JPH04118101U - Liquid supply dispersion device in vacuum belt dryer - Google Patents

Liquid supply dispersion device in vacuum belt dryer

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Publication number
JPH04118101U
JPH04118101U JP3780291U JP3780291U JPH04118101U JP H04118101 U JPH04118101 U JP H04118101U JP 3780291 U JP3780291 U JP 3780291U JP 3780291 U JP3780291 U JP 3780291U JP H04118101 U JPH04118101 U JP H04118101U
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JP
Japan
Prior art keywords
conveyor belt
endless conveyor
vacuum
belt
dryer
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
JP3780291U
Other languages
Japanese (ja)
Other versions
JP2558539Y2 (en
Inventor
哲雄 小西
隆一 堤
Original Assignee
株式会社日阪製作所
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 株式会社日阪製作所 filed Critical 株式会社日阪製作所
Priority to JP1991037802U priority Critical patent/JP2558539Y2/en
Publication of JPH04118101U publication Critical patent/JPH04118101U/en
Application granted granted Critical
Publication of JP2558539Y2 publication Critical patent/JP2558539Y2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

(57)【要約】 【目的】 真空ベルト乾燥機で液状材料を乾燥する際に
無端搬送ベルト上での液状材料の膜厚を均一にし、これ
によって最終製品の微粒化を促進する。 【構成】 固定式吐出管8から無端搬送ベルト3上に供
給された液状の被乾燥材料9を、無端搬送ベルト上に対
向間隔Lを置いて配設されたならし板10によって押し
拡げ、均一な厚みに調整する。
(57) [Summary] [Purpose] To make the film thickness of the liquid material uniform on the endless conveyor belt when drying the liquid material using a vacuum belt dryer, thereby promoting atomization of the final product. [Structure] The liquid material to be dried 9 supplied from the fixed discharge pipe 8 onto the endless conveyor belt 3 is forced and spread uniformly by leveling plates 10 arranged on the endless conveyor belt with an opposing interval L. Adjust to the desired thickness.

Description

【考案の詳細な説明】[Detailed explanation of the idea]

【0001】0001

【産業上の利用分野】[Industrial application field]

本考案は真空ベルト乾燥機における給液分散装置に関するものである。 The present invention relates to a feed liquid dispersion device for a vacuum belt dryer.

【0002】0002

【従来の技術】[Conventional technology]

液状、スラリー状、もしくはペースト状に調合された食品材料や薬品材料の乾 燥装置として真空ベルト乾燥機が使用されている。真空ベルト乾燥機は、例えば 、特開昭63ー148967号公報に示すように、真空容器内に無端搬送ベルトを架設し 、この無端搬送ベルトの回動域に第1および第2の恒率乾燥ゾーン、減率乾燥ゾ ーンならびに冷却ゾーンを順次配設すると共に、無端搬送ベルトの回動経路の上 流側に首振り式の原材料吐出ノズルを設け、これに対応して無端搬送ベルトの回 動経路の下流側にはクラッシャ装置を配設することによって連続乾燥装置に構成 されている。 Drying of food and pharmaceutical ingredients formulated in liquid, slurry, or paste form A vacuum belt dryer is used as the drying device. Vacuum belt dryers are for example As shown in Japanese Patent Application Laid-open No. 63-148967, an endless conveyor belt is installed inside a vacuum container. , a first and second constant rate drying zone and a decreasing rate drying zone are located in the rotating region of this endless conveyor belt. In addition to sequentially arranging the cooling zone and the cooling zone, An oscillating raw material discharge nozzle is installed on the flow side, and the endless conveyor belt rotates accordingly. Constructed into a continuous drying device by installing a crusher device on the downstream side of the flow path. has been done.

【0003】0003

【考案が解決しようとする課題】[Problem that the idea aims to solve]

上記真空ベルト乾燥機を使用することによって、噴霧乾燥機や凍結乾燥機で問 題とされていた乾燥コストの高騰や製品の溶解性や成分変化が解決されることは 事実であるが、首振り式の原材料吐出ノズルは駆動装置を必要とするため運転コ ストが高騰し、また首振り運動の方向変換点で無端搬送ベルト上への原材料の供 給量が局部的に増大してしまうという問題点が指摘されている。このような死点 の形成に起因する原材料の分散不良を解消するためには、原材料吐出ノズルの首 振り速度を無端搬送ベルトの幅方向に沿って変化させたり、揺動軌跡を調整した りする必要があり、このような構造にした場合には、装置の複雑化や保守管理作 業がむづかしくなるという別の問題が発生する。 By using the above-mentioned vacuum belt dryer, you can avoid problems with spray dryers and freeze dryers. The problem of soaring drying costs and changes in product solubility and composition will not be resolved. Although it is true, the swing-type raw material discharge nozzle requires a drive device, so the operation cost is low. In addition, the supply of raw materials onto the endless conveyor belt at the point of change of direction of the oscillating motion increases. It has been pointed out that the problem is that the amount of supply increases locally. dead center like this In order to eliminate poor dispersion of raw materials caused by the formation of The swing speed was changed along the width direction of the endless conveyor belt, and the swing trajectory was adjusted. This type of structure increases the complexity of the equipment and requires maintenance work. Another problem arises, which is that the work becomes difficult.

【0004】 特に被乾燥材料がペンキ添加剤のようなチキソトロピック性(揺変性)材料で ある場合には、真空乾燥終了後、微粒化することによって粒子表面積を大きくす る必要があり、無端搬送ベルト上に撒布されたときの被乾燥材料の膜厚の不均一 が大きな障害となる。即ち、膜厚の厚い部分の乾燥が終了していない段階でも膜 厚の薄い部分は乾燥が終了することによって当該部分の品温が上昇するため無端 搬送ベルトの表面に溶着し易くなり、微粒化が阻害されることによってペンキ添 加剤の表面積が小さくなってしまう。0004 Especially if the material to be dried is a thixotropic material such as a paint additive. In some cases, after vacuum drying, the particle surface area can be increased by atomization. unevenness in film thickness of the material to be dried when spread on the endless conveyor belt. is a major obstacle. In other words, even when the thick part of the film has not completely dried, When the thickness of a thin part is finished, the temperature of the part increases as the drying process ends. Paint additives tend to adhere to the surface of the conveyor belt and prevent atomization. The surface area of the additive becomes smaller.

【0005】[0005]

【課題を解決するための手段】[Means to solve the problem]

上記課題の解決手段として本考案は、液状、スラリー状、もしくはペースト状 に調合された原材料を真空容器内に設けられた無端搬送ベルト上に供給して乾燥 する真空ベルト乾燥機において、上記無端搬送ベルトの上流域に原材料の吐出管 を固設し、この原材料吐出管から見て下流側の無端搬送ベルト上に、無端搬送ベ ルトの上面との間に所定の対向間隔を置き、かつ、ベルトの幅方向全域に亘って 原材料のならし板を配置したことを特徴とする真空ベルト乾燥機における給液分 散装置を提供するものである。 As a means of solving the above problems, the present invention provides a liquid, slurry, or paste form. The mixed raw materials are fed onto an endless conveyor belt inside a vacuum container and dried. In the vacuum belt dryer, the raw material discharge pipe is located upstream of the endless conveyor belt. An endless conveyor belt is fixedly installed on the endless conveyor belt on the downstream side as seen from this raw material discharge pipe. with a predetermined spacing between the upper surface of the belt and the entire width of the belt. Liquid supply in a vacuum belt dryer characterized by a leveling board for raw materials It provides a dispersion device.

【0006】[0006]

【作用】[Effect]

吐出管の開口部から無端搬送ベルト上に液状、スラリー状、もしくはペースト 状の原材料を吐出する。この後、上記吐出管から眺めて無端搬送ベルトの下流側 に配設されているならし板によって厚く堆積している原材料を押し拡げ、ならし 板の設置点を通過した原材料にならし板の下縁と無端搬送ベルトの上面との間隔 と等しい膜厚を与える。このように膜厚を均一化された原材料は、無端搬送ベル トの回転によって恒率乾燥ゾーン、減率乾燥ゾーン、ならびに冷却ゾーンに順次 到達し、所定の温度条件下に真空乾燥処理を施こされ、微細な粒径を持った製品 に仕上げられる。 Liquid, slurry, or paste is transferred from the opening of the discharge pipe onto the endless conveyor belt. Discharges the raw material of the shape. After this, the downstream side of the endless conveyor belt as seen from the above discharge pipe The thickly accumulated raw materials are spread out using leveling plates installed in the Distance between the lower edge of the flattening plate and the top surface of the endless conveyor belt Gives a film thickness equal to . The raw material whose film thickness has been made uniform in this way is transferred to an endless conveyor belt. The constant rate drying zone, decreasing rate drying zone, and cooling zone are sequentially moved by A product with a fine particle size that has been vacuum dried under specified temperature conditions. Finished in.

【0007】[0007]

【実施例】【Example】

真空ベルト乾燥機(1)は、10torr前後の真空度に保持された真空容器(2 )内に無端搬送ベルト(3)を回転可能に張設支持し、この無端搬送ベルト(3 )の回動域に上流側から下流側に向って第1の恒率乾燥ゾーン(4)、第2の恒 率乾燥ゾーン(5)、減率乾燥ゾーン(6)、ならびに冷却ゾーン(7)を順次 配設することによって連続的な真空乾燥手段を構成している。無端搬送ベルト( 3)の回動経路の上流側には、管壁の下面に複数個の原料吐出孔を整列配置状態 で穿設してなる原材料の吐出管(8)が無端搬送ベルト(3)の回動方向に対し て略直交するように固設されており、この原材料吐出管(8)から見て下流側の 無端搬送ベルト(3)上には図3に拡大図示するようにこの無端搬送ベルト(3 )の上面との間に原材料(9)の膜厚と略等しい所定の対向間隔Lを置き、かつ 、無端搬送ベルト(3)の幅方向全域に亘って延びるようにならし板(10)を 設置する。上記吐出管(8)および、ならし板(10)に対応して無端搬送ベル ト(3)の回動経路の下流側には、真空乾燥された原材料(9)の粉砕装置とし て上下動する剪断刃を具えたプレクラッシャ(11)、およびメッシュと回転ブ レードからなるメインクラッシャ(12)が設けられている。ならし板(10) と無端搬送ベルト(3)との対向間隔Lは、被乾燥材料(9)の種類と特性に応 じて調節する。このためならし板(10)にはアジャストスクリュー等の間隔調 整機構が付設されている。 The vacuum belt dryer (1) consists of a vacuum container (2) maintained at a vacuum level of around 10 torr. ), an endless conveyor belt (3) is rotatably stretched and supported within the endless conveyor belt (3). ), from the upstream side to the downstream side, there is a first constant rate drying zone (4) and a second constant rate drying zone (4). rate drying zone (5), lapse rate drying zone (6), and cooling zone (7) in sequence. This arrangement constitutes continuous vacuum drying means. Endless conveyor belt ( 3) On the upstream side of the rotation path, multiple raw material discharge holes are aligned on the lower surface of the pipe wall. The raw material discharge pipe (8) is perforated with respect to the rotating direction of the endless conveyor belt (3). The pipes are fixedly installed so that they are substantially orthogonal to each other, and the downstream side when viewed from this raw material discharge pipe (8) On the endless conveyor belt (3), as shown in an enlarged view in FIG. ) with a predetermined facing distance L approximately equal to the film thickness of the raw material (9), and , a leveling plate (10) is provided so as to extend over the entire width direction of the endless conveyor belt (3). Install. An endless conveyor belt corresponding to the above-mentioned discharge pipe (8) and leveling plate (10) On the downstream side of the rotary path of (3), there is a crushing device for vacuum-dried raw materials (9). A pre-crusher (11) equipped with a shearing blade that moves up and down, and a mesh and rotating blade. A main crusher (12) consisting of a blade is provided. Leveling board (10) and the endless conveyor belt (3), depending on the type and characteristics of the material to be dried (9). Adjust accordingly. For this reason, the leveling plate (10) has adjustment screws etc. Equipped with an adjustment mechanism.

【0008】 以下表1に示すようにチキソトロピック性を具えたペンキ添加剤の真空乾燥剤 例に基づいて本考案装置の運転条件と製品特性を説明する。[0008] Vacuum drying agent for paint additives with thixotropic properties as shown in Table 1 below. The operating conditions and product characteristics of the device of the present invention will be explained based on an example.

【0009】[0009]

【表1】 [Table 1]

【0010】 尚、上記表1には首振り式の吐出ノズルを具えた従来装置による真空乾燥例を 比較対象として併記する。0010 Table 1 above shows examples of vacuum drying using conventional equipment equipped with a swing-type discharge nozzle. They are also listed for comparison.

【0011】[0011]

【考案の効果】[Effect of the idea]

無端搬送ベルト(3)上に供給された被乾燥材料(9)をならし板(10)で 堰止めることによって無端搬送ベルト(3)の上面とならし板(10)の下縁と の対向間隔と略等しい一定の膜厚に押し拡げる。 The material to be dried (9) fed onto the endless conveyor belt (3) is leveled with a leveling plate (10). By damming, the upper surface of the endless conveyor belt (3) and the lower edge of the leveling plate (10) The film is spread to a constant film thickness that is approximately equal to the opposing spacing.

【0012】 この膜厚の一定化によって無端搬送ベルト(3)上における被乾燥材料(9) の乾燥条件が均一化され、余分な熱が真空乾燥に関与しない理想的な乾燥状態が 維持される。この結果、乾燥時の被乾燥材料(9)の表面積が増大し、微粒化さ れた高品質の製品が得られる。また、無端搬送ベルト(3)の全面に被乾燥材料 (9)が展延されるから非給液空間が減少し、乾燥能力も大幅に向上する。0012 By keeping the film thickness constant, the material to be dried (9) on the endless conveyor belt (3) An ideal drying condition is created where the drying conditions are uniform and no excess heat is involved in vacuum drying. maintained. As a result, the surface area of the material to be dried (9) increases during drying, resulting in less atomization. The result is a high quality product. In addition, the material to be dried is placed on the entire surface of the endless conveyor belt (3). (9) is spread, so the non-liquid supply space is reduced and the drying capacity is greatly improved.

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

【図1】真空ベルト乾燥機の縦断面図[Figure 1] Longitudinal cross-sectional view of a vacuum belt dryer

【図2】真空ベルト乾燥機の平面図[Figure 2] Plan view of vacuum belt dryer

【図3】ならし板と無端搬送ベルトの部分拡大図[Figure 3] Partially enlarged view of leveling plate and endless conveyor belt

【符号の説明】[Explanation of symbols]

1 真空ベルト乾燥機 2 真空容器 3 無端搬送ベルト 8 原材料の吐出管 9 被乾燥材料 10 ならし板 1 Vacuum belt dryer 2 Vacuum container 3 Endless conveyor belt 8 Raw material discharge pipe 9 Material to be dried 10 Leveling board

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】 液状、スラリー状、もしくはペースト状
に調合された原材料を真空容器内に設けられた無端搬送
ベルト上に供給して乾燥する真空ベルト乾燥機におい
て、上記無端搬送ベルトの上流域に原材料の吐出管を固
設し、この原材料吐出管から見て下流側の無端搬送ベル
ト上に、無端搬送ベルトの上面との間に所定の対向間隔
を置き、かつ、ベルトの幅方向全域に亘って原材料のな
らし板を配置したことを特徴とする真空ベルト乾燥機に
おける給液分散装置。
Claim 1: In a vacuum belt dryer that supplies and dries raw materials prepared in the form of liquid, slurry, or paste onto an endless conveyor belt provided in a vacuum container, a dryer is provided in the upstream region of the endless conveyor belt. A raw material discharge pipe is fixedly installed on the endless conveyor belt on the downstream side as seen from the raw material discharge pipe, with a predetermined opposing interval between the top surface of the endless conveyor belt and the entire width of the belt. A liquid supply dispersion device for a vacuum belt dryer, characterized in that a leveling plate for raw materials is arranged.
JP1991037802U 1991-03-28 1991-03-28 Liquid supply disperser in vacuum belt dryer Expired - Fee Related JP2558539Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1991037802U JP2558539Y2 (en) 1991-03-28 1991-03-28 Liquid supply disperser in vacuum belt dryer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1991037802U JP2558539Y2 (en) 1991-03-28 1991-03-28 Liquid supply disperser in vacuum belt dryer

Publications (2)

Publication Number Publication Date
JPH04118101U true JPH04118101U (en) 1992-10-22
JP2558539Y2 JP2558539Y2 (en) 1997-12-24

Family

ID=31919454

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1991037802U Expired - Fee Related JP2558539Y2 (en) 1991-03-28 1991-03-28 Liquid supply disperser in vacuum belt dryer

Country Status (1)

Country Link
JP (1) JP2558539Y2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2022536113A (en) * 2019-08-14 2022-08-12 安尼康(福建)環保設備有限公司 Peristaltic propulsion drying equipment

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5361968B2 (en) * 2011-09-28 2013-12-04 株式会社日阪製作所 Liquid supply dispersion device

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6060661A (en) * 1983-09-14 1985-04-08 Ricoh Co Ltd Control method of copying machine
JPS6124628A (en) * 1984-07-13 1986-02-03 Yamaha Motor Co Ltd Seat construction in small type vehicle
JPS62151130A (en) * 1985-12-24 1987-07-06 山崎 定 Crepe baking apparatus
JPS63148967A (en) * 1986-12-11 1988-06-21 Hisaka Works Ltd Vacuum belt drier
JPH01159003A (en) * 1987-12-17 1989-06-22 Okawara Mfg Co Ltd Belt type continuous vacuum drying apparatus

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6060661A (en) * 1983-09-14 1985-04-08 Ricoh Co Ltd Control method of copying machine
JPS6124628A (en) * 1984-07-13 1986-02-03 Yamaha Motor Co Ltd Seat construction in small type vehicle
JPS62151130A (en) * 1985-12-24 1987-07-06 山崎 定 Crepe baking apparatus
JPS63148967A (en) * 1986-12-11 1988-06-21 Hisaka Works Ltd Vacuum belt drier
JPH01159003A (en) * 1987-12-17 1989-06-22 Okawara Mfg Co Ltd Belt type continuous vacuum drying apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2022536113A (en) * 2019-08-14 2022-08-12 安尼康(福建)環保設備有限公司 Peristaltic propulsion drying equipment

Also Published As

Publication number Publication date
JP2558539Y2 (en) 1997-12-24

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