グレグロッダー石けん素材供給ロホッノ4−より送付さ
れた、含有水分2〇−近傍の固状石けん素材は、プレグ
ロッダー円胴内で回転するスクリ具つに依って多管群よ
構成る、加熱を目的とした熱交換器管内を通過する間に
、管外部よシ蒸気又は他の加熱媒体で加熱され半熔融状
類似状11に斉らせらね、次いで混和、攪拌を受け、か
かる熱交換器での加熱、そして混和室での混和、攪拌の
工1!i&を少く共、それぞれ−回以上経て、連絡管路
を通過して、櫛形固定ビンの間隙を通過して回転する二
一ターヒンを回転軸に装着した、シリンダーで構成され
る、剪断、混和、分散、熟成シリンダー中に送入される
。連絡管路では、外部より、I4イブ路を経て、圧縮空
気又は他の圧縮気体が連絡管路内を通過する半熔融状類
似状態の石けんの流に中に注入される。剪断、混和、分
散、熟成シリンダー内では、連絡管路で注入された気体
を、繊細な気泡に分散し気体ケ含んだ均質な石けん塊と
してそして、その杉林を保持し得る状態で絞p室開口部
より連続棒として、水より比重の軽い、石けんが圧出さ
れる。この石けん連続棒を切断してビレットと成し、次
いで型打ち底型して浮き石けん製品を得る事が出来た。
The solid soap material with a moisture content of around 20, sent from Gregrodder soap material supply Rochno 4-, is made up of a multi-tube group by a screw rotating inside the Pregrodder cylinder, and is intended for heating. While passing through the heat exchanger tube, the outside of the tube is heated with steam or other heating medium to uniformly form a semi-molten analogue 11, and then mixed and stirred, heated in such a heat exchanger, And mixing and stirring in the mixing room 1! The shearing, mixing, Dispersion and feeding into maturation cylinders. In the connecting line, compressed air or other compressed gas is injected from the outside via the I4 pipe into the flow of semi-molten soap passing through the connecting line. Shearing, mixing, dispersing, and maturing Inside the cylinder, the gas injected through the connecting pipe is dispersed into delicate bubbles to form a homogeneous soap mass containing gas. Soap, which has a lighter specific gravity than water, is squeezed out as a continuous rod. This continuous bar of soap was cut into billets, and then molded into a bottom mold to obtain a floating soap product.

なお、此処での説明は脂肪酸のナトリウム塩又は脂肪酸
のナトリウム塩と脂肪酸のカリウム塩の混合物より成る
、脂肪酸アルカリ金属塩に就いて記述したが、本発明は
固型合成洗剤又は石けんと合成洗剤両者の混合物である
固型浮き洗滌剤に関しても適用されるものである。
Note that although the explanation here has been made with respect to fatty acid alkali metal salts consisting of sodium salts of fatty acids or mixtures of sodium salts of fatty acids and potassium salts of fatty acids, the present invention is applicable to solid synthetic detergents or both soap and synthetic detergents. This also applies to solid floating detergents that are mixtures of.

圧縮空気又は他の圧縮気体を半熔融状類似状態の石けん
の流れ中に注入する連絡管路で、香料、着色剤又は他の
添加剤を外部よp半熔融状類似状態の石けんの流れ中に
注入する事も可能であり、本発明の思想を逸脱するもの
ではない。
A connecting line through which compressed air or other compressed gas is injected into the flow of semi-molten soap, and where fragrances, colorants or other additives are externally injected into the flow of semi-molten soap. Injection is also possible and does not depart from the spirit of the present invention.

以下、図面に基づいて本発明を説明する。The present invention will be explained below based on the drawings.

第1図は本発明の一実施例を示すものである。FIG. 1 shows an embodiment of the present invention.

1はプレグロッ〆一で2は多管群よ構成る、管群を構成
する管内通過面けん加熱の為の熱交換器で、3は熱交換
器2で加熱された石けんを攪拌、混和し、その石けんの
温度差を減少させる為の混和攪拌室、5は、剪断、混和
、分散、熟成シリンダーで4は最終の混和攪拌室3と剪
断、混和、分散、熟成シリンダー5の石けん供給口とを
連結する連絡管路で、6は末端に開口部を有した絞り室
で、7は連絡管路4を通過する、半熔融状類似状態の石
けんの流れ中に、最終的に得られる石けんが使用時に、
水又は温湯で浮かぶ様な比重を有する様な割p合いて圧
縮空気又は他の圧縮気体を注入する為の圧縮気体管路で
あゐ。
1 is a pre-glot finisher, 2 is a multi-tube group, and is a heat exchanger for heating the passing surface inside the tubes constituting the tube group; 3 is a heat exchanger for stirring and mixing the soap heated by the heat exchanger 2; A mixing and stirring chamber 5 is a shearing, mixing, dispersing, and maturing cylinder for reducing the temperature difference of the soap, and 4 is a final mixing and stirring chamber 3 and a soap supply port of the shearing, mixing, dispersing, and maturing cylinder 5. Connecting connecting pipes, 6 is a squeezing chamber with an opening at the end, and 7 is a flow of soap in a state similar to that of a semi-molten state that passes through the connecting pipe 4, and the soap finally obtained is used. Sometimes,
This is a compressed gas pipe for injecting compressed air or other compressed gas at a rate that has a specific gravity such that it floats on water or hot water.

ブレプロラダ−1は固状のペレット又はりビン又は、フ
レーク形態の石けん素材供給の為、円胴端部のホラ−f
−3から送付さ−れた石けん素材を図には示して居ない
駆動装置に依って、回転する回転軸12を回転軸として
円胴9内で回転する、スフリーラ10が装備され、円胴
9の外周には、スクリユウ10の回転に依る石けん素材
の円胴9内での圧出、移送を容易にする為の冷却水循環
の為のジャケット11が装着されて居る。
The Brepro ladder 1 has a hollow f at the end of the cylinder to supply soap material in the form of solid pellets, bottles, or flakes.
A soap material sent from -3 is equipped with a soap material 10 that rotates within the cylinder 9 with a rotating shaft 12 as the rotation axis by a drive device not shown in the figure. A jacket 11 for circulating cooling water is attached to the outer periphery of the bar to facilitate the extrusion and transfer of soap material within the cylinder 9 by the rotation of the screw 10.

多管群より成る管内通過面けん加熱の為の熱交換器2は
同一中心軸を有して垂直に間隔を隔てて垂直に配置され
た、同一ピッチの多孔円板よ構成る2枚の管板22の対
面する穴同志を管13でそれぞれ連結し、管13内を石
けんが通過する多管群を構成し、此の多管群は両端の2
枚の管板22の外周部で連結され次外胴14で包囲され
、外胴14は加熱蒸気入口15及び出口16を有して周
り、多管群を構成する管13のそれぞれを管外よシ蒸気
で加熱する。多管群より成る熱交換器2の水平中心部に
は、スクリユウ10の延長軸である回転軸17が貫通し
て周り、回転軸17の外周には、回転軸170回転を妨
げないで、かつ多管群加熱蒸気と遮断する為の新らたな
管路が、間隔を隔てて垂直に配置された2枚の管板の中
心部同志を貫通して連結装着されて居る。
A heat exchanger 2 for heat exchanger heating at a pipe passage surface, which is made up of a group of multiple tubes, consists of two tubes that have the same central axis, are vertically spaced apart, and are composed of perforated disks with the same pitch. The facing holes of the plate 22 are connected by pipes 13 to form a multi-tube group through which the soap passes, and this multi-tube group has two holes at both ends.
The outer shell 14 has a heating steam inlet 15 and an outlet 16, and is surrounded by a heated steam inlet 15 and an outlet 16. Heat with steam. A rotating shaft 17, which is an extension of the screw 10, passes through the horizontal center of the heat exchanger 2, which is made up of a group of multiple tubes. A new pipe line for isolating the multi-tube group heating steam is connected and passed through the centers of two vertically spaced tube plates.

混和攪拌室3は円胴23内にてスフリーラ10の延長軸
である回転軸17が存在し、回転軸17に攪拌、混和の
手段として、円胴23内で回転する、多孔円類似形板1
8が回転軸lフに傾斜して装着されて居る。此の傾斜し
て回転軸17に装着された、多孔円類似形板18ri、
例えば種型の攪拌翼でありても差し支えない。
The mixing/stirring chamber 3 has a rotary shaft 17, which is an extension of the souffler 10, in the cylinder 23, and a perforated circular-like plate 1, which rotates in the cylinder 23, is attached to the rotary shaft 17 as a stirring and mixing means.
8 is mounted at an angle to the rotation axis l. This perforated circle-like plate 18ri is mounted on the rotating shaft 17 in an inclined manner,
For example, a seed-shaped stirring blade may be used.

前記し九加熱の為の熱交換器2及び混和攪拌蔓3の新た
な一組が次いで接続されて居シ、最終の混和、攪拌室3
の出口端は、連絡管路4で、剪断、混和、分散、熟成シ
リンダー5の半熔融状面けん供給口24と連結されて居
り、連絡管路4内には、外部より圧縮空気輸送管路7が
貫通して周り、その先端には少く共一つ以上のノズル2
1が装備されてRD、圧縮空気管路7からの圧縮空気が
ノズル21を通じて、連絡管路4内を通過する、半熔融
状類似状態の石けんの流れ中VC注入される0図では示
されて居々い圧縮空気源より送付される圧縮空気は、−
次減圧弁37及び圧力計38で圧力を調整されて、気体
流量計39及び二次減圧弁40及び圧力計41及びニー
ドルバルブ42の手段に依って、一定の圧力の一定量の
圧縮空気が配管7を通じて、ノズル21から連絡管路4
中の半熔融状類似状態の石けんの流れの中に圧出された
石けんが比重0.8から0.95に斉らせられる様な割
シ合いで注入される。
A new set of heat exchanger 2 for heating and mixing and stirring chamber 3 are then connected to the final mixing and stirring chamber 3.
The outlet end of the connecting pipe 4 is connected to the semi-molten surface supply port 24 of the shearing, mixing, dispersing, and maturing cylinder 5, and the communicating pipe 4 is connected to a compressed air transport pipe from the outside. 7 passes through and surrounds it, and at least one or more nozzles 2 are installed at its tip.
1 is equipped with RD, the compressed air from the compressed air line 7 is injected through the nozzle 21 into the flow of soap in a semi-molten state, which passes through the connecting line 4 (not shown in the figure). Compressed air sent from a common compressed air source is -
The pressure is adjusted by the secondary pressure reducing valve 37 and the pressure gauge 38, and a constant amount of compressed air at a constant pressure is supplied to the pipe by means of the gas flow meter 39, the secondary pressure reducing valve 40, the pressure gauge 41, and the needle valve 42. 7, from the nozzle 21 to the connecting pipe 4
The pressed soap is injected into the flow of soap, which is in a semi-molten state, at such a rate that its specific gravity is uniformly adjusted from 0.8 to 0.95.

剪断、混和、分散、熟成シリンダー5は円胴25内壁面
に、一定のピッチで半月形横断面形状の固定ビン26が
櫛型に装着され、回転軸28には、やはり半月形の横断
面形状を有し、固定ビンの直面部と回転の際に、半月形
横断面形状より成るニーダ−ビン27の直面部が向い合
う方向で配置されたニーダ−ビン27が回転軸28にら
せん状に装着されて居シ、回転軸28の回転に依シ、ニ
ーダ−ビン27は隣り合った固定ビン26同志の間−を
通過する事によ)、よ〕効果的な剪断の作用をも伴った
、混和、分散が行なわれる。連絡管路4中でノズル21
から半熔融状類似状態の石けんの流れの中に注入された
圧縮空気は、剪断、混和、分散、熟成シリンダー内を通
過する間に、小胞状気体として繊細に、良好に石けん塊
中に分散され、実質上均質な石けん塊として、絞り室6
−へと送付される。剪断、混和、分散、熟成シリンダー
の回転軸28の石けんの流れ方向に関して、上流側延長
軸は、図示されていない、外部よりの駆動によフ回転運
動が与えられる。
In the shearing, mixing, dispersing, and maturing cylinder 5, fixed bins 26 each having a half-moon cross section are attached to the inner wall surface of the cylinder 25 in a comb shape at a constant pitch. The kneader bin 27 is arranged in such a direction that the face part of the fixed bin faces the face part of the kneader bin 27 having a half-moon cross-sectional shape during rotation, and is spirally attached to the rotating shaft 28. Depending on the rotation of the rotary shaft 28, the kneader bins 27 pass between adjacent fixed bins 26), with an effective shearing action. Mixing and dispersion are performed. Nozzle 21 in connecting pipe 4
The compressed air injected into the flow of soap in a semi-molten state is delicately and well dispersed into the soap mass as a vesicular gas while passing through the shearing, mixing, dispersing and maturing cylinder. , as a substantially homogeneous soap mass in the squeezing chamber 6
− will be sent to. With respect to the soap flow direction of the rotating shaft 28 of the shearing, mixing, dispersing, maturing cylinder, the upstream extension shaft is given a rotational motion by an external drive (not shown).

回転速度は100 rpmから30 Orpmで充分カ
結果が得られる。
Sufficient results can be obtained at a rotation speed of 100 rpm to 30 rpm.

回転軸28の石けんの流れ方向に関して下流側には、回
転軸28の一端を支える、回転軸軸受け29が円胴25
内壁面に装着された、回転軸軸受は支持部材30によシ
保持されて居る。
On the downstream side of the rotating shaft 28 in the soap flow direction, a rotating shaft bearing 29 supporting one end of the rotating shaft 28 is connected to the cylinder 25.
A rotary shaft bearing mounted on the inner wall surface is held by a support member 30.

を通過した半熔融状類似状態の石けん塊に攪拌、混和作
用を与える攪拌羽根32が装着されて居る。
A stirring blade 32 is attached to give a stirring and mixing effect to the semi-molten soap mass that has passed through the soap block.

回転軸軸受は支持部材30を通過した半熔融状類似状態
の石けん塊に更に、攪拌、混和作用を与える目的での攪
拌羽根又は他の回転抵抗体の、回転軸28の延長軸31
への装着によシ、回転による攪拌、混和作用を行う事は
本発明にとって必須の事項である。何故なれば、回転軸
軸受は支持部9゜ 材30を通過する事に依って、剪断、混和、分散、熟成
作用を受けた半熔融状類似状態の石けん塊の流れは、分
剰され、分離層を生じ易く、攪拌羽根32の回転による
攪拌、混和によって、はじめて、此の分側層を解消し、
均一な組織の繊細な気泡を一様に分散した、良好な浮き
石けんを得ることが出来るからである。
The rotating shaft bearing is an extension shaft 31 of the rotating shaft 28 of a stirring blade or other rotational resistance body for the purpose of further stirring and mixing the soap lump in a state similar to that of a semi-molten state that has passed through the support member 30.
It is essential for the present invention to perform agitation and mixing by rotation during installation. This is because the rotating shaft bearing passes through the supporting portion 9° material 30, so that the flow of soap lumps in a state similar to a semi-molten state that has been subjected to shearing, mixing, dispersion, and aging is divided into parts and separated. It is easy to form layers, and only by stirring and mixing by the rotation of the stirring blade 32 can this side layer be eliminated.
This is because it is possible to obtain a good floating soap in which fine air bubbles with a uniform structure are uniformly dispersed.

固定ビン26及びニーダ−ピン27の横断面形状は、本
実施例では半月形形状を有して居るが、そO横断面形状
を半月形形状に必らずしも限定するものではなく、例え
ば、円形横断面形状であっても本発明の思想を逸脱する
ものではない。
Although the fixed bin 26 and the kneader pin 27 have a half-moon shape in cross-section in this embodiment, the cross-sectional shape is not necessarily limited to the half-moon shape; for example, , a circular cross-sectional shape does not depart from the spirit of the present invention.

剪断、混和、分散、熟成シリンダー5の出口端には、先
端に圧出石けん棒の横断面形状を定める、所謂、口金と
称せられる開口部材34がホルダー35で装着されて居
る絞〕室6が、接続されて居シ、絞〉室の外套36は、
圧出石けん棒の温度よシ、少く共低くない温度の温水が
循環して居る。
At the outlet end of the shearing, mixing, dispersing, and maturing cylinder 5, there is a diaphragm chamber 6 in which an opening member 34, also called a mouthpiece, which defines the cross-sectional shape of the extruded soap bar at its tip is attached by a holder 35. The mantle 36 of the connected chamber is
Warm water, at a temperature not lower than that of the pressed soap bar, is being circulated.

開口部材34の圧田連続石けん棒の望まれる横断面形状
を与える開口部から、半熔融状類似状態の、しかし、そ
の形状を保持し得る、可塑性を有した状態での浮き石け
ん連続棒が圧出される。
From the opening of the opening member 34 that gives the desired cross-sectional shape of the pressed continuous soap bar, a floating continuous bar of soap in a state similar to a semi-molten state, but with plasticity capable of retaining its shape, is pressed. Served.

此の連続頁けん棒は、圧出後、望まれる長さの短い長さ
の個々の棒片に切断され、そして渥打ち成製され浮き石
けん製品を容易に製造する事が出来る。
After extrusion, this continuous bar can easily be cut into individual bar pieces of desired short length and hammered into floating soap products.

混和攪拌室3の円胴23の外側には、ジャケット19が
、連絡管路4の外側には、ジャケット20が、剪断、混
和、分散、熟成シリンダー5の円胴25の外側にはジャ
ケット33がそれぞれ錬備されて居り、これは浮き石け
ん製造装置運転中には、特に、加熱又は冷却等O熱収支
を外部より特に必要とするもので社なく、浮自石けん製
造装置運転中断時、或いは中断後の再開始の際に1混、
和攪拌室3、連絡管路4、及び剪断、混和、分散、熟成
シリンダー5内に滞留して居る半熔融状類似状態の石け
んの温度低下による、冷却同化を防止する為の熱水の循
環による保温、又は、滞留した石けんが、固化した場合
、運転再開に先立って加熱蒸気によって固化した滞留石
けんを半熔融状類似状態迄加温する為のものである。
A jacket 19 is placed on the outside of the cylinder 23 of the mixing and stirring chamber 3, a jacket 20 is placed on the outside of the connecting pipe 4, and a jacket 33 is placed outside the cylinder 25 of the shearing, mixing, dispersing, and maturing cylinder 5. They are prepared separately during the operation of the floating soap production equipment, especially those that require O heat balance from the outside, such as heating or cooling, and are not used during the operation of the floating soap production equipment or when the operation of the floating soap production equipment is interrupted. 1 mix when restarting later,
By circulating hot water to prevent cooling and assimilation by lowering the temperature of the soap, which is in a state similar to a semi-molten state, staying in the stirring chamber 3, the connecting pipe 4, and the shearing, mixing, dispersing, and maturing cylinder 5. This is to keep the soap warm or to heat the solidified soap to a state similar to a semi-molten state using heated steam before restarting operation if the soap has solidified.

第2図は混和攪拌室3に於いて円胴23内壁面に近接し
て回転するように、回転軸17に傾斜して装着された、
円類似形状の外郭を有した、多孔板である、多孔円類似
形板18の縦断面図であシJ第3図はこの多孔円類似形
板を■−■方向つ咲禮凱豐1■外である。
FIG. 2 shows a rotary shaft 17 mounted at an angle to the rotating shaft 17 so as to rotate close to the inner wall surface of the cylinder 23 in the mixing and stirring chamber 3.
Fig. 3 is a longitudinal cross-sectional view of a perforated circular-like plate 18, which is a perforated plate having a circular-like outer contour. It's outside.

多孔円類似形板18は石けん素材が通過する多数の孔1
8&を有し、石けんの流れに抵抗な与える邪魔板となる
The porous circle-like plate 18 has a large number of holes 1 through which the soap material passes.
It has 8&, and serves as a baffle plate that provides resistance to the flow of soap.

以上、説明したように本発明に係る連続式浮き石けん製
造装置においては、フラッシング乾all、〆−テータ
ー等を必要とせずt九連続式クラッチ4−1@−チータ
ー絞シ排出室等に高粘度の椿融状石けんを供給するため
の一ング等の付属設備等も必要としないで、石けん製造
業界において通常の手段で容易に入手可能力水分20〜
25%の固状乾燥面けんを用いて、装置構造を複雑にす
るこ・となく簡単な工程で、使用に際し適度な摩擦溶解
性を有し経時に伴う収縮変形の少い優れた品質の浮き石
けんを得ることかで龜る。
As explained above, in the continuous type floating soap manufacturing apparatus according to the present invention, there is no need for flushing, drying, closing, etc. It is easily available in the soap manufacturing industry by normal means without the need for additional equipment such as a tool for dispensing camellia molten soap with a water content of 20 to 20%.
Using 25% solid dry surface buoy, it is a simple process without complicating the structure of the device, and it has an appropriate friction solubility during use and has low shrinkage and deformation over time, making it an excellent quality float. It's hard to get soap.

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

第1図は本発明に係る連続式浮き石けん製造装置の垂直
断面図、第2図は第1図の装置内で用いる多孔円類似形
板の縦断面図、第3図は第2図の■−1方向の矢視図で
ある。 1・・・ブレプロラダー、2・・・熱交換器、3・・・
混和攪拌室、4・・・連絡管路、5・・・剪断混和分散
熟成シリンダ、6・・・絞り室、7・・・圧縮気体管路
、8・・・ホッノダー、9・・・円胴、10・・・スク
リムつ、12・・・回転軸、13・・・管、17・・・
回転軸、18′・・・多孔円類似形板、21・・・ノズ
ル、22・・・管板、26・・・固定ビン、27・−・
ニーダ−ピン、29・・・回転軸軸受け、30・・・回
転軸軸受は支持部材、32・・・攪拌羽根。 特許出願人 アイデアル石鹸株式会社 特許出瓢代理人 弁理士 青 木   朗 弁理士西舘和之 弁現出中山恭介 弁理士 山 口 昭 之 第 2図 P− 第3図
Fig. 1 is a vertical sectional view of a continuous floating soap manufacturing apparatus according to the present invention, Fig. 2 is a longitudinal sectional view of a plate similar to a perforated circle used in the apparatus of Fig. 1, and Fig. 3 is a vertical sectional view of It is an arrow view of -1 direction. 1... Brepro ladder, 2... Heat exchanger, 3...
Mixing/stirring chamber, 4: Connecting pipe, 5: Shearing, mixing, dispersing and maturing cylinder, 6: Squeezing chamber, 7: Compressed gas pipe, 8: Hochnoder, 9: Cylindrical cylinder , 10... Scrim, 12... Rotating shaft, 13... Pipe, 17...
Rotating shaft, 18'... Porous circular similar plate, 21... Nozzle, 22... Tube plate, 26... Fixed bottle, 27...
Kneader pin, 29... Rotating shaft bearing, 30... Rotating shaft bearing is a supporting member, 32... Stirring blade. Patent Applicant: Ideal Soap Co., Ltd. Patent Agent: Akira Aoki, Patent Attorney: Kazuyuki Nishidate, Patent Attorney: Kyosuke Nakayama, Patent Attorney: Akira Yamaguchi, Figure 2, P-Figure 3

Claims (1)

【特許請求の範囲】[Claims] 1、一端に乾燥固状石けん素材供給の為の開口部を設は
九円胴内にて回転するスクリ為つを装備し次スクリ、つ
圧出機の円胴出口端に、外部より、蒸気又は他の加熱媒
体に依9、管内を通過する石けんを管外周面より加熱す
る、多管群より成る熱交換器を連結し、次いで熱交換器
で加熱さ訃圧出された石けんを、円胴内で機械的に混和
、攪拌する為の回転する攪拌翼又は、石けんの流れに対
して抵抗を与え、混和、攪拌機能を有した回転邪魔板を
装備した混和攪拌室を構成す石円胴を連結し、かかる多
管群よ構成る加熱の為0熱交換器及び混和攪拌室よ構成
る一連の工程の少く共−組以上の工程を装備し、最終の
混和撹拌室出口には、粘着性を有した、半熔融状類似状
態に斉らせられた石けんを、シリンダー内壁面に櫛形に
固定ピンが装着され、スクリ為り圧出機スクリムつの回
転軸とは別個の回転軸に、ニーダ−ビンが回転軸の回転
により隣り合った固定ビン同志の間隙を通過する様に装
着され、剪断の作用をも伴り危、混和、分散、熟成の作
用が石けんに対して与えられる、剪断、混和、分散、熟
成シリンダー中に、送付する為の連絡管路を接続し、該
、連w1管路内には、外部より導管に依り供給される圧
縮空気又は他の圧縮気体を半熔融状類似状態の石けんの
流れ中に注入する為の少く共一つ以上の圧縮気体出口を
構成する小孔が装備されて層り、剪断、混和、分散、熟
成シリンダー出口側には回転軸の一端を支える軸受けが
あり、軸受けはシリンダー内壁面から支持部材で保持さ
れて居シ、そして此の回転軸軸受は支持部材を通過した
石けん塊に更に、混和、攪拌作用金与える攪拌羽根又は
、石けんの流れに対し、抵抗を与える混和、攪拌機能を
有した、邪魔板が回転軸の軸受けを通過し次出口側延長
軸に装着されて周り、そして、剪断、混和、分散、熟成
シリンダー田口端には、先端に圧出面けん連続棒の望ま
れる、横断面形状を与える形状の開口部を有した絞り室
が連結されて居る事を%黴とした連続式浮き石けん製造
装置。
1. One end is equipped with an opening for supplying dry solid soap material, and the second screw is equipped with a screw that rotates inside a nine-cylinder cylinder. Alternatively, depending on another heating medium, a heat exchanger consisting of a group of multiple tubes is connected to heat the soap passing through the tubes from the outer peripheral surface of the tubes, and then the soap heated by the heat exchanger and pressed out is heated in a circular A stone cylinder that constitutes a mixing and stirring chamber equipped with rotating stirring blades for mechanically mixing and stirring within the barrel, or a rotating baffle plate that provides resistance to the flow of soap and has mixing and stirring functions. The multi-tube group is equipped with at least a series of steps consisting of a heat exchanger for heating and a mixing and stirring chamber, and the final mixing and stirring chamber outlet is equipped with an adhesive A comb-shaped fixing pin is attached to the inner wall of the cylinder, and the soap, which has been brought into a state similar to a semi-molten state, is placed in a kneader on a rotating shaft that is separate from the scrim-like rotating shaft of the scrim extruder. - The bottles are mounted so that they pass through the gap between adjacent fixed bottles by the rotation of the rotating shaft, and the soap is subjected to dangerous, mixing, dispersing, and maturing effects due to the shearing action. A connecting pipe is connected to the mixing, dispersing, and maturing cylinder for sending compressed air or other compressed gas supplied from the outside through the pipe into the connecting pipe. The cylinder is equipped with small holes constituting at least one outlet for injecting at least one compressed gas into the soap stream, shearing, mixing, dispersing, and maturing.The outlet side of the cylinder supports one end of the rotating shaft. There is a bearing, and the bearing is held by a support member from the inner wall surface of the cylinder, and this rotating shaft bearing is used to further mix and stir the soap lumps that have passed through the support member. On the other hand, the baffle plate with the mixing and stirring function that gives resistance passes through the bearing of the rotating shaft and is attached to the next outlet side extension shaft, and the tip of the shearing, mixing, dispersion, and ripening cylinder Taguchi end A continuous type floating soap production device in which a squeezing chamber having an opening shaped to give a desired cross-sectional shape of a continuous extruding surface bar is connected to the bar.
JP16409781A 1981-10-16 1981-10-16 Continuous floating soap manufacturing equipment Expired JPS5927796B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16409781A JPS5927796B2 (en) 1981-10-16 1981-10-16 Continuous floating soap manufacturing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16409781A JPS5927796B2 (en) 1981-10-16 1981-10-16 Continuous floating soap manufacturing equipment

Publications (2)

Publication Number Publication Date
JPS5865799A true JPS5865799A (en) 1983-04-19
JPS5927796B2 JPS5927796B2 (en) 1984-07-07

Family

ID=15786704

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16409781A Expired JPS5927796B2 (en) 1981-10-16 1981-10-16 Continuous floating soap manufacturing equipment

Country Status (1)

Country Link
JP (1) JPS5927796B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5912999A (en) * 1982-07-12 1984-01-23 東山油脂工業株式會社 Method and apparatus for producing improved float soap bar
WO1996025480A1 (en) * 1995-02-17 1996-08-22 Flores Michel Ramirez Low-density toilet soap

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011122187A1 (en) 2010-03-29 2011-10-06 株式会社ピーアンドピーエフ Framed soap and method for producing same
JP5763310B2 (en) 2010-08-12 2015-08-12 株式会社ピーアンドピーエフ Frame kneaded soap and method for producing the same

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5912999A (en) * 1982-07-12 1984-01-23 東山油脂工業株式會社 Method and apparatus for producing improved float soap bar
JPH0365400B2 (en) * 1982-07-12 1991-10-11
WO1996025480A1 (en) * 1995-02-17 1996-08-22 Flores Michel Ramirez Low-density toilet soap

Also Published As

Publication number Publication date
JPS5927796B2 (en) 1984-07-07

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