JPH0629662Y2 - Vacuum dryer - Google Patents

Vacuum dryer

Info

Publication number
JPH0629662Y2
JPH0629662Y2 JP3085988U JP3085988U JPH0629662Y2 JP H0629662 Y2 JPH0629662 Y2 JP H0629662Y2 JP 3085988 U JP3085988 U JP 3085988U JP 3085988 U JP3085988 U JP 3085988U JP H0629662 Y2 JPH0629662 Y2 JP H0629662Y2
Authority
JP
Japan
Prior art keywords
drying
inert gas
vacuum
valve
container
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.)
Expired - Lifetime
Application number
JP3085988U
Other languages
Japanese (ja)
Other versions
JPH01134893U (en
Inventor
光彦 渡辺
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.)
Tokin Corp
Original Assignee
Tokin Corp
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 Tokin Corp filed Critical Tokin Corp
Priority to JP3085988U priority Critical patent/JPH0629662Y2/en
Publication of JPH01134893U publication Critical patent/JPH01134893U/ja
Application granted granted Critical
Publication of JPH0629662Y2 publication Critical patent/JPH0629662Y2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Drying Of Solid Materials (AREA)
  • Treatment Of Sludge (AREA)

Description

【考案の詳細な説明】 〔分野の概要〕 本考案は、サマリウムコバルト磁石微粉末の乾燥に使用
する装置で、一般には酸化し易い物質の泥漿から乾燥粉
を得るための真空乾燥機の構造に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Outline of Field] The present invention relates to an apparatus used for drying fine powder of samarium-cobalt magnet, and generally relates to a structure of a vacuum dryer for obtaining dry powder from sludge which is an easily oxidizable substance. It is a thing.

〔従来技術の内容と問題点〕 従来、泥漿の乾燥方法としては、泥漿をそのまま真空
乾燥機に入れて真空乾燥させる方法と、フイルターを
設けた真空乾燥容器内に不活性ガスを注入し、溶媒を圧
搾排出させた後、不活性ガスにより泥漿を乾燥させる方
法、の2つの方法があるが、の方法で乾燥を行うと、
乾燥能力を十分にするためには設備が大型化してしま
い、又、乾燥効率も悪いという欠点があり、又、の方
法では、大量に不活性ガスを使用するため乾燥コストが
多大となるという欠点があった。
[Contents and problems of conventional technology] Conventionally, as a method for drying sludge, a method of putting the sludge in a vacuum dryer as it is and vacuum drying, and injecting an inert gas into a vacuum drying container provided with a filter to remove the solvent There are two methods of drying the slurry with an inert gas after squeezing and discharging.
In order to obtain sufficient drying capacity, there is a drawback that the equipment becomes large and the drying efficiency is poor, and in the method of (1), a large amount of inert gas is used, resulting in a large drying cost. was there.

〔考案の目的〕[Purpose of device]

本考案は、上記の欠点を除去するため、真空乾燥装置に
第1図に示す様な濾過機能を持たせた構造とし、1つの
容器内で泥漿の濾過と乾燥を1つの装置により小型で、
且つ低コストで行うことを目的とする。
In order to eliminate the above-mentioned drawbacks, the present invention has a structure in which a vacuum drying device has a filtering function as shown in Fig. 1, and the filtration and drying of the sludge in one container can be made compact by one device,
Moreover, the purpose is to carry out at low cost.

〔考案の構成〕 本考案は、、酸化し易い物質を含む泥漿の乾燥を行うた
めの真空乾燥装置であって、底面にフイルタを設け、外
壁にヒーターを設けた真空乾燥容器にフイルターの底部
より分岐して外気及び真空ポンプへ通じるパイプに夫々
バルブを設けた構造とし、真空乾燥容器上面の蓋部に不
活性ガス注入用バルブと、底部から前記排出口バルブに
至る途中のパイプに不活性ガス注入用バルブを設け構成
した真空乾燥装置である。
[Construction of the Invention] The present invention is a vacuum drying apparatus for drying sludge containing a substance that easily oxidizes, and a vacuum drying container provided with a filter on the bottom surface and a heater on the outer wall is installed from the bottom of the filter. A valve is provided for each pipe branching to the outside air and the vacuum pump, and an inert gas injection valve is provided on the lid on the top of the vacuum drying container, and an inert gas is provided on the pipe from the bottom to the outlet valve. It is a vacuum drying device provided with an injection valve.

〔実施例による説明〕[Explanation by Examples]

以下、本考案の実施例を図面を用い詳細に説明する。 Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.

本考案は、真空乾燥容器内の泥漿の濾過、及び乾燥を行
うために、真空乾燥容器の本体、フイルター、ヒータ
ー、真空吸引、及び不活性ガスの注入ができる様に構成
したもので、設備と運転経費の両面で安価に、酸化し易
い物質の泥漿の乾燥が行えることを特徴とする。
The present invention is configured so that the main body of the vacuum drying container, the filter, the heater, the vacuum suction, and the injection of the inert gas can be used for filtering and drying the sludge in the vacuum drying container. It is characterized in that the sludge, which is a substance that is easily oxidized, can be dried at low cost in terms of both operating costs.

第1図に於て、真空乾燥容器1の中に泥漿10を入れた状
態で、容器の蓋2を密閉し、初め、濾過及び乾燥時に不
活性ガスを注入するバルブ7より不活性ガスを注入し、
濾過時に溶媒を排出させるためのバルブ5を開けること
により、フイルター3を介して泥漿の濾過を行う(この
時、乾燥時に真空ポンプに容器内の気体を吸引させる時
に開けるバルブ8及びフイルター目詰まり除去用の不活
性ガス注入バルブ6は閉じた状態とする)。フイルター
3を介して濾過された溶媒は、真空乾燥容器1から矢印
Bの方向へ流れ、外部へ排出される。濾過終了後、前記
バルブ5及び前記バルブ7を閉め、真空ポンプ9を作動
させて、前記バルブ8を開ける事により、濾過後の圧搾
体の乾燥を行う。この時、4のヒーターにより圧搾体の
加熱を行ない、又、前記バルブ7より不活性ガスを少量
ずつ注入する事により、溶媒の蒸発を促進させ、乾燥時
間を短縮する。又、乾燥中にフイルターが目詰まりした
場合には、一旦前記バルブ6以外のバルブを閉めた状態
で前記バルブ6を開け、前記バルブ6より真空状態の容
器中に不活性ガスを逆流させることにより、フイルター
の目詰まり除去する。
In FIG. 1, with the slurry 10 put in the vacuum drying container 1, the lid 2 of the container is closed, and the inert gas is first injected through the valve 7 for injecting the inert gas during filtration and drying. Then
By opening the valve 5 for discharging the solvent at the time of filtration, the sludge is filtered through the filter 3 (at this time, the valve 8 which is opened when the gas in the container is sucked by the vacuum pump at the time of drying and the clogging of the filter are removed). The inert gas injection valve 6 for use is closed). The solvent filtered through the filter 3 flows from the vacuum drying container 1 in the direction of arrow B and is discharged to the outside. After the filtration is completed, the valves 5 and 7 are closed, the vacuum pump 9 is operated, and the valve 8 is opened to dry the compressed body after filtration. At this time, the compressed body is heated by the heater of 4, and the evaporation of the solvent is promoted by injecting the inert gas little by little through the valve 7, thereby shortening the drying time. If the filter is clogged during drying, the valve 6 is opened with the valves other than the valve 6 closed once, and the inert gas is caused to flow backward from the valve 6 into the vacuum container. , Remove the clogging of the filter.

従来の加熱型真空乾燥装置では、乾燥の時間を短縮する
ために、伝熱面積を広くとる方法が用いられているた
め、容器が大型化し、酸化し易い物質を扱うためには、
容器中の真空度を上げるために、容器各部に、シールの
方法にも特別の配慮が必要であり、更に容器の大型化に
伴って真空ポンプも大型化する等、設備コスト面での欠
点が大きかった。このため、酸化し易い物質の泥漿の乾
燥方法には、設備が比較的小規模で済む不活性ガスを用
いた泥漿の乾燥方法をとることが一般的となっている。
この方法は、容器内の泥漿中に不活性ガスを通すことに
より、泥漿中の溶媒をガスと一緒に外部へ排出して乾燥
させようとする方法である。しかし、この方法では、泥
漿から乾燥粉に至るまでに大量の不活性ガスを使用する
ことになり、不活性ガスが高価であるために、ランニン
グコストが大きくなってしまうという欠点があった。
In the conventional heating type vacuum drying device, in order to shorten the drying time, a method of taking a large heat transfer area is used, so that the container becomes large and in order to handle substances that are easily oxidized,
In order to raise the degree of vacuum in the container, it is necessary to give special consideration to the sealing method for each part of the container, and the vacuum pump also becomes larger as the container becomes larger. It was great. For this reason, as a method for drying the sludge, which is a substance that easily oxidizes, it is general to use a method for drying the sludge using an inert gas, which requires a relatively small facility.
This method is a method in which an inert gas is passed through the sludge in the container to discharge the solvent in the sludge together with the gas to the outside for drying. However, this method has a drawback that a large amount of inert gas is used from the slurry to the dry powder, and the running cost becomes high because the inert gas is expensive.

本考案の真空乾燥装置によれば、ヒーターと不活性ガス
の併用のために、従来の真空乾燥装置のように大きな伝
熱面積を必要とすることなく、乾燥が可能となるため、
従来に比べ設備が小規模で済み設備コストは従来の真空
乾燥装置の約1/10程度に低減させることが可能となり、
又、不活性ガスを用いた従来の方法に比べ、ヒーター及
び真空ポンプの効果により、この不活性ガスの使用量を
従来の1/5以下に低減させることが可能となり、乾燥の
ランニングコストの大幅な削減を行うことができる。こ
の装置は、その構造が単純且つ小型であるために、外気
に漏洩はほとんどなく、泥漿→圧搾体→乾燥粉に至るま
での一連の作業が完全に外気に触れずに行えるため、酸
化し易い物質の乾燥に幅広く応用することが可能であ
り、且つ、日常の保守・点検・清掃等も簡単に行うこと
ができる。
According to the vacuum dryer of the present invention, since the heater and the inert gas are used in combination, it is possible to perform the drying without requiring a large heat transfer area unlike the conventional vacuum dryer.
Compared to the conventional equipment, the equipment is smaller and the equipment cost can be reduced to about 1/10 of the conventional vacuum drying equipment.
In addition, compared to the conventional method using an inert gas, the amount of this inert gas used can be reduced to 1/5 or less of the conventional one due to the effect of the heater and vacuum pump, which greatly reduces the running cost of drying. Can be reduced. Since the structure of this device is simple and small, it hardly leaks to the outside air, and the series of operations from sludge to pressed body to dry powder can be performed completely without touching the outside air, so it is easily oxidized. It can be widely applied to the drying of substances, and daily maintenance, inspection and cleaning can be easily performed.

〔考案の効果〕[Effect of device]

以上述べた如く、本考案による設備を使用することによ
り、短時間で、且つ乾燥コストの大幅な低減が可能な、
従来よりも安価な酸化し易い物質の乾燥粉末の提供が可
能となった。
As described above, by using the equipment according to the present invention, it is possible to significantly reduce the drying cost in a short time.
It has become possible to provide a dry powder of an easily oxidizable substance that is less expensive than before.

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

第1図は、本考案による真空乾燥装置の系統図。 1……真空乾燥装置。2……容器の蓋。 3……フイルター。4……ヒーター。 9……真空ポンプ。10……泥漿。 5……濾過時に溶媒を排出させるためのバルブ。 6……フイルター目詰まり除去用の不活性ガス注入バル
ブ。 7……濾過及び乾燥時に不活性ガスを注入するバルブ。 8……乾燥時に真空ポンプに容器内の気体を吸引させる
時に開けるバルブ。 A……排出口(真空排気方向)。 B……排出口…(溶媒の流出方向)。
FIG. 1 is a system diagram of a vacuum dryer according to the present invention. 1 ... Vacuum drying device. 2 ... Lid of container. 3 ... Filter. 4 ... heater. 9 ... Vacuum pump. 10 ... slurry. 5 ... Valve for discharging solvent during filtration. 6 ... Inert gas injection valve for removing clogging of the filter. 7: Valve that injects an inert gas during filtration and drying. 8: A valve that opens when the vacuum pump sucks the gas in the container during drying. A: Discharge port (vacuum exhaust direction). B ... Discharge port ... (solvent outflow direction).

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】酸化し易い物質を含む泥漿の乾燥を行うた
めの真空乾燥装置であって、底面にフイルタを設け、外
壁にヒーターを設けた真空乾燥容器に、フイルターの底
部より分岐して外気及び真空ポンプへ通じるパイプに夫
々バルブを設けた構造とし、真空乾燥容器上面の蓋部に
不活性ガス注入用バルブと、底部から前記排出口バルブ
に至る途中のパイプに不活性ガス注入用バルブを設け構
成したことを特徴とする真空乾燥装置。
1. A vacuum drying device for drying sludge containing a substance which is easily oxidized, wherein a vacuum drying container having a filter on the bottom and a heater on the outer wall is branched from the bottom of the filter to the outside air. Also, the pipes leading to the vacuum pump are each provided with a valve, and an inert gas injection valve is provided on the lid of the top surface of the vacuum drying container, and an inert gas injection valve is provided on the pipe from the bottom to the outlet valve. A vacuum drying device characterized by being provided.
JP3085988U 1988-03-07 1988-03-07 Vacuum dryer Expired - Lifetime JPH0629662Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3085988U JPH0629662Y2 (en) 1988-03-07 1988-03-07 Vacuum dryer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3085988U JPH0629662Y2 (en) 1988-03-07 1988-03-07 Vacuum dryer

Publications (2)

Publication Number Publication Date
JPH01134893U JPH01134893U (en) 1989-09-14
JPH0629662Y2 true JPH0629662Y2 (en) 1994-08-10

Family

ID=31256287

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3085988U Expired - Lifetime JPH0629662Y2 (en) 1988-03-07 1988-03-07 Vacuum dryer

Country Status (1)

Country Link
JP (1) JPH0629662Y2 (en)

Also Published As

Publication number Publication date
JPH01134893U (en) 1989-09-14

Similar Documents

Publication Publication Date Title
JP3631931B2 (en) Automatic pneumatic pump
JPH0629662Y2 (en) Vacuum dryer
CN214950158U (en) Chemical industry is with high-efficient centrifuge of taking drying device
CN217868592U (en) Negative pressure suction equipment for deep dehydration of sludge
JP3271710B2 (en) Apparatus for dewatering waste and removing waste by vacuum and partial structure constituting a vacuum accumulator connected to a suction conduit of the apparatus
CN210583124U (en) A dry integration equipment of cooking for rhizome class medicinal material
CN208346014U (en) A kind of sludge Minton dryer
JPS5925779Y2 (en) Transfer device for fluids containing solids
JPS5910321A (en) Dust collecting device
CN2307616Y (en) Screw-type continuous counterflow extraction device
CN220116401U (en) Sludge collecting and drying device
CN208653070U (en) A kind of hot wind suction filtration drying device
JP2683605B2 (en) Vacuum fry device
JPH0629242Y2 (en) Sediment continuous recovery device
JPH0220004Y2 (en)
JPH02115424A (en) Forced drainage device for bathtub having jet function
CN215855713U (en) Take blowdown and air-dried silt to hold and connect ton package dolly
CN210845516U (en) Drainage device of vacuum jig
JPH01171611A (en) Device for treating liquid sample
CN114768274B (en) Bear gall powder drying equipment and bear gall powder drying method
JP3030369U (en) Solvent gas recovery or suction device in washing device, distillation regeneration device or reduced pressure drying device
JPS62193614A (en) Vacuum dehydrator
CN110186062A (en) A kind of catalytic unit for exhaust-gas treatment
JPS5815377Y2 (en) Transfer device for moromi etc.
JPS6342365Y2 (en)