JPS5820228A - Granulator for sodium percarbonate and method for granulating same - Google Patents

Granulator for sodium percarbonate and method for granulating same

Info

Publication number
JPS5820228A
JPS5820228A JP11964081A JP11964081A JPS5820228A JP S5820228 A JPS5820228 A JP S5820228A JP 11964081 A JP11964081 A JP 11964081A JP 11964081 A JP11964081 A JP 11964081A JP S5820228 A JPS5820228 A JP S5820228A
Authority
JP
Japan
Prior art keywords
screw
feed
granulator
kneading
blades
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
JP11964081A
Other languages
Japanese (ja)
Other versions
JPS5924085B2 (en
Inventor
Junichiro Sugano
菅野 順一郎
Shuichi Kobayashi
秀一 小林
Tomoyuki Yui
油井 知之
Tsuneo Fujimoto
藤本 常夫
Minoru Kubota
稔 窪田
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.)
Mitsubishi Gas Chemical Co Inc
Original Assignee
Mitsubishi Gas Chemical Co Inc
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 Mitsubishi Gas Chemical Co Inc filed Critical Mitsubishi Gas Chemical Co Inc
Priority to JP11964081A priority Critical patent/JPS5924085B2/en
Priority to US06/313,199 priority patent/US4416606A/en
Priority to DE3141993A priority patent/DE3141993C2/en
Publication of JPS5820228A publication Critical patent/JPS5820228A/en
Publication of JPS5924085B2 publication Critical patent/JPS5924085B2/en
Expired legal-status Critical Current

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  • Glanulating (AREA)

Abstract

PURPOSE:To obtain a granular sodium percarbonate having a proper particle size, hardness and bulk specific gravity, by specifying blade shapes in the feed region, the kneading and mixing region and a breaking region of the screw of a granulator. CONSTITUTION:In the feed region of a granulator, two screws are formed by succeedingly sending trapezoid screw blades 3 to send a material into said feed region and, in the first half of the kneading and mixing region, one screw is formed from a succeedingly sending ribbon like screw blade 4 and the other screw is formed from a reversely sending fragmentary twisted screw blade 5 as well as, in the latter half thereof, both screws are formed from reversely sending trapezoid blades 6. In the breaking region, protruded teeth 7 are attached to both screw shafts to break a small amount of agglomerated particles in granules. When sodium percarbonate is granulated by this granulator, a granular substance with a proper particle size, hardness, bulk density and solubility is obtained without carrying out special pretreatment.

Description

【発明の詳細な説明】 本発明ns粉体を■潤状態で連続的に混練、!!印して
一粒状に造粒する混練、I!和造粒機及び造粒方法に調
し、轡に粉体状の過炭酸ソーダを顆粒状に造粒するに好
適な造粒機に係る◎過炭酸ソーダは炭酸ソーダと過酸化
水素とを反応させることにより容易に得られ、漂白剤勢
として用いられている。過炭酸ソーダの粉末は飛散する
と鼻を刺歇するため職扱い上好ましくなく、また黴幹末
てけ長期間に亘って保存した場合固結し易く、サラサラ
した状態を保持することは極めてiiIm″t”1hる
◎また、過炭酸ソーダは湿気に対して不安定″r!あり
、湿気により含有している活性酸素の含有率が低下し易
(、湿気との接触面積を小さくすることが望ましいこと
、などbら一般に顆粒状に造粒されている〇従来、過炭
酸ソーダの造粒には、周知のニーダ−により適当な結合
剤勢の添加剤及び水の存在下Kflh線、控匍後、多孔
板すら押出す押出造粒機、あるいはへンシェルミキサー
IIJi#式め造粒機などが一般に用411られている
[Detailed Description of the Invention] The ns powder of the present invention is kneaded continuously in a wet state! ! Kneading by marking and granulating into one grain, I! A granulator suitable for granulating powdered soda percarbonate into granules using a Japanese granulator and granulation method. ◎Soda percarbonate is made by reacting soda carbonate and hydrogen peroxide. It is easily obtained by drying and is used as a bleaching agent. Soda percarbonate powder stings the nose if it scatters, making it undesirable for work.Also, it is easy to solidify when stored for a long period of time, and it is extremely difficult to maintain it in a dry state. 1 hour◎Also, soda percarbonate is unstable to moisture.The content of active oxygen in it tends to decrease due to moisture (and it is desirable to reduce the area of contact with moisture). , etc. are generally granulated into granules. Conventionally, soda percarbonate is granulated using a well-known kneader in the presence of an appropriate binder additive and water, Kflh wire, quenching, An extrusion granulator that extrudes even a perforated plate, a Henschel mixer IIJi # type granulator, etc. are generally used.

しふしながら、上記の多孔板ふら押出す押出造粒方法は
比較的形状の揃った造粒品が得られるが、得られる造粒
品は硬く、會た多孔板の孔径の制約すら粒子は大台(水
に対する溶解速度が遅い。さらに多孔板の孔が目詰りし
易く、このために多孔板の取り換えを頻繁に行なう必要
があるなど連続運転を行なうことが111mて島るなど
の欠点がある0また、へンシエルミキサー型形式の造粒
機は、短時間に造粒が行なわれ、摩擦熱も少ないなどの
長所がある反面、造粒された粒子は軟tI)<、脆く、
輸送中に破砕され易く、また嵩比重が小さいなどの欠点
があるロ一方、混錬、押粕する装置として、容器内に互
いkThみ合って回転する二本のスクリューを備え、材
料を連続的に混練、!!和する装置が種々知られている
。この全知の装置により過炭酸ソーダの造粒を行なって
も、粒、子の粒度、硬さ、嵩比重、及び溶解速R勢のい
ずれをも十分、に満足する粒子を得ることができない〇 本発明はこの様な種々の欠点に鎌みなされたものであっ
て、本発明の造粒機は一供給する過炭酸ソーダ粉を格別
な前処理を行なうことなく、一段て連続的に混練、袢和
、造粒を行なうことが?きると共に%得られる粒子の粒
度、硬さ、嵩比重及び水に対する溶解速度等いずれkも
十分に満足てきる顆粒状過炭酸ソーダを調造する造粒機
及び造粒方法を提供するものである・すなわち本発明は
、容器内に互いkThみ合って1転する二本のスクリュ
ーが並設されて怠り、該容器の一端には上方に開口する
材料投入口が、他端には下方に開口する吐出口がそれぞ
れ設けられ、容!上面kcは押え蓋を設けた押え蓋形式
の混練、te造粒機であって、該7造粒機はフィード域
、混線!!和域及び解砕域とbらなり、前記フィード域
は二本のスクリュー共に履送りの台形状のスクリューブ
レードが形成され、前記混線!!和域は、一方のスクリ
ューが逆送りのスクリューブレード虻、対応する他方・
1履送りのスクリューブレードにそれぞれ形成されてお
り、bつ逆送りのスフ1ニーブレードは断片履のねじれ
を持ったスフ11ニーブレードであり、履送りのブレー
ドはリボン状羽II形であり、これらが交互(なる如く
少なくとも二個新設けられた前半部と、二本のスクリュ
ー共に逆送りの台形状のスクリューブレードとされた後
半部とbらなり、前記解砕域は相方共和スクリュー軸に
複数本の5I!起状の解砕歯が設けられており、容器の
押え蓋は前記フィード域及び混練箆匍域の前記の前半部
に相当する部位は同定l[が、混錬控粕域の#記の後半
11128mする部位は上下に可動可能な押え蓋が職付
けられており、曽記解砕域は開放された構造すらなる造
粒機に関し、さらに、該造粒様の前記材料投入口よりJ
[s過炭酸ソーダ粉、添加剤及び水を供給し、混線、捏
和、造粒させ、吐出口すら造粒物を排出させることわら
なる過炭酸ソーダの造粒法に関する〇本発明を添付した
図INkより′具体的Ic1I!明する。第1図は、本
発明に係る造粒機の一何を示す横断千聞図を、第2II
Iけ縦断側面図を、第3111線第2IIlのムー人断
iitrmをそれぞれ示す・図面忙右いて、1は造粒機
の容器、2はスクリュー軸、Sは履送り台形状のスクリ
ューブレード、4瞠履送りの9ボン状羽根形のスクリュ
ーブレード、Sは断片履のねじれを持った逆送りスクリ
ュープレー〆、6は逆送りの台形状のスクリューブレー
V、 7は解砕歯、8は材料投入口、・け吐出口、10
は固定式押え蓋、11け可動式押え叢、12,13及び
14は冷却水の導入又は排出口、をそれぞれ示す@ 本発明の造粒機は添付しt−図面に示すようにフィード
域i、協練、!!和域璽及び解砕域菖と力)ら構成され
ている・夏のフィード域は二本のスクリュー共に履送り
の台形状のスフ1シユーブレード8が形成8れて詣り、
材料の送り込みが行なわれる・璽の混練、複相域は、一
方のスクリューブレードは履送りのリボン状の羽根形の
プレーP虻形威8れ、対応する他方のスクリューブレー
ドは逆送りでbつ断片曹のねじれを持つたスクリューブ
レード6か形成されて詣り、これらが交互忙なる様に配
設された鎗半部璽1と、二本のスクリュ、−共和逆送り
の台形状のブレード6が形成された後半s12とふらな
り、該帯域で材料の混線、!!和が十分に行なわれると
共に造粒される。そして1の解砕域番士相方共スクリュ
ー軸に央起状の解砕*7が複数本取り付けられて怠り、
#域に送り込!れた造粒物が若干凝集しているのを解砕
する。
However, although the extrusion granulation method of extruding through a perforated plate described above yields a granulated product with a relatively uniform shape, the resulting granulated product is hard, and even with the restriction of the pore size of the perforated plate, the particles are large. (The dissolution rate in water is slow. Furthermore, the holes in the perforated plate are easily clogged, which necessitates frequent replacement of the perforated plate, and there are disadvantages such as the need for continuous operation. 0 In addition, the Henschel mixer type granulator has the advantages of granulating in a short time and generating less frictional heat, but on the other hand, the granulated particles are soft and brittle.
On the other hand, as a kneading and lees-pressing device, two screws that rotate in tandem with each other are installed in the container to continuously feed the materials. Knead it! ! Various devices are known that perform summation. Even if soda percarbonate is granulated using this omniscient device, it is not possible to obtain particles that satisfy all of the particle size, hardness, bulk specific gravity, and dissolution rate R. The invention has been made to address these various drawbacks, and the granulator of the present invention is capable of continuously kneading and granulating the supplied sodium percarbonate powder without any special pretreatment. Is it possible to perform granulation? To provide a granulator and a granulation method for preparing granular soda percarbonate which is fully satisfactory in terms of particle size, hardness, bulk specific gravity, dissolution rate in water, etc.・In other words, in the present invention, two screws that rotate once are arranged in parallel in a container, and one end of the container has a material input port that opens upward, and the other end has a material input port that opens downward. Each outlet is provided with a discharge port, which allows the volume to flow! The upper surface KC is a presser lid-type kneading and TE granulator equipped with a presser lid, and the 7 granulators are in the feed area and cross line! ! The feeding area is divided into a merging area and a crushing area, and the feed area is formed with trapezoidal screw blades for feeding both screws, and the above-mentioned crosstalk! ! In the Japanese area, one screw has a reverse-feeding screw blade, and the other screw has a reverse feed.
They are each formed on a screw blade with one shoe feed, and the second reverse feed 1 knee blade is a second 11 knee blade with the twist of a single shoe, and the shoe feed blade is a ribbon-shaped feather II type. These are arranged alternately (at least two new front half parts and a second half part where both screws have trapezoidal screw blades that feed in opposite directions), and the crushing area is connected to the shaft of the companion screw. A plurality of 5I!-shaped crushing teeth are provided, and the holding lid of the container corresponds to the aforementioned front half of the feed area and the kneading lees area. The second half of ## is equipped with a presser lid that can move up and down, and the Zeng crushing area is connected to a granulator with an open structure, and the material input for granulation is J from the mouth
[s] This invention relates to a method for granulating soda percarbonate, which involves supplying soda percarbonate powder, additives, and water, mixing, kneading, granulating, and discharging the granules even from the discharge port. From figure INk'specific Ic1I! I will clarify. FIG.
A vertical cross-sectional side view of I is shown, and a cross-sectional view of IITRM of No. 2 II on line 3111 is shown.In the drawings, 1 is the container of the granulator, 2 is the screw shaft, S is the track-shaped screw blade, 4 9 Bon-shaped vane-shaped screw blade with ball feed, S is a reverse feed screw play with a twist of a single shoe, 6 is a trapezoidal screw blade V with reverse feed, 7 is a crushing tooth, 8 is a material input Mouth, outlet, 10
1 shows a fixed presser lid, 11 movable pressers, and 12, 13, and 14 cooling water inlet or outlet ports, respectively. , Collaboration! !・The summer feed area consists of two screws, each of which has a trapezoidal shape 1 and a shoe blade 8.
In the multi-phase area where the material is fed and kneaded, one screw blade is fed with a ribbon-like blade-shaped play P, and the corresponding other screw blade is fed in reverse. A screw blade 6 with a screw blade 6 is formed and arranged so that these blades are arranged alternately, and two screws, a trapezoidal blade 6 with a reverse feed. The formed second half s12 and the material crosstalk in the band,! ! After sufficient summation, the mixture is granulated. Then, both the crushing area guard and the crushing area number 1 were neglected because multiple central-shaped crushers *7 were attached to the screw shaft.
# Send it to the area! The slightly agglomerated granules are broken up.

本発明の造粒機は、フィード域及び混練、控和域のスク
リューブレードが、願送り、断片履逆送り、リボン状羽
S形の履送り、及び逆送りのブレードに形成されて参り
、bつこれらを上記の様虻配設すること虻よってフィー
ド域!bら送り込蒙れた材料は混練、ll和域厘虻おい
て順送りの台形状のブレードによる送り及びねじれを持
ったブレード及び台形状の逆送りブレード化よる戻りの
作用により十分なる混線及び控和が行なわれτ造粒され
る0造粒物けフィード域すらの送りの力と二本のスクリ
ュー共虻、逆送りのブレードに形成された前記の混線、
複相域の後半部に7右ける逆送りの力とが適mにバラン
スされて適宜解砕域MIC送り出されて来る。解砕域に
送り出される造粒物は、通常、若干凝集LTkす、また
若干チキントロピー性を有シている◎皺解砕域て・を凝
集物を解砕すると同時虻チキントOビー性の解放がなさ
れるが、この目的を十分忙達威するkは、該解砕域虻右
いて造粒物を一定時間滞1lI8せ一種の攪拌が行なわ
れるようにすることが望ましい@この作用を効果的に行
なわせる虻は、たとえば、解砕域における造粒物の入す
側、すなわち混練、!!和域の後半部12側の解砕歯は
、造粒物が幾分逆送りkなるm虻若干角度を設けた羽根
状の彫状とすると6%解砕歯め取り付は本数を解砕域に
おける造粒物の入口側と出口側とで異ならせ、入口側を
1flc出口側を粗に設ける等が好適な一つの態様であ
る・該解砕域の構造は上記したもの忙特定される訳てな
く、混練、複相域すら送り出される材料の状1111y
より適宜決められ、たとえば、P相方が比較的弱い粒子
の場合には解砕機能を主体とする様な棒状の突起とする
ことができ、逆K11l)’!力が強い粒子の場合は主
にチキントロピー性を解放する機能をもたせる11に送
り羽根状の突起とすることがてきる。
In the granulator of the present invention, the screw blades in the feed zone, kneading, and attenuation zone are formed into blades for continuous feeding, reverse feeding for fragments, S-shaped ribbon feeding, and reverse feeding blades, and b Place these in the above-mentioned manner to feed the flies! The materials fed from the above are kneaded, and the material is thoroughly mixed and suppressed by the feeding action of a progressively feeding trapezoidal blade and the return action of a twisted blade and a trapezoidal reverse feeding blade. The feeding force even in the zero granulation feed area where summation is carried out and τ granulation is carried out, the two screws collide, and the above-mentioned crosstalk formed in the blade of reverse feeding,
The reverse feed force applied to the latter half of the multi-phase area is appropriately balanced and sent to the crushing area MIC as appropriate. The granules sent to the crushing zone usually have some agglomeration and some chicken tropism. When the aggregates are crushed in the wrinkle crushing zone, the granules are released at the same time. However, in order to fully accomplish this purpose, it is desirable to leave the granules in the crushing zone for a certain period of time and to perform a kind of agitation. For example, the horseflies that are made to do this are on the side where the granules are input in the crushing area, that is, kneading! ! The crushing teeth on the 12 side of the rear half of the area are shaped like wings with a slight angle so that the granules are fed slightly backwards. One preferred embodiment is to make the inlet and outlet sides of the granules different in the area, and to roughly provide the inlet side with 1 flc and the outlet side.The structure of the crushing area is as specified above. The condition of the material that is kneaded and even sent out in the multi-phase region is 1111y.
For example, if the P partner is a relatively weak particle, it can be a rod-shaped protrusion that mainly has a crushing function, and the opposite K11l)'! In the case of particles with strong force, a feather-like protrusion can be used to feed the particle 11, which mainly has the function of releasing chicken tropism.

また、本発明の造粒機においては、混練、痙和域の後半
部12 K相当する部位忙は上下に可動可能な押え蓋を
設け、(Jも該蓋は前記後半部璽2の逆送りの台形状の
スクリューブレードの全部を蓋することなく出口側が若
干解放状態になっている。この様な構造とするととくよ
り、複相力が強く嵩比重の比較的大きい造粒物を得たい
場合にはり可動可能な押え蓋を若干下げればよく、逆に
複相力が比較的弱く、嵩比重の小さい造粒物を得たい場
合には可動可能な押え蓋を若干上げる機忙調節すればよ
い。また、逆送りの台形状のスクリューブレードの全部
を蓋することなく、出口側が若干解放状態となっている
こと虻より、押出される造粒物の団塊状のものをある程
度はぐすことがてきる。
In addition, in the granulator of the present invention, a part corresponding to the rear part 12K of the kneading and spasticity area is provided with a presser lid that is movable up and down (J also has a presser lid that can be moved in the reverse direction of the rear part 2). The trapezoidal screw blade is not entirely covered and the outlet side is left slightly open.Such a structure is especially useful when you want to obtain a granulated product with strong multiphase force and relatively large bulk specific gravity. It is sufficient to slightly lower the movable presser foot lid, and conversely, if the multiphase force is relatively weak and you want to obtain a granulated product with a small bulk specific gravity, you may adjust the mechanism by slightly raising the movable presser foot lid. In addition, since the trapezoidal screw blade of the reverse feed is not completely covered and the outlet side is slightly open, it is possible to remove some of the nodules of the extruded granules. Ru.

本発明の造粒機は冷却を必要とする場合忙は造粒機容器
の外套及びスクリュー軸内の所定の導管虻冷却水を通す
ことができる。本発明の造粒積和より過炭酸ソーダ粉を
造粒する際の条件は、造粒機の大会さ、能力、原料過炭
酸ソーダ粉の粒度、水分、添加剤のs#All1kcよ
り異なり一義的に決めることはてきないが、たとえば、
スクリュー羽根の11270m、トップ全長2400w
M1スクνユ−回転数40〜80 r、p、mで原料の
供給量は700〜2000ゆ/ h r 、で島る0ま
た、添加剤、水の添加量は造粒物の含水率を10〜16
9@度虻する様に原料過炭酸ソーダ粉の含水量、添加剤
の種類など虻より決められる◎ 本発明の造粒様により造粒された造粒物は、吐出口9よ
り排出され、次いて高速回転するナイフカッターを備え
た整粒機により整粒したの( ち、乾燥され製品とされる。該整粒機は二枚羽根状のナ
イフカッターが回転輪に適当な間隔を設けて8〜12枚
重ねて取り付けられ、長さ25〜15011mの造粒物
投入用ホッパーか設けられた蓋を有するが、底のない円
筒状の11112、刃の先端と前記円筒の内壁との閲K
ffiThな間隙を設けて、配置された構造ムらなり、
該ナイフカッターは1000〜4000 r、pomて
高速1転される。ナイフカッター数が同じ場合、1転数
が速く鉤記円筒状の容器の長さが長い程平均粒径は小さ
くなる。たとえば円筒状容器の長8が25wてナイフカ
ッターの数が8枚で、回転数が400 Or、pom 
 の場合忙醤を得られる粒子の平均径は410jIてあ
り、円筒状容器の長さが15010(r)ときは、得ら
れる平均粒vkは430#″′e島る。また円筒状容器
の長さが同じて、回転数が同じであると会、ナイフカッ
ターの数を増すと平均粒径は小さくなる傾向(島る0た
とえば、回転数4000 r、p、mて、円筒状の容器
の長さが1506のと会、ナイフカッターの数−t−1
2&としたときは平均粒径は340μである0 本発明の方法により得られる造粒されたlIR晶の諸物
性のうち、粒子の嵩比重、硬さ、溶解速度などは主とし
て造粒機IIC右いて造粒される際の混練、控匍の状態
が影響し、粒度は整粒様の条件忙より決まる。
When the granulator of the present invention requires cooling, cooling water can be passed through designated conduits in the jacket of the granulator vessel and in the screw shaft. The conditions for granulating soda percarbonate powder using the granulation product of the present invention are uniquely different from the size and capacity of the granulator, the particle size of the raw material soda powder, water content, and the s#All1kc of additives. Although it is not possible to decide, for example,
Screw blade 11270m, total top length 2400w
M1 screw rotation speed is 40 to 80 r, p, m, raw material supply rate is 700 to 2000 y/hr, and the amount of additive and water added depends on the water content of the granules. 10-16
◎ The granulated material granulated by the granulation method of the present invention is discharged from the discharge port 9, and then The granules are sized using a sizing machine equipped with a knife cutter that rotates at high speed. ~ 12 sheets are stacked and have a lid equipped with a hopper for introducing granules with a length of 25 to 15011 m, but the cylindrical shape 11112 has no bottom, and there is no visibility between the tip of the blade and the inner wall of the cylinder.
The structure is arranged with ffiTh gaps,
The knife cutter is rotated at a high speed of 1000 to 4000 rpm. When the number of knife cutters is the same, the faster the number of revolutions per rotation and the longer the length of the hooked cylindrical container, the smaller the average particle diameter. For example, the length of the cylindrical container is 25W, the number of knife cutters is 8, and the rotation speed is 400 Or, pom.
In this case, the average diameter of the particles obtained is 410jI, and when the length of the cylindrical container is 15010(r), the average particle diameter vk obtained is 430#'''e. For example, when the number of knife cutters is the same and the number of rotations is the same, the average particle size tends to become smaller as the number of knife cutters increases. Saga 1506 meeting, number of knife cutters-t-1
When 2&, the average particle size is 340μ.0 Of the various physical properties of the granulated lIR crystal obtained by the method of the present invention, the bulk specific gravity, hardness, dissolution rate, etc. of the particles are mainly determined by the granulator IIC. It is affected by the conditions of kneading and holding during granulation, and the particle size is determined by the granulation conditions.

「 五 ) 8〜10嘩の原料過炭酸ソーダを材料投入ロアより20
kl/hr9、添加剤としてメタケイ酸ソーダ15@溶
il(バインダー水)  2 J / h r 。
5) Add 8 to 10 liters of raw material soda percarbonate to 20 liters from the material input lower.
kl/hr9, sodium metasilicate 15@dissolved (binder water) 2 J/hr as an additive.

を供給した0スクリユーの回転速度80 r、p、ms
可動押え蓋1oの高さを6wlに調節して混練、I!印
造粒を行なった◎なお、容器の外套及びスクリュー軸内
の導管忙冷却水を通した。運転開始1時間後ふら安定し
た造粒物が得られた。次いで得られた造粒物を400 
Or、p、mで回転するナイフカッターを備えた円筒の
長さ1508mの整粒機忙より整粒したのち、乾燥し、
製品を得た0製品の諸物性・1下記の通りであった。
The rotational speed of the screw that supplied 80 r, p, ms
Adjust the height of the movable presser foot lid 1o to 6wl and knead, I! Mark granulation was performed. ◎ Cooling water was passed through the conduit inside the container jacket and screw shaft. One hour after the start of operation, a stable granulated product was obtained. Then, the obtained granules were heated to 400
After sizing using a cylindrical sizing machine with a length of 1508 m equipped with a knife cutter that rotates at Or, p, and m, it is dried.
The physical properties of the obtained product were as follows.

比較例 m1llのへ/シェルミキサー製形式の造粒機を使用し
た0該造粒様に実施例と同様の原料過炭酸ソーダ粉体を
20kg導入し、メタケイ酸ソーダ15−溶ml(バイ
ンダー水) 2Jを加えて3分間控匍造粒L1得られた
造粒物を実施例と同様の整粒機により整粒し1乾燥−1
で1J1品を得た。この製品の諸物性は下記の通りであ
り、溶解速度は極めて速いが、粒子の嵩比重が小さく強
度が―いことが咽らbてあ・るOこれは製品として十分
満足できない。
Comparative Example A shell mixer type granulator was used for 1 ml. 20 kg of the same raw material soda percarbonate powder as in the example was introduced into the granulation method, and 15 ml of sodium metasilicate solution (binder water) was added. Add 2J and hold for 3 minutes to granulate L1 The obtained granules were sized using the same granulating machine as in Example 1 Dry-1
I got one item from 1J. The physical properties of this product are as follows: Although the dissolution rate is extremely fast, the bulk specific gravity of the particles is small and the strength is poor, which is not fully satisfactory as a product.

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

第1図は本発明の造粒機の横断平面図、第2図は縦断側
面図、第3図は第2図のムー人断面図をそれぞれ示す。 1−容器、  2−スクリュー軸、 3−順送り台形状のスクリューブレード、4−順送りリ
ボン状羽根形スクリューブレード、6−断片型のねじれ
を持ったスクリューブレード、6・−逆送り台形状のス
クリューブレード、7−・解砕歯、1o−固定式押え蓋
11−可動式押え蓋 特許出願人 三菱瓦斯化学株式会社 代表者長野和吉
FIG. 1 is a cross-sectional plan view of the granulator of the present invention, FIG. 2 is a longitudinal side view, and FIG. 3 is a cross-sectional view of the granulator of the present invention. 1 - container, 2 - screw shaft, 3 - progressive trapezoidal screw blade, 4 - progressive ribbon vane screw blade, 6 - screw blade with piecemeal twist, 6 - reverse trapezoidal screw blade , 7--Crushing teeth, 1o-Fixed presser cover 11-Movable presser cover Patent applicant Kazuyoshi Nagano, representative of Mitsubishi Gas Chemical Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] (1)容器内に互いKThみ台って回転する二本のスク
!ニーが並設され讐怠り、該容器の一端には上方<、S
Oする材料投入口が、他端には下方に開口する吐出口が
それぞれ−けられ、容器上面には押え−を設けた押えl
lI形式の混線、I!倉造粒機てあって、該造粒機はフ
ィード域、混練!旬域及び解砕域とb−らなり、鍵記フ
ィーr域は二本のスクリュー共に願融すの台形波のスク
リューブレードが形成され、―記拠練1!1111域は
、一方のスクリューが逆送りのスクリューブレードに、
対応する他方は履送りのスクリューブレードにそれぞれ
彫威されて怠り、bつ逆送りのスクリューブレードは断
片履のねじれを持ったスクリュー共”し”−ドて島り、
原送りのブレード線リボン状羽根形てあり、これらが交
互になる如く少なくとも二個次設けられた前半部と、二
本のスクリュー共に逆送りめ台形状のスフ1フユーブレ
ードとされた後学部とbらなり、前記解砕域は相方共に
スクリュー軸に複数本の央起状の解砕歯が設けられてお
り、容器の押え蓋は前記フィード域及び混練控和域の前
記の前半部に軸当する部位は固定蓋が、混練控和域の前
記の後半部に相当する部位は可動可能な押え蓋が職付け
られており、前記解砕域は開放された構造すらなる造粒
機 (21容器内に互いKThみ合って同転する二本のスク
リ且−が並設されており、該容器の一端には上方に開口
する材料投χ口が、他端には下方に開口する吐出口がそ
れぞれ設けられ、容器上面には押え蓋を設けた押え蓋形
式の混 “練I?!相造粒機であって、該造粒機はフィ
ード域、混練I!和域及び解砕域とbらなり、前記フィ
ード域は二本のスクリュー共に履送りの台形状のスクリ
ューブレードが形成され、前記混練複相域は、一方のス
クリューが逆送りのスクリューブレードに、対応する他
方は順送りのスクリューブレードにそれぞれ形成されて
おり、bつ逆送りのスクリューブレードは断片製のねじ
れを持ったスクリューブレードてあり、頴送りのブレー
ドはリボン状羽根形であり、これらが交互になる如く少
なくとも二個次設けられた前半部と、二本のスクリュー
共に逆送りの台形状のスクリューブレードとされた後半
部とカーらなり、前記解砕域は相方共にスクリュー軸に
複数本の央起状の解砕歯が設けられており、容器の押え
蓋は前記フィード域及び混練複相域の前記の前半部に相
当する部位は固定蓋が、混線複相域の前記の後半部に相
当する部位は上下に可動可能な押え蓋が亀付けられて参
り、前記解砕域は開ミ 放された構造ムらなる造粒機を使用し、該造粒域の前記
材料投入口より過炭酸ソーダ粉、添加剤及び水を供給し
、混練複相造粒させ、吐出口より造粒物を排出させるこ
とを特徴とする過炭酸ソーダの造粒方法
(1) Two scrolls that rotate with each other in the container! knees are arranged side by side, and one end of the container has an upper <, S
A presser foot is provided on the upper surface of the container, with a material input port opening downward and a discharge port opening downward at the other end.
Interference in lI format, I! There is a warehouse granulator, the granulator has a feed area, a kneading area! It has a shape of 1.1 and 1.2, and a trapezoidal wave screw blade is formed in the key record field and the crushing region. On the reverse-feeding screw blade,
The corresponding other screw blades are carved by the screw blades of the forward feed, and the two screw blades of the reverse feed are carved and the screws with the torsion of the backward feed are both ``shi'' - deformed.
The blade wire has a ribbon-like blade shape of the original feed, and the front part is provided in at least two parts so that these are alternately arranged, and the rear part is made of two screws that are both reverse-feeding trapezoidal blades. Both of the crushing zones are provided with a plurality of central crushing teeth on the screw shaft, and the presser lid of the container is in shaft abutment with the front half of the feed zone and the kneading restraint zone. A fixed lid is installed in the area where the kneading is carried out, a movable presser lid is installed in the area corresponding to the latter half of the kneading and holding area, and the crushing area is equipped with a granulator with an open structure (21 containers). There are two screws arranged side by side inside the container that rotate in parallel with each other, and one end of the container has a material injection port that opens upward, and the other end has a discharge port that opens downward. It is a kneading-I phase granulator in the form of a presser lid with a presser lid on the upper surface of the container. In the feed region, both screws have trapezoidal screw blades, and in the kneading multi-phase region, one screw has a backward-feeding screw blade, and the other screw has a forward-feeding screw blade. The two reverse screw blades are screw blades with a fragmentary twist, and the two screw blades are ribbon-shaped blades, and at least two screw blades are provided so that these blades are alternately arranged. The first half of the two screws are shaped like trapezoidal screw blades, and the second half has trapezoidal screw blades that feed in opposite directions. The holding lid of the container is fixed at the portion corresponding to the first half of the feed region and the kneading multi-phase region, and is movable up and down at the portion corresponding to the latter half of the cross-conducting multi-phase region. Using a granulator with a structure in which the crushing area is open and the presser lid is attached, soda percarbonate powder, additives, and water are introduced from the material input port of the granulating area. A method for granulating soda percarbonate, which comprises: supplying sodium percarbonate, kneading and multi-phase granulation, and discharging the granules from a discharge port.
JP11964081A 1980-10-22 1981-07-30 Granulator for soda percarbonate Expired JPS5924085B2 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP11964081A JPS5924085B2 (en) 1981-07-30 1981-07-30 Granulator for soda percarbonate
US06/313,199 US4416606A (en) 1980-10-22 1981-10-20 Apparatus for granulating sodium percarbonate
DE3141993A DE3141993C2 (en) 1980-10-22 1981-10-22 Device for granulating sodium percarbonate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11964081A JPS5924085B2 (en) 1981-07-30 1981-07-30 Granulator for soda percarbonate

Publications (2)

Publication Number Publication Date
JPS5820228A true JPS5820228A (en) 1983-02-05
JPS5924085B2 JPS5924085B2 (en) 1984-06-07

Family

ID=14766447

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11964081A Expired JPS5924085B2 (en) 1980-10-22 1981-07-30 Granulator for soda percarbonate

Country Status (1)

Country Link
JP (1) JPS5924085B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108940122A (en) * 2018-08-10 2018-12-07 明毅强 A kind of granulation device of health food processing
CN110919813A (en) * 2019-11-29 2020-03-27 景德镇陶瓷大学 Spiral-hemisphere branch combined intelligent silicon nitride dry granulation integrated device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108940122A (en) * 2018-08-10 2018-12-07 明毅强 A kind of granulation device of health food processing
CN110919813A (en) * 2019-11-29 2020-03-27 景德镇陶瓷大学 Spiral-hemisphere branch combined intelligent silicon nitride dry granulation integrated device

Also Published As

Publication number Publication date
JPS5924085B2 (en) 1984-06-07

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