JPS62121634A - Method and apparatus for spray type granulation of heat-meltable substance - Google Patents

Method and apparatus for spray type granulation of heat-meltable substance

Info

Publication number
JPS62121634A
JPS62121634A JP8520685A JP8520685A JPS62121634A JP S62121634 A JPS62121634 A JP S62121634A JP 8520685 A JP8520685 A JP 8520685A JP 8520685 A JP8520685 A JP 8520685A JP S62121634 A JPS62121634 A JP S62121634A
Authority
JP
Japan
Prior art keywords
spray
heat
particles
melting
spray patterns
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
JP8520685A
Other languages
Japanese (ja)
Other versions
JPH06185B2 (en
Inventor
Masabumi Matsunaga
正文 松永
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.)
Nordson KK
Original Assignee
Nordson KK
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 Nordson KK filed Critical Nordson KK
Priority to JP8520685A priority Critical patent/JPH06185B2/en
Publication of JPS62121634A publication Critical patent/JPS62121634A/en
Publication of JPH06185B2 publication Critical patent/JPH06185B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE:To prepare particles having a perfectly globular shape with good yield, by attracting particles formed by spraying to the central part of a spray pattern by line of electric force generated by voltage applied to the electrostatic charging electrode provided to the intermediate part of a jet group. CONSTITUTION:A heat-meltable substance F is injected and sprayed in a solid state by respectively operating electric or pneumatic type valves 3, 4. Because two spray patterns SA, SB are respectively directed outwardly, they do not cross or overlap. However, if voltage is applied to an electrode, line of electric force is generated and a large number of particles of the heat-meltable substance in the spray patterns are attracted to the center (Pa Pa', Pb Pb') by said line of electric force to be penetrated between two fan-shaped spray patterns SA, SB. That is, said particles fill the gap between the spray patterns SA, SB.

Description

【発明の詳細な説明】 従来、熱溶融性物質のスプレィによる造粒方法は・二流
体スプレィ又はエアレススプレィ等によ又は水によって
冷却し、固化し、球状の粒子を製造していた。その場合
、上述のスプレィされ互の間隙を拡げるため、出来得る
限りスプレィパターンを拡大して粒子相互間の距離をあ
ける必要があり、それに沿って設計された噴出口が用い
られてきた。しかし、その噴出口だけによるスプレィパ
ターンの拡大拡張にも限度があり、矢張り互着発生を十
分に防ぐことは出来なかった。本発明の動機は、噴出口
設計以外の手段をもって、これら互着発生を完全に防止
することであった。
DETAILED DESCRIPTION OF THE INVENTION Conventionally, the method of granulating a hot melt material by spraying is to produce spherical particles by cooling and solidifying by two-fluid spray, airless spray, etc. or by water. In this case, in order to widen the above-mentioned gaps between the sprayed particles, it is necessary to enlarge the spray pattern as much as possible to increase the distance between the particles, and jet ports designed in accordance with this have been used. However, there is a limit to the expansion and expansion of the spray pattern using only the spout, and it has not been possible to sufficiently prevent the occurrence of mutual sticking. The motive of the present invention was to completely prevent these occurrences of mutual sticking by means other than the nozzle design.

本発明の目的は、熱溶融性物質のスプレィ式造粒法にお
いて、スプレィパターンをより拡大し、粒子相互間の互
着を防いで完全球形の粒子歩溜り良く製造する製造する
方法を提供するものである。
An object of the present invention is to provide a method of manufacturing perfectly spherical particles with a good yield by expanding the spray pattern and preventing mutual adhesion of particles in a spray granulation method for heat-melting substances. It is.

そもそも本発明は、本出願人による昭和60年6月6θ
日付特許出願[粉体塗料のスプレィパターンの形成方法
とそのスプレィ装置」及び同じく昭和60年4月 日付
特許出願「流動体のスプレィパターンの形成方法とその
スプレィ装置」の両発明を基としたものであり、その後
の実験により、上記以外の対象物即ち熱溶融性物質の造
粒方法に対しても別種の効果のあることを発見し、改め
て出願するに至ったものである。
In the first place, the present invention was developed by the applicant in June 1985.
This invention is based on the inventions of the patent application dated April 1988, ``Method for forming a spray pattern of powder coating and its spraying device,'' and the same patent application dated April 1985, ``Method of forming a spray pattern of fluid, and its spraying device.'' Through subsequent experiments, it was discovered that there is a different type of effect on granulation methods for objects other than those mentioned above, that is, heat-fusible substances, and this led to the filing of a new application.

本発明の要旨を述べると、熱溶融性物質の溶融体を、複
数箇の噴出口より、これら噴出口が互いにある必要な角
度をもってスプレィパターンが重複しないようにスプレ
ィせしめ、かつこれらスプレィ中の粒子を、上記複数箇
の噴出口群のはゾ中間部に設けられた静電気荷電用電極
への電圧印荷によって発生した電気力線により、上記分
散した複数箇のスプレィパターンの中間部に引き寄せ、
それによってスプレィパターン全体をより拡大し、粒子
分布を均一化し、かつ粒子相互の間隙をあけ、粒子間の
互着を未然に防ぐ方法である。
The gist of the present invention is to spray a molten body of a heat-fusible substance from a plurality of jet ports at a necessary angle to each other so that the spray patterns do not overlap, and to spray particles in the spray. is drawn to the middle part of the plurality of dispersed spray patterns by electric lines of force generated by applying a voltage to the electrostatic charging electrode provided at the middle part of the plurality of jet nozzle groups,
This is a method of expanding the entire spray pattern, making the particle distribution more uniform, and creating gaps between the particles to prevent particles from sticking together.

なお、本発明の対象とする熱溶融性物質とは熱溶融性の
天然及び合成の高分子を始めとし、これらと低分子との
混合物及び質量の比較的小なる低分子より成る各種の物
質である。また、作られる粒子の大きさは100ミクロ
ン前後及びそれ以下のものであり、それ以上のものの造
粒は困難である。
The heat-melting substances targeted by the present invention include heat-melting natural and synthetic polymers, mixtures of these with low molecules, and various substances consisting of low molecules with relatively small masses. be. Further, the size of the particles produced is around 100 microns or less, and it is difficult to granulate particles larger than that.

次に本発明による造粒方法について説明する。Next, the granulation method according to the present invention will be explained.

第1図を参照されたい。同図におけるスプレィ装置は、
前述の本出願人による昭和60年4月日付特許出願「流
動体のスプレィパターンの形成方法とそのスプレィ装置
」におけるスプレィ装置を利用したものである。即ち、
熱溶融体の噴出口8A、8Bは2箇以上とし、これらは
互いに外方に向けである必要角度をもってセットされて
いる。また、これら噴出口の中間部には静電気荷電用電
極10が備えられている。このような三筒の噴出口より
、熱溶融体Fは、電気又は空気式操作弁3,4の作動に
よって同時にそれぞれ噴出しスプレィされる。これらの
二本のスプレィSA、SBは、それぞれ上述の如く外方
に向けられているため、交叉したり重複することはない
。所が、上記の電極に電圧が印荷されると、電気力線が
発生し、それによって上記のスプレィ中の熱溶融性物質
の多くの粒子が中央の方に引き寄せられ(Pa−> P
a’ ; Pb−+ Pb’。
Please refer to FIG. The spray device in the same figure is
This invention utilizes the spray device described in the above-mentioned patent application filed in April 1985 by the present applicant entitled "Method for Forming Spray Pattern of Fluid and Spray Apparatus". That is,
There are two or more spout ports 8A and 8B for the hot melt, and these are set at a required angle toward each other outward. Furthermore, an electrostatic charging electrode 10 is provided in the middle of these jet ports. The hot molten material F is simultaneously ejected and sprayed from these three ejection ports by actuation of electric or pneumatic operation valves 3 and 4, respectively. Since these two sprays SA and SB are directed outward as described above, they do not intersect or overlap. However, when a voltage is applied to the above electrode, electric lines of force are generated, which pulls many particles of the hot melt substance in the above spray towards the center (Pa->P
a';Pb-+Pb'.

・・・・・・)上述の2本の扇状スプレィパターンSA
・SBの間に進入する。即ち二本のスプレィパターンS
A、SBの間を埋めるのである。言い換えると・双方の
スプレィパターンが拡大し、それらの粒子の分布密度が
小となり、粒子間隔が犬となって、粒子相互が近接して
互着するようなことはなくなるのである。
......) Two fan-shaped spray patterns SA mentioned above
・Enter between SB. That is, two spray patterns S
It fills in the space between A and SB. In other words, both spray patterns are expanded, the distribution density of the particles is reduced, and the spacing between the particles becomes narrow, so that the particles no longer stick together closely.

このような状態で凝縮し、球状となった多数の粒子は空
中を降下、その間自然冷却して球形の粒子となる。たゾ
し、その大きさは100ミクロン前後まであり、それ以
上大きく、しかも多量の造粒は困難である。理由は、粒
子が犬であると、当然重量が犬となり、電気力線による
吸引作用の効果が得難くなるからである。
A large number of spherical particles condense in this state and fall through the air, during which time they cool naturally and become spherical particles. However, their size is up to around 100 microns, and it is difficult to granulate larger amounts. The reason is that if the particle is a dog, its weight will naturally be a dog, and it will be difficult to obtain the effect of the suction action by electric lines of force.

なお、上述においては、スプレィ後の粒子の自然冷却を
述べたが、それが物質によって冷却不十分の場合、又は
粒子の生産が比較的多量の中に落すとか、若しくは、ス
プレィする雰囲気の温度を冷却器等によって下げる等の
手段が用る。本発明は更に冷却効果を上げるため、次の
冷却法を加える。
In addition, although the above mentioned natural cooling of the particles after spraying, if the cooling is insufficient due to the substance, or if the particles are produced in a relatively large amount, or if the temperature of the spraying atmosphere is Measures such as lowering the temperature using a cooler etc. are used. In order to further increase the cooling effect, the present invention adds the following cooling method.

即ち、上述した本発明によるスプレィを行なうスプレィ
室内に高圧液体ガスを噴出せしめる。
That is, high-pressure liquid gas is ejected into the spray chamber in which the above-described spray according to the present invention is performed.

例えば窒素ガス、炭酸ガス等である。これによって、ス
プレィされた熱溶融性物質の凝縮した粒子は、短時間に
冷却固化し、完全なる球形粒子となって、接触、外力等
による互着を完全に防止することが出来るのである。
For example, nitrogen gas, carbon dioxide gas, etc. As a result, the condensed particles of the sprayed heat-fusible substance are cooled and solidified in a short period of time, becoming perfectly spherical particles, completely preventing them from sticking to each other due to contact, external force, etc.

上記方法に基く構造を第2図に示す。先づスプレィ装置
は本出願人による昭和60年4月日付出願1流動体のス
プレィパターン形成方法とそのスプレィ装置」に記載さ
れたスプレィ装置である。即ち複数箇の噴出口18A、
18B  と静電気荷電用電極20を有するスプレィ装
置であり、該スプレィ装置は、その全周囲を包むスプレ
ィ室13の上方部に取付けられ、また該スプレィ室の下
方側壁側には高圧液化ガスの噴出口15.16が設けら
れ、図には示されていないが高圧液化ガスタンクへと接
続されている。また、該スプレィ室の底部には、造粒さ
れた粒子の移送装置が設けられる。同図にてはホッパー
19が示されているが、その他、シュート、コンベアな
ども取付けらる。
A structure based on the above method is shown in FIG. First, the spray device is a spray device described in Application No. 1 “Method for Forming Spray Patterns of Fluid and Spray Apparatus Therefor” dated April 1985 by the present applicant. That is, a plurality of spout ports 18A,
18B and an electrostatic charging electrode 20, the spray device is attached to the upper part of the spray chamber 13 that surrounds the entire periphery of the spray chamber 13, and has a high-pressure liquefied gas ejection port on the lower side wall side of the spray chamber. 15,16 are provided and are connected to a high pressure liquefied gas tank (not shown). A granulated particle transfer device is also provided at the bottom of the spray chamber. Although the hopper 19 is shown in the figure, other components such as a chute and a conveyor may also be attached.

なお、スプレィ装置としては、前述の如く、本出願人に
よる昭和60年4月 日付特許出願[流動体のスプレィ
パターン形成方法とそのスプレィ装置」の明細書中、特
許請求の範囲に記シーされた三種のスプレィ装置が適用
出来る。
In addition, as mentioned above, the spray device is as described in the claims in the specification of the patent application filed in April 1985 by the present applicant titled “Method for forming spray pattern of fluid and its spray device”. Three types of spray devices are applicable.

を取付けたものである。第二は、第3図に示す如く、噴
出器21.22と噴出口28A、28B との間に中間
アダプター20を設けたもの、第三は、第4図に示す如
く、−箇の吐出器31に対し複数箇の噴出口38A、3
8Bを設けたものである。
This is the one with the . The second type is one in which an intermediate adapter 20 is provided between the jets 21 and 22 and the jet ports 28A and 28B, as shown in FIG. 3, and the third one is as shown in FIG. 31, a plurality of spout ports 38A, 3
8B is provided.

なお上記の図は、何れも噴出ロ三筒の例を挙げたもので
あるが三筒以上取付けることも出来る。
Although the above figures show examples of three jetting cylinders, it is also possible to install three or more cylinders.

また、第6図及び第4図においては噴出口は固定式のも
のを示しであるが、これらを角度可変式の噴出口取付金
具を開設することによって、可動式とすることも出来る
Further, although FIGS. 6 and 4 show fixed jet outlets, they can also be made movable by providing angle-variable jet outlet fittings.

以上の如く、本発明の方法によれば、熱溶融性物質の加
熱溶融体を複数箇の噴出口よりスプレィ、同時に静電気
荷電用電極への電圧印荷によって、上記のスプレィによ
り作られた複数のスプレィパターンの空白部を埋め、ス
プレィパターンの範囲をより拡大することによって、ス
プレィ中の粒子相互の間隔を拡げ、粒子の互着を防いで
、球形粒子製造の歩溜り向上に寄与するものである。
As described above, according to the method of the present invention, a heated melt of a heat-fusible substance is sprayed from a plurality of jetting ports, and at the same time a voltage is applied to an electrostatic charging electrode, whereby a plurality of By filling in the blank areas of the spray pattern and further expanding the range of the spray pattern, the spacing between particles during spraying is increased, preventing particles from sticking to each other, and contributing to improving the yield of spherical particle production. .

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

第1図は本発明(以下すべて本発明につき省略)による
熱溶融性物質のスプレィによる造粒方法の説明図  第
2図は造粒装置の正面図第6図は同上用スプレィ装置の
中間アダプタ式のものの正面図  第4図は同上用スプ
レィ装置の一箇の吐出器に対し複数箇の噴出口を設けた
ものの正面図 主要な符号の説明 1.2.I+、12.21.22.@・・・・・・吐出
器 3゜4.23,24.33・・・・・・電磁操作弁
  5,6・・・・・・ヒンジ板  8A、8B、 1
8A、 18B、28A、28B。
Fig. 1 is an explanatory diagram of the granulation method by spraying a heat-melting substance according to the present invention (hereinafter all omitted for the present invention) Fig. 2 is a front view of the granulation device Fig. 6 is an intermediate adapter type of the spray device for the above Figure 4 is a front view of the same spray device as above, in which a single discharger is provided with a plurality of spout ports. Explanation of main symbols 1.2. I+, 12.21.22. @...Discharge device 3゜4.23, 24.33...Solenoid operated valve 5,6...Hinge plate 8A, 8B, 1
8A, 18B, 28A, 28B.

Claims (1)

【特許請求の範囲】 1、熱溶融性物質のスプレイ式造粒法において、加熱溶
融体を、複数箇集束され、かつそれらが互いに必要とす
る角度αの与えられた噴出口8A、8Bより、それぞれ
のスプレイパターンSA、SBが重複しないように噴出
スプレイさせ、これらスプレイによって生じた粒子を、
上記複数箇の噴出口群の中間部に設けられた静電気荷電
用電極10への電圧印荷によって生じた電気力線により
、複数箇に分散されているスプレイパターンの中央部の
方に引き寄せて、それらスプレイパターンの空間部を埋
め、スプレイパターンを全体的に拡大かつ粒子分布を均
一化し、各粒子間の間隔をあけることによって粒子相互
の接触、互着を未然に防ぐことを特徴とする熱溶融性物
質のスプレイ式造粒方法。 2、スプレイされた空中の液状粒子に対し、高圧液化ガ
スを吹き付けることによって冷却固化を促進せしめるこ
とを特徴とする特許請求の範囲第1項記載の熱溶融性物
質のスプレイ式造粒方法。 3、特許請求の範囲第1項及び第2項記載の「スプレイ
」は「二流体スプレイ」又は「エアレススプレイ」であ
るもの。 4、熱溶融性物質のスプレイ式造粒装置において、集束
された複数箇の噴出口18A、18Bとそれら噴出口群
の中間部に静電気荷電用電極20等の設けられたスプレ
イ装置を、該スプレイ装置の全周囲を包囲するスプレイ
室13内の上方部に設け、かつ該スプレイ室の下方には
高圧液化ガスの噴出口15、16の設けられることを特
徴とする熱溶融性物質のスプレイ式造粒装置。
[Claims] 1. In the spray granulation method of heat-melting substances, the heated melt is focused at a plurality of spout ports 8A and 8B each having a required angle α to each other, The spray patterns SA and SB are ejected so that they do not overlap, and the particles generated by these sprays are
The lines of electric force generated by applying a voltage to the electrostatic charging electrode 10 provided in the middle of the plurality of jet nozzle groups draw the spray pattern toward the center of the plurality of spray patterns, Thermal melting is characterized by filling the spaces in the spray pattern, expanding the spray pattern as a whole, making the particle distribution uniform, and preventing particles from coming into contact with each other or sticking to each other by creating spaces between each particle. Spray granulation method for sexual substances. 2. The spray-type granulation method of a heat-fusible substance according to claim 1, wherein the sprayed liquid particles in the air are sprayed with high-pressure liquefied gas to promote cooling and solidification. 3. The "spray" described in claims 1 and 2 is a "two-fluid spray" or an "airless spray." 4. In a spray type granulation device for heat-melting substances, a spray device having a plurality of focused jet ports 18A, 18B and an electrostatic charging electrode 20, etc. provided in the middle of the group of jet ports is used for spraying. A spray method for manufacturing a heat-melting substance is provided in the upper part of a spray chamber 13 that surrounds the entire periphery of the apparatus, and that jet ports 15 and 16 for high-pressure liquefied gas are provided in the lower part of the spray chamber. Grain device.
JP8520685A 1985-04-20 1985-04-20 Spray-type granulation method of heat-fusible substance and its granulation apparatus Expired - Lifetime JPH06185B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8520685A JPH06185B2 (en) 1985-04-20 1985-04-20 Spray-type granulation method of heat-fusible substance and its granulation apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8520685A JPH06185B2 (en) 1985-04-20 1985-04-20 Spray-type granulation method of heat-fusible substance and its granulation apparatus

Publications (2)

Publication Number Publication Date
JPS62121634A true JPS62121634A (en) 1987-06-02
JPH06185B2 JPH06185B2 (en) 1994-01-05

Family

ID=13852124

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8520685A Expired - Lifetime JPH06185B2 (en) 1985-04-20 1985-04-20 Spray-type granulation method of heat-fusible substance and its granulation apparatus

Country Status (1)

Country Link
JP (1) JPH06185B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007509739A (en) * 2003-10-30 2007-04-19 ラボラトワール セローノ ソシエテ アノニム Method and apparatus for cooling and atomizing liquid or pasty substances
US10981130B2 (en) 2016-09-21 2021-04-20 Dressler Group GmbH & Co. KG Device and method for producing pulverulent plastics with a spherical structure

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007509739A (en) * 2003-10-30 2007-04-19 ラボラトワール セローノ ソシエテ アノニム Method and apparatus for cooling and atomizing liquid or pasty substances
US10981130B2 (en) 2016-09-21 2021-04-20 Dressler Group GmbH & Co. KG Device and method for producing pulverulent plastics with a spherical structure

Also Published As

Publication number Publication date
JPH06185B2 (en) 1994-01-05

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