JPS62117601A - Spray drier - Google Patents

Spray drier

Info

Publication number
JPS62117601A
JPS62117601A JP25487785A JP25487785A JPS62117601A JP S62117601 A JPS62117601 A JP S62117601A JP 25487785 A JP25487785 A JP 25487785A JP 25487785 A JP25487785 A JP 25487785A JP S62117601 A JPS62117601 A JP S62117601A
Authority
JP
Japan
Prior art keywords
hot air
sides
dryer
spray disk
particles
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.)
Pending
Application number
JP25487785A
Other languages
Japanese (ja)
Inventor
Kaoru Hattori
薫 服部
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP25487785A priority Critical patent/JPS62117601A/en
Publication of JPS62117601A publication Critical patent/JPS62117601A/en
Pending legal-status Critical Current

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  • Drying Of Solid Materials (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

PURPOSE:To obtain large particles from a small amt. of material in a small space by forming the main drier body into a flat shape and blowing hot air from both side surfaces around a spray disk as a spiral flow in the direction opposite to the rotating direction of the spray disk. CONSTITUTION:The main dryer body is formed into a flat shape and the center line of the rotation of the spray disk 4 is oriented at right angle or almost right angle to both side surfaces 1 and 1' of the main body. A liq. to be sprayed is supplied to the spray disk 4 from a liq. feed pipe 5 along the rotating shaft of the spray disk 4. The drying hot air is blown into the main body from a hot air blowing port 6 through a hot air inlet pipe 7 and a spiral flow in the direction opposite to the rotating direction of the spray disk 4 is produced. Besides, the hot air used for drying is sent to a separator on the outside of the system along with dried particles from a hot air outlet 8. The particles are dropped through an oval small-bore part and a hopper 3 while being dried and discharged from a particle discharge port 9.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は比較的小量の大粒子を得る目的の。[Detailed description of the invention] [Industrial application field] The purpose of the present invention is to obtain relatively small amounts of large particles.

言わば試験用等の噴霧乾燥機に関する。In other words, it relates to a spray dryer for testing purposes.

[従来の技術] 従来の回転噴霧板を備えた小量物を得る目的の試験用等
の噴震乾燥機は、大容量のものを単に縮小し噴霧板の回
転数を多くして微粒子を得るようになっている。大粒子
を得るには多量付着するのを承知で噴震板の回転数を小
さくするなどして対処しているのが現状である。
[Prior art] Conventional spray dryers equipped with a rotating spray plate and used for tests to obtain small quantities of material simply reduce the size of a large capacity product and increase the number of rotations of the spray plate to obtain fine particles. It looks like this. Currently, in order to obtain large particles, the number of rotations of the blast plate is reduced, knowing that a large amount of particles will adhere.

第5図でその構造を説明する。この図は従来の代表例で
あると共に大型のものと大差はない乾燥機の本体は上部
に円筒部40.下部に円錐部41を配し、垂直に組み立
てられている。
The structure will be explained with reference to FIG. This figure shows a typical example of a conventional dryer and is similar to a large-sized dryer. A conical part 41 is disposed at the bottom, and it is assembled vertically.

高速で回転し、液体を噴震する噴霧板4は。The spray plate 4 rotates at high speed and sprays liquid.

円筒の中心線上に水平に円筒部40内に設置されている
。噴霧される液体は、噴霧板4の回転軸に沿って設置さ
れている液供給管5より、噴霧板4に供給される。乾燥
用の熱風は熱風入口管7を通り円筒部40の上部の熱風
吹き込み口6より乾燥機本体に吹き込まれ乾燥に使用さ
れる。そして熱風は乾燥機本体下部の円錐部41の熱風
出口8より9!、産物の一部と共に集塵器におくられる
。残りの粒子は円錐部41のF部の粒子排出口9より捕
集される。
It is installed within the cylindrical portion 40 horizontally on the center line of the cylinder. The liquid to be sprayed is supplied to the spray plate 4 from a liquid supply pipe 5 installed along the rotation axis of the spray plate 4. The hot air for drying passes through the hot air inlet pipe 7 and is blown into the dryer main body from the hot air blowing port 6 at the top of the cylindrical part 40, and is used for drying. And the hot air is 9 from the hot air outlet 8 of the conical part 41 at the bottom of the dryer main body! , are sent to the dust collector along with some of the product. The remaining particles are collected from the particle outlet 9 in the F section of the conical section 41.

[発明が解決する手段] 一般に噴震乾燥機は、大粒子を得ようとすると、噴震さ
れた粒子の飛ぶ距離が長くなり必然的に円筒部分の直径
が大きくなり、それに応じて他の部分も大きくなって遂
に、大型の大容量処理の設備になってしまう、少ない液
量に応じて乾燥機を小型即ち1円筒部を小さくすれば、
粒子の飛ぶ距離が不足して乾燥機本体に未乾燥粒子の付
着が多くな色、このことは乾燥粒子の収率が低下するの
みならず粒子の粒度分布、見掛密度等が変わってしまう
大きな欠点がある。
[Means to be Solved by the Invention] In general, in a spout dryer, when trying to obtain large particles, the distance that the ejected particles fly becomes longer and the diameter of the cylindrical part inevitably becomes larger, and the diameter of the cylindrical part increases accordingly. However, if the dryer is made smaller, i.e., each cylindrical part is made smaller, depending on the small amount of liquid,
Colors where there are many undried particles attached to the dryer body due to insufficient flying distance of the particles, this not only reduces the yield of dried particles but also changes the particle size distribution, apparent density, etc. There are drawbacks.

本発明は比較的小量の大粒子を得ることのできる、専有
面積、専有空間の小さい回転噴霧乾燥機を提供しようと
するものである。
The present invention aims to provide a rotary spray dryer that can obtain a relatively small amount of large particles and that occupies a small area and space.

[問題を解決する手段] 本発明は回転噴震板で噴霧された液滴の飛ぶ方向を広く
とり更に、ド方には乾燥区間を追加し、噴霧板の回転中
心線の方向を狭くした。偏平な空間をもち、熱風を噴霧
板の周辺の両側面より、噴霧板の回転方向と逆な旋回流
を与えて吹き込むことを特徴とするものである。
[Means for solving the problem] In the present invention, the flying direction of droplets sprayed by a rotating spray plate is widened, a drying section is added to the rear side, and the direction of the rotational center line of the spray plate is narrowed. It has a flat space and is characterized by blowing hot air from both sides around the spray plate while giving a swirling flow that is opposite to the direction of rotation of the spray plate.

[作用] 本発明は粒子の飛ぶ方向に広げた偏平型の噴21乾燥機
であり、大粒子の飛ぶ距離と、乾燥空間は十分に確保で
きる。又乾燥機本体は偏平であるので、建物の壁面など
と平行に狭い幅に作れるので、その専有空間は小さい、
したがって  ′噴震乾燥は小空間で小景物の大粒子が
得られる[実施例] 以下図面を参照しつつ本発明の詳細な説明する。第1図
は実施例の両側面を中央より切断した図であり、尚図中
第5図に示したものと同一のものには同符号を付しであ
る。
[Function] The present invention is a flat-type jet 21 dryer that is spread out in the direction in which particles fly, and a sufficient distance for large particles to fly and a sufficient drying space can be ensured. Also, since the dryer itself is flat, it can be made narrow and parallel to the wall of a building, so it occupies a small space.
Therefore, 'Eruption drying allows large particles of small objects to be obtained in a small space [Example] The present invention will be described in detail below with reference to the drawings. FIG. 1 is a view of both sides of the embodiment cut away from the center, and the same parts as shown in FIG. 5 are given the same reference numerals.

本体は、ほぼ卵形で小径の方をドにした平面で垂直に相
対立している2面よりなる両側面1及び1′と、その周
端を囲む帯状面2と、最下部にホッパ一部3を付けたも
のである。
The main body has two sides 1 and 1' which are substantially oval in shape and are vertically opposed to each other on a flat surface with the smaller diameter side facing the other side, a band-like surface 2 surrounding the peripheral edge, and a hopper at the bottom. This is the one with section 3 attached.

回転する噴霧板4は1両側面上部の大径部に左、右と、
ヒほぼ同距離の位置に、噴霧液滴の飛ぶ方向と1両側面
とがほぼ平行になるように取り付けられている。即ち噴
霧板の回転の中心線は両側面[,1′と直角又はほぼ直
角になっCいる。
The rotating spray plate 4 has left and right sides on the large diameter part at the top of both sides.
The two sides are mounted at approximately the same distance from each other so that the flight direction of the sprayed droplets is approximately parallel to both sides. That is, the center line of rotation of the spray plate is perpendicular or almost perpendicular to both sides [, 1'.

噴霧される液体は、液供給管5より噴霧板4の回転軸に
沿って噴霧板4に供給される。乾燥用の熱風は熱風人口
管7を通り1両側面1,1′の噴霧板4の周辺付近に設
けられた熱風吹き込み口6より、噴霧板4の回転方向と
は逆な旋回流を堡えらオ魁て偏・ltな乾燥機本体に吹
き込まれる。これは両側面の噴′JIj板周辺付近に未
乾燥粒子−が付着するのを防止し且つ1粒子の飛ぶ距離
を極力押える有効な手段でもある。又両側面より吹き出
た熱風は噴霧板4及びその周辺で衝突するので粒tとの
接触は4−分に行なわれるので伝熱上好ましいことであ
る。
The liquid to be sprayed is supplied to the spray plate 4 from the liquid supply pipe 5 along the rotation axis of the spray plate 4. The hot air for drying passes through the hot air manifold pipe 7, and from the hot air blowing ports 6 provided near the periphery of the spray plate 4 on both sides 1 and 1', a swirling flow opposite to the direction of rotation of the spray plate 4 is created. It is blown into the main body of the dryer. This is an effective means for preventing undried particles from adhering to the vicinity of the jet plates on both sides and for minimizing the distance that each particle flies. Further, since the hot air blown from both sides collides with the spray plate 4 and its surroundings, contact with the particles t takes place in 4 minutes, which is favorable in terms of heat transfer.

乾燥に使用した熱風は、一部の乾燥粒子と共に熱風量[
18より系外の分離機に送られる。
The hot air used for drying has a hot air volume [
18 to a separator outside the system.

粒子は本体のほぼ卵形の小径部及びホッパ一部を乾燥し
ながら落下して粒子排出口9より排出される。
The particles fall while drying through the approximately egg-shaped small diameter portion of the main body and a portion of the hopper, and are discharged from the particle discharge port 9.

第1図は第3図のA−にの断面図で1両側面1.1′が
平面であり、左右ほぼ対称である。しかし必ずしも両側
面は平面でなくてもよく、又左右対称でなくてもよい、
得られる製品の粒度分布、液の物性、液の供給量、熱風
量、熱風の吹き込み速度及び、両側面の強度などによっ
て両側面の形が定まる。尚両側面よりの熱風量は左右同
じでなくてもよい、これは噴霧された粒子群の流れの形
状によりそれぞれ決定される址である。
FIG. 1 is a sectional view taken along the line A- in FIG. 3, and both sides 1.1' are flat, and the device is substantially symmetrical. However, both sides do not necessarily have to be flat, nor do they have to be symmetrical.
The shape of both sides is determined by the particle size distribution of the resulting product, the physical properties of the liquid, the amount of liquid supplied, the amount of hot air, the blowing speed of the hot air, and the strength of both sides. Note that the amount of hot air from both sides does not have to be the same on the left and right sides; this is determined by the shape of the flow of the sprayed particle groups.

尚図示してないが熱風排出口と粒子排出口を一緒にして
、その後分離することもできる。
Although not shown, the hot air outlet and the particle outlet may be combined and then separated.

第2図は断面図であり5両側面1.rは凹レンズ形であ
る。その下部はホッパー3になっている。
Figure 2 is a cross-sectional view of 5 both sides 1. r has a concave lens shape. At the bottom is hopper 3.

第3図は両側面1を外部より見た圓である。FIG. 3 shows a circle with both sides 1 viewed from the outside.

下部が長くなっているのは重力で落下しつつある粒子の
乾燥を完了させるための空間である。
The longer bottom part is a space for the particles that are falling due to gravity to dry completely.

尚この空間に熱風を若干吹き込んで乾燥能力の向上をは
かることもある。
In addition, some hot air may be blown into this space to improve the drying ability.

第4図は第3図と本質的には同じものであるが両側面の
上部を角ばらせたものである。
FIG. 4 is essentially the same as FIG. 3, but the upper portions of both sides are rounded.

本発明は基本的には得ようとする粒子の大きさで相対立
している両側面の大きさが定まり、乾燥物の毎時の取得
量、熱風量及び、液の物性等で両側面1,1′の間隔が
定まる。
In the present invention, the sizes of the opposite sides are basically determined by the size of the particles to be obtained, and the size of the two sides is determined by the amount of dry matter obtained per hour, the amount of hot air, the physical properties of the liquid, etc. The interval of 1' is determined.

尚本発明は両側面を水平にすることはできない、又その
必要もない。
In the present invention, both sides cannot be made horizontal, nor is it necessary.

[発明の効果] 本発明は実施例に示したごとく、液の噴霧する方向に広
い偏平な空間があり1粒子の飛ぶ距離が大きいし又、乾
燥時間も多いので、小容積にもかかわらず、大粒子が効
率よく得られる。
[Effects of the Invention] As shown in the examples, the present invention has a wide flat space in the direction in which the liquid is sprayed, the distance that one particle flies is long, and the drying time is long, so despite the small volume, Large particles can be obtained efficiently.

このことは今までに見られない試験等の小容量機種とし
ての大きな特徴であり、粒度分布、見掛密度等を主にし
た乾燥品の研究に利するところは大きい。
This is a major feature of a small-capacity model that has never been seen before, and is of great benefit for research on dry products, focusing on particle size distribution, apparent density, etc.

又本体は偏q(であるので、建物の壁面等に片寄せて設
置できるので、場所を取らない噴霧乾燥機としての効果
も大きい。
Also, since the main body is biased, it can be installed on one side of the wall of a building, etc., so it is highly effective as a space-saving spray dryer.

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

第1図、第2図は本発明の実施例の断面図である。 第3図、第4図は本発明の実施例の相対立している両側
面を外部より見た図である。尚第1図は第3図のA−A
’よりの断面図に相当する。 第5図は従来型の例の説明用の断面図である図中の符号
は。 ■、1′は両側面、   2は帯状面。 3はホッパー、    4は噴霧板。 5は液供給管、    6は熱風吹き込み口、8は熱風
出口、    9は粒子排出口。 を示す。
1 and 2 are cross-sectional views of embodiments of the present invention. FIGS. 3 and 4 are external views of opposing sides of an embodiment of the present invention. In addition, Figure 1 is A-A in Figure 3.
Corresponds to a cross-sectional view from '. FIG. 5 is an explanatory cross-sectional view of a conventional example. Reference numerals in the figure indicate. ■, 1' is both sides, 2 is the band surface. 3 is a hopper, 4 is a spray plate. 5 is a liquid supply pipe, 6 is a hot air inlet, 8 is a hot air outlet, and 9 is a particle outlet. shows.

Claims (1)

【特許請求の範囲】 a)乾燥機本体は、ほぼ卵形をした面を2面大径の方を
上にして、所要の間隔で垂直に対立させて両側面を作り
、この周端を帯状の面で包み下方の小径部にホッパーを
つけた、偏平な空間であり、 b)回転する噴霧板は、両側面上方の大円径の部分のほ
ぼ中心に、両側面に平行になるように乾燥機本体内に設
置して、液体を噴霧させ、c)乾燥用熱風は、回転噴霧
板の周辺に近い両側面より、互いに衝突するように且つ
、噴霧板の回転方向と逆な旋回流を与えて吹き込み、d
)熱風の排出口と乾燥粒子の排出口は乾燥機本体下部に
取り付けられている。 以上の構造を特徴とした偏平な噴霧乾燥機。
[Claims] a) The main body of the dryer has two substantially oval-shaped surfaces with the larger diameter facing up, vertically opposing each other at a predetermined interval to form both sides, and the peripheral edge of the dryer body is formed into a band-like shape. It is a flat space with a hopper attached to the small diameter part at the bottom, and b) The rotating spray plate is placed approximately in the center of the large diameter part above both sides, so that it is parallel to both sides. installed in the dryer main body to spray the liquid, and c) the drying hot air is directed from both sides near the periphery of the rotating spray plate so that they collide with each other and create a swirling flow that is opposite to the rotational direction of the spray plate. give and blow, d
) The hot air outlet and dry particle outlet are installed at the bottom of the dryer body. A flat spray dryer featuring the above structure.
JP25487785A 1985-11-15 1985-11-15 Spray drier Pending JPS62117601A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25487785A JPS62117601A (en) 1985-11-15 1985-11-15 Spray drier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25487785A JPS62117601A (en) 1985-11-15 1985-11-15 Spray drier

Publications (1)

Publication Number Publication Date
JPS62117601A true JPS62117601A (en) 1987-05-29

Family

ID=17271071

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25487785A Pending JPS62117601A (en) 1985-11-15 1985-11-15 Spray drier

Country Status (1)

Country Link
JP (1) JPS62117601A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS648904U (en) * 1987-07-06 1989-01-18

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS648904U (en) * 1987-07-06 1989-01-18

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