JPS5834002A - Ultrasonic spray drying method - Google Patents

Ultrasonic spray drying method

Info

Publication number
JPS5834002A
JPS5834002A JP13145081A JP13145081A JPS5834002A JP S5834002 A JPS5834002 A JP S5834002A JP 13145081 A JP13145081 A JP 13145081A JP 13145081 A JP13145081 A JP 13145081A JP S5834002 A JPS5834002 A JP S5834002A
Authority
JP
Japan
Prior art keywords
liquid
particles
container
atomized
cyclone
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
JP13145081A
Other languages
Japanese (ja)
Inventor
Ichiro Tsutsui
一郎 筒井
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 JP13145081A priority Critical patent/JPS5834002A/en
Publication of JPS5834002A publication Critical patent/JPS5834002A/en
Pending legal-status Critical Current

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  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

PURPOSE:To instantaneously dry a liquid sample, by atomizing said liquid sample into a high temp. air stream by utilizing ultrasonic waves. CONSTITUTION:When a liquid supplying pump 2 is rotated and a heater 7 is switched on as well as a suction fan 14 is rotated, a liquid containing fine particles is atomized by an ultrasonic sprayer 3 and introduced into a drying cylinder 8. On the other hand, air accelerated by the heater 7 is flowed into the upper part of the drying cylinder 8 tangentially at a high velocity to dry the atomized liquid herein. The dried coarse particles are fallen into a container 9 and the remainder of dried particles are flowed into a first cyclone 10 along with hot air to be classified into small particles and fine particles and the former is dropped into a small particle container. The fine particles are sent to a second cyclone 12 to be collected by a container 13. In addition, because the particle size of atomized particles can be controlled by the flow amount of the liquid sample and the speed adjustment of the liquid sending pump, the adjustment of the particle size of the powder becomes possible.

Description

【発明の詳細な説明】 本発明は乾燥すれば微粉体になる物質または懸濁液を微
粒子状にし、比表面積を著しく増大させて熱風に曝し、
液滴を乾燥するいわゆる噴霧乾燥方法の改良に関するも
のである。詳しく云えば、高温気流中に、上記の液体試
料を超音波を利用して霧状にし、瞬間的に乾燥する方法
に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention involves turning a substance or suspension that becomes a fine powder when dried into fine particles, significantly increasing the specific surface area, and exposing the fine particles to hot air.
This invention relates to improvements in the so-called spray drying method for drying droplets. Specifically, the present invention relates to a method of atomizing the above-mentioned liquid sample using ultrasonic waves in a high-temperature air stream and instantaneously drying it.

従来の噴霧乾燥法はコンプレッサーを必要とし液体と空
気を調節して霧を発生す−る方法と、高速モータによっ
て羽根を回し、これに液体を注いで遠心力によって霧を
発生する方法がある。本発明はこれらの方法と根本的に
異る噴霧発生法を用いた乾燥装置で、以下図を参照して
説明する。
Conventional spray drying methods include a method that requires a compressor and generates mist by adjusting the liquid and air, and a method that uses a high-speed motor to turn blades and pour the liquid into the blades to generate mist using centrifugal force. The present invention is a drying apparatus using a spray generation method fundamentally different from these methods, and will be explained below with reference to the drawings.

1は試料液、2は流量調節器付きの送液ポンプである。1 is a sample liquid, and 2 is a liquid sending pump with a flow rate regulator.

3は超音波噴霧発生器で、中心を送液管Pが通っている
。4は超音波噴霧発生器用アンプで、これを操作するこ
とにより、振動数等の調節が可能である。7はヒーター
でヒータ一温度調節器5によって温度制御が行われる。
3 is an ultrasonic spray generator, and a liquid feeding pipe P passes through the center thereof. 4 is an amplifier for the ultrasonic spray generator, and by operating this, it is possible to adjust the vibration frequency, etc. Reference numeral 7 denotes a heater whose temperature is controlled by a heater temperature controller 5.

6I/iヒ一タ一温度調節器用アンプである。8は乾燥
筒で、上部に超音波噴霧発生器3で発生した超音波ノズ
3aがあり、該ノズル3aの中心に送液管Pが位置して
いる。乾燥筒8の下端には粗粒容器9がとりつけられて
いる。乾燥筒8の上部には前記ヒーター7で加熱された
加熱空気送給管7aが接続フランジ17を介し接線的に
接続されている。10は第1サイクロンで、その入口管
10aが乾燥筒8の下部に接続され、その出口管10b
は第2サイクロン12の入口管12aに接続されている
。14は吸引ファン、15は風量調節器である。16は
乾燥空気流量計で、第1サイクロンの入口管10a と
同じく出口管10b間にとりつけられている。11は第
1サイクロンの細粒容器、13は第2サイクロンの微粒
容器である。
This is an amplifier for the 6I/i temperature controller. Reference numeral 8 denotes a drying cylinder, on the top of which there is an ultrasonic nozzle 3a generated by the ultrasonic spray generator 3, and in the center of the nozzle 3a a liquid feeding pipe P is located. A coarse particle container 9 is attached to the lower end of the drying cylinder 8. A heated air supply pipe 7a heated by the heater 7 is tangentially connected to the upper part of the drying cylinder 8 via a connecting flange 17. 10 is a first cyclone, whose inlet pipe 10a is connected to the lower part of the drying cylinder 8, and whose outlet pipe 10b is connected to the lower part of the drying cylinder 8.
is connected to the inlet pipe 12a of the second cyclone 12. 14 is a suction fan, and 15 is an air volume regulator. A dry air flowmeter 16 is installed between the inlet pipe 10a and the outlet pipe 10b of the first cyclone. 11 is a fine grain container of the first cyclone, and 13 is a fine grain container of the second cyclone.

以上の構成であるから、送液ポンプ2を回し、かつヒー
ター7をONに、又吸引ファン14を回転させると、微
粒子を含有する液体は超音波噴霧発生器3で霧化されて
乾燥筒内に入る。一方ヒーター7で加熱された空気は乾
燥筒8の上部に接線的に高速で流入しここで霧化されだ
液体を乾燥させる。この場合霧の粒子の大小加減は、試
料液の流量及び送液ポンプの速度加減によって調節でき
る。
With the above configuration, when the liquid feed pump 2 is turned, the heater 7 is turned on, and the suction fan 14 is rotated, the liquid containing fine particles is atomized by the ultrasonic spray generator 3 and placed inside the drying cylinder. to go into. On the other hand, the air heated by the heater 7 flows tangentially into the upper part of the drying tube 8 at high speed and dries the atomized liquid there. In this case, the size of the mist particles can be adjusted by adjusting the flow rate of the sample liquid and the speed of the liquid pump.

乾燥した粒子の粗粒は容器9に落下し、他は熱風と共に
第1サイクロン10に流入しここで細粒と微粒に分級さ
れ、細粒は細粒容器11に落下する。微粒は第2サイク
ロンに送られここで容器13に収集される。
Coarse particles of the dried particles fall into a container 9, and the rest flow into a first cyclone 10 together with hot air, where they are classified into fine particles and fine particles, and the fine particles fall into a fine particle container 11. The fines are sent to a second cyclone where they are collected in a container 13.

本発明は従来の噴霧乾燥器のごとく圧縮空気を使用しな
いので、コンプレッサーを必要としない。
The present invention does not use compressed air like conventional spray dryers and therefore does not require a compressor.

したがってコンプレッサーの空気を加熱しなくてよいの
で節電となる。
Therefore, there is no need to heat the air in the compressor, which saves electricity.

霧の粒子の加減は試料液の流量、液送ポンプの速度調節
によって調節できるので、粉体の粒度調節が可能である
。したがって従来のごとく、粒子の大きさが変ったとき
、噴霧ノズルを交換する必要がない。
Since the amount of mist particles can be adjusted by adjusting the flow rate of the sample liquid and the speed of the liquid feed pump, it is possible to adjust the particle size of the powder. Therefore, there is no need to replace the spray nozzle when the particle size changes, as was the case in the past.

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

図は本方法を実施する装置を示す。 図において;− 1試料液       2送液ポンプ(流量調節器付)
3超音波噴霧発生器  4超音波噴霧発生器用アンプ5
ヒータ一温度調節器  6ヒ一タ一温度調節器用アンプ
7ヒーター      8乾燥筒 9粗粒容器      10第1サイクロン11細粒容
器     12第2サイクロン13微粒容器    
 14吸引ファン15吸引ファン用風量調節器 16乾
燥空気流量計17接続ガラス製フランジ 以上 出願人 筒  井  −部 代理人 弁理士 大 橋   勇
The figure shows an apparatus for carrying out the method. In the figure: - 1 Sample liquid 2 Liquid sending pump (with flow rate regulator)
3 Ultrasonic spray generator 4 Amplifier for ultrasonic spray generator 5
Heater - Temperature regulator 6 Heater - Temperature regulator amplifier 7 Heater 8 Drying tube 9 Coarse grain container 10 First cyclone 11 Fine grain container 12 Second cyclone 13 Fine grain container
14 Suction fan 15 Air volume regulator for suction fan 16 Dry air flow meter 17 Connecting glass flange and above Applicant Tsutsui -be representative Patent attorney Isamu Ohashi

Claims (1)

【特許請求の範囲】[Claims] 乾燥筒の上端より高温気流中に試料の溶液または懸濁液
を超音波によって霧状に落下させ、瞬間的に乾燥させる
ことを特徴とする超音波噴霧乾燥法。
An ultrasonic spray drying method that is characterized by dropping a solution or suspension of a sample in the form of a mist using ultrasonic waves into a high-temperature air stream from the top of a drying cylinder, and instantaneously drying it.
JP13145081A 1981-08-24 1981-08-24 Ultrasonic spray drying method Pending JPS5834002A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13145081A JPS5834002A (en) 1981-08-24 1981-08-24 Ultrasonic spray drying method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13145081A JPS5834002A (en) 1981-08-24 1981-08-24 Ultrasonic spray drying method

Publications (1)

Publication Number Publication Date
JPS5834002A true JPS5834002A (en) 1983-02-28

Family

ID=15058235

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13145081A Pending JPS5834002A (en) 1981-08-24 1981-08-24 Ultrasonic spray drying method

Country Status (1)

Country Link
JP (1) JPS5834002A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0628331A1 (en) * 1993-05-11 1994-12-14 Ultrasonic Dryer Ltd. Spray drying system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0628331A1 (en) * 1993-05-11 1994-12-14 Ultrasonic Dryer Ltd. Spray drying system

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