JPS59501939A - Method and equipment for dehydrating liquid or pasty mixtures - Google Patents
Method and equipment for dehydrating liquid or pasty mixturesInfo
- Publication number
- JPS59501939A JPS59501939A JP83503147A JP50314783A JPS59501939A JP S59501939 A JPS59501939 A JP S59501939A JP 83503147 A JP83503147 A JP 83503147A JP 50314783 A JP50314783 A JP 50314783A JP S59501939 A JPS59501939 A JP S59501939A
- Authority
- JP
- Japan
- Prior art keywords
- mixture
- microwave generator
- microwave
- shaft
- wall surface
- 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
Links
- 239000000203 mixture Substances 0.000 title claims description 29
- 238000000034 method Methods 0.000 title claims description 16
- 239000007788 liquid Substances 0.000 title claims description 9
- 235000011837 pasties Nutrition 0.000 title claims 2
- 238000012545 processing Methods 0.000 claims description 26
- 230000018044 dehydration Effects 0.000 claims description 9
- 238000006297 dehydration reaction Methods 0.000 claims description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 8
- 238000005192 partition Methods 0.000 claims description 6
- 239000011521 glass Substances 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 5
- 238000001035 drying Methods 0.000 claims description 4
- 238000007599 discharging Methods 0.000 claims description 3
- 238000000926 separation method Methods 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 2
- 239000010935 stainless steel Substances 0.000 claims description 2
- 238000009792 diffusion process Methods 0.000 claims 1
- 238000013022 venting Methods 0.000 claims 1
- 238000013519 translation Methods 0.000 description 8
- 238000004519 manufacturing process Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 235000009508 confectionery Nutrition 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 240000001549 Ipomoea eriocarpa Species 0.000 description 1
- 235000005146 Ipomoea eriocarpa Nutrition 0.000 description 1
- 241001440346 Tamba Species 0.000 description 1
- 239000005862 Whey Substances 0.000 description 1
- 102000007544 Whey Proteins Human genes 0.000 description 1
- 108010046377 Whey Proteins Proteins 0.000 description 1
- 239000012620 biological material Substances 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000012937 correction Methods 0.000 description 1
- 238000003977 dairy farming Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000012994 industrial processing Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000009916 joint effect Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 235000020183 skimmed milk Nutrition 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 230000009469 supplementation Effects 0.000 description 1
- 238000012549 training Methods 0.000 description 1
- 230000002747 voluntary effect Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/38—Treatment of water, waste water, or sewage by centrifugal separation
- C02F1/385—Treatment of water, waste water, or sewage by centrifugal separation by centrifuging suspensions
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L3/00—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs
- A23L3/005—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs by heating using irradiation or electric treatment
- A23L3/01—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs by heating using irradiation or electric treatment using microwaves or dielectric heating
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L3/00—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs
- A23L3/40—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs by drying or kilning; Subsequent reconstitution
- A23L3/48—Thin layer-, drum- or roller-drying
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/16—Evaporating by spraying
- B01D1/18—Evaporating by spraying to obtain dry solids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B5/00—Other centrifuges
- B04B5/10—Centrifuges combined with other apparatus, e.g. electrostatic separators; Sets or systems of several centrifuges
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B5/00—Drying solid materials or objects by processes not involving the application of heat
- F26B5/08—Drying solid materials or objects by processes not involving the application of heat by centrifugal treatment
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B7/00—Drying solid materials or objects by processes using a combination of processes not covered by a single one of groups F26B3/00 and F26B5/00
Abstract
(57)【要約】本公報は電子出願前の出願データであるため要約のデータは記録されません。 (57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】 液体まだはのり状の混合物の脱水方法とその装置本発明は、液体またはのり状の 混合物の脱水方法、特にかかる混合物を粉末またはや粒にするだめの脱水方法に 関するものである。本発明は、まだ、かかる方法を実施するため装置を含む0 種々の産業工程は一つまたは数種類の脱水工程を含む。たとえば粉末状または顛 粒状の最終製品を得たシ、または特定の汚染廃棄物を処理するためなどである。[Detailed description of the invention] A method and apparatus for dehydrating a liquid or paste-like mixture A method of dehydrating a mixture, especially a method of dehydrating such a mixture into powder or granules. It is related to The present invention still includes an apparatus for carrying out such a method. Various industrial processes include one or several types of dewatering steps. For example, powdered or For example, to obtain granular final products or to treat certain contaminated wastes.
いずれの場合においても、除去すべき水の量が多いと極めて大量のエネルギーが 消費される。本発明の脱水方法は、エネルギー効率が非常に良いだめ工業レベル での応用が可能であると共に、特にその高い効率のために実験室レベルや小量生 産(製菓業における)にも応用可能である。In either case, the large amount of water to be removed requires extremely large amounts of energy. consumed. The dehydration method of the present invention is very energy efficient and can be used at industrial level. It is particularly suitable for laboratory-level and small-scale production applications due to its high efficiency. It can also be applied to the confectionery industry.
この趣旨において、本発明は、液体またはのシ状の混合物にマイクロ波と遠心力 とを同時に作用させることを特徴とする、液体またはのり状の混合物の脱水方法 に関するものである。To this effect, the present invention provides a method for applying microwave and centrifugal force to liquid or cylindrical mixtures. A method for dehydrating a liquid or paste-like mixture, characterized by the simultaneous action of It is related to.
上記に定義した脱水方法の最良の実施例において、混合物はマイクロ波放射装置 のまわりに非常に均一に粉砕、分配され、混合物の最も重い組成物を分離する遠 心分離工程中において、マイクロ波が混合物に対して最も効果的に作用できるよ うにする。In the best embodiment of the dehydration method defined above, the mixture is heated in a microwave radiator. It is very evenly milled and distributed around the During the heart separation process, microwaves can be used to work most effectively on the mixture. I will do it.
本発明は、また、対称軸のまわりを回転するように取付けられ前記混合物を受け 入れるだめの処理槽、この処理槽を回転するだめの装置、および前記処理槽内に 沈められた少くとも1基のマイクロ波発生器とから成ることを特徴とする、液体 またはの)状の混合物の脱水装置にも関するものである。The invention also provides a method for receiving said mixture mounted for rotation about an axis of symmetry. A processing tank to be placed in, a device for rotating this processing tank, and a device inside the processing tank. and at least one submerged microwave generator. The present invention also relates to a dehydrating device for a mixture of (or).
一つの実施例によれば、処理槽の回転軸は中空であり、マイクロ波発生器を収容 し効果的に保護することができる。According to one embodiment, the rotating shaft of the treatment tank is hollow and houses a microwave generator. and can be effectively protected.
他の実施例によれば、マイクロウェーブ発生器゛は処理槽の下部の中央に処理槽 の回転軸の延長にもうけられたガラス管の中に収納されている。According to another embodiment, the microwave generator is located in the bottom center of the processing tank. It is housed in a glass tube that is an extension of the rotating shaft.
本発明は添付図面に関連してあくまで例示として示した、本発明の原理による脱 水装置の説明からより良く理解され、本発明のその他の特徴も明らかになるであ ろう。The present invention has been described by way of example only in conjunction with the accompanying drawings, in accordance with the principles of the invention. From the description of the water device, it will be better understood and other features of the invention will become apparent. Dew.
第1図は本発明による装置の概略かつ一部破断立面図である。FIG. 1 is a schematic and partially cut away elevational view of a device according to the invention.
第2図は第1図の線■−■における断面図、第3図は第1図に示した装置の製造 の一変形の一部破断した概略立面図、 第4図は液体混合物濃縮および乾燥工程における第3図の装置の据付の実施例を 示す概略側立面図、である。Figure 2 is a sectional view taken along the line ■-■ in Figure 1, and Figure 3 is the manufacturing of the device shown in Figure 1. Schematic elevational view, partially broken away, of a variant of Figure 4 shows an example of the installation of the apparatus of Figure 3 in a liquid mixture concentration and drying process. FIG. 2 is a schematic side elevation view.
第1図において、装置は、中空の軸12により形成された左右対称軸のまわりに 回転するように取付けられた処理槽11、および処理槽11の中に沈められた、 捷だ特殊な構成においては中空軸12の中にもうけられたマイクロ波発生器13 .14.15 (通常「マグネトロン」と称する)から主として成っている。中 空軸12は、フレーム16の軸受16aおよび16bにより垂直位置に維持され ている。In FIG. 1, the device is arranged around an axis of symmetry formed by a hollow shaft 12. A processing tank 11 mounted to rotate, and a processing tank submerged in the processing tank 11. In a special configuration, a microwave generator 13 is installed in the hollow shaft 12. .. 14.15 (usually referred to as a "magnetron"). During ~ The empty shaft 12 is maintained in a vertical position by bearings 16a and 16b of the frame 16. ing.
ここに示した実施例では、処理槽11は、それぞれのベースによシ組立てられた 2個の同心の円錐形部分17および18がら主として成る。下側の円錐形部分1 7は朝顔形に非常に広がっており、処理する混合物のだめの容器を形成している 。混合物は下部パイプ19を通して送り込まれ、軸12のまわりに形成された環 状空間20を通って円錐形部分17に投入される。In the embodiment shown here, the treatment tanks 11 are assembled on their respective bases. It mainly consists of two concentric conical sections 17 and 18. Lower conical part 1 7 is very spread out in the shape of a morning glory and forms a reservoir for the mixture to be processed. . The mixture is fed through the lower pipe 19 and passes through the ring formed around the shaft 12. It enters the conical part 17 through the shaped space 20.
この環状空間は、パイプ19が開口している固定された下部カラー21と、処理 槽11と一体になっておシ横穴がもうけられた上部カラー22とにより形成され 、その内径は固定カラーの外径に合わせて調節されている。半径方向の仕切壁2 3が中空軸12の内部に固着されておシ、円錐形部分17および18の2枚の組 立フランジ17aおよび18aの外側の間に挿入されている。これにより処理槽 11が回転される。この仕切壁の外縁付近にもうけられた大きな開口24により 、混合物が遠心力で装置の上部へ送られる。スリーブ29により形成され処理槽 の上部にもうけられた上部軸受25により、処理槽が軸12のまわりを回転する 際の安定性が向上する。This annular space has a fixed lower collar 21 into which the pipe 19 opens and a processing It is formed by the upper collar 22 which is integrated with the tank 11 and has a side hole. , whose inner diameter is adjusted to the outer diameter of the fixed collar. Radial partition wall 2 3 is fixed inside the hollow shaft 12, and a set of two conical parts 17 and 18 is formed. It is inserted between the outsides of vertical flanges 17a and 18a. This allows the processing tank to 11 is rotated. Due to the large opening 24 made near the outer edge of this partition wall, , the mixture is sent to the top of the device by centrifugal force. A processing tank formed by the sleeve 29 The processing tank rotates around the shaft 12 by an upper bearing 25 provided at the upper part of the tank. Improved stability during operation.
らせんスクリューコンベヤ28を形成する搬送装置が処理槽うになっている。こ のだめには、らせんスクリューコンベヤを形成する前記装置は、軸12に取付け られたスリーブ29に連結されており、軸12は処理槽の上に突出しており、そ れにはベルト31によって駆動される滑車30が取付けられている。The conveying device forming the spiral screw conveyor 28 serves as a processing tank. child In Nodame, said device forming a helical screw conveyor is mounted on the shaft 12. The shaft 12 protrudes above the processing tank, and the shaft 12 is connected to a sleeve 29 that is A pulley 30 driven by a belt 31 is attached to this.
さらに、処理槽11を回転させるための装置がスリーブ29の上方に軸12に取 付けられ、もう一つのベルト33により、M動される滑車22を含む。ベルト3 1および33は平行であり、同じモータ (図示しない)に取付けられている。Further, a device for rotating the processing tank 11 is attached to the shaft 12 above the sleeve 29. It includes a pulley 22 which is attached and moved by another belt 33. belt 3 1 and 33 are parallel and attached to the same motor (not shown).
処理槽とらせんスクリューコンベヤを形成する搬送装置との間の回転速度の差は 、滑車30と32の直径に若干の差異をもうけることにより決定することができ る。らせんスクリューコンベヤを形成するこの搬送装置は全体的にかご形であり 、その縦柱35は、処理槽の内側壁面の方向に突出し、処理に際して混合物の最 も粗大な部分を装置の頂上に向ってゆっくりと運ぶことができるらせん通路を形 成しているブレード36に取付けられている。上部横材37aは柱35をスリー ブ29に対して剛性的に連結し、下部横材37bは該柱を下方に取付けられた軸 受37cに剛性的に連結して軸12のまわシを回転するようにしている。乾燥し た製品を排出するための装置が処理槽の上部に取付けられている。それは、処理 槽11の上部を取囲んでいる輪状の容器38と該容器から延びる排出パイプ39 とから成る。それに関して、処理槽は、らせんスクリューコンベヤ28を形成す る搬送装置の上部付近に位置され容器38の中へ開いている数個の横穴40を含 む。この搬送装置28は円錐形表面27と協力するので、類似した全体形状を有 している。即ち柱35は中空の軸12と同心の、仮想の切断された円錐筒上に規 則的に間隔をおいてもうけられている。軸12は二つの部分に分れている。即ち 、貿下部42は軸のこの空間に軸方向に整列されたマイクロ波発生器を収納して おり、上部43 (部分44によシ部分42から隔離されている)はフレーム1 6の上方において処理槽の外側へ延び、かつ処理槽内に開口する横穴45を含み 、混合物の処理中に生じるガスや水蒸気を排出する手段を形成している。従って 上部43は吸引装置47を備えた排出管46に終っている。The difference in rotational speed between the processing tank and the conveying device forming the helical screw conveyor is , can be determined by making a slight difference in the diameters of pulleys 30 and 32. Ru. This conveying device, which forms a helical screw conveyor, is generally cage-shaped. , the vertical column 35 protrudes in the direction of the inner wall surface of the treatment tank, and the vertical column 35 is arranged to It also forms a spiral passageway that allows coarse parts to be carried slowly towards the top of the device. It is attached to the blade 36 which is made of The upper horizontal member 37a connects the pillar 35 with three The lower cross member 37b connects the column rigidly to the shaft 29 mounted below. It is rigidly connected to the receiver 37c so that the shaft 12 can be rotated. dry A device is installed at the top of the treatment tank for discharging the product. It is processing A ring-shaped container 38 surrounding the upper part of the tank 11 and a discharge pipe 39 extending from the container It consists of In that regard, the treatment tank forms a helical screw conveyor 28. It includes several lateral holes 40 located near the top of the conveyor and opening into the container 38. nothing. This conveying device 28 cooperates with the conical surface 27 and therefore has a similar overall shape. are doing. That is, the pillar 35 is defined on an imaginary truncated conical cylinder concentric with the hollow shaft 12. It is produced at regular intervals. The shaft 12 is divided into two parts. That is, , the lower part 42 accommodates microwave generators aligned in the axial direction in this space of the shaft. The upper part 43 (separated from the upper part 42 by a part 44) is attached to the frame 1. 6, including a horizontal hole 45 extending to the outside of the processing tank and opening into the processing tank. , forming means for discharging gases and water vapor generated during processing of the mixture. Therefore The upper part 43 ends in a discharge pipe 46 with a suction device 47.
マイクロ波発生装置13.14.15は軸12の下端を貫通している電線48に よシ給電される。開口49が各発生器に面して軸12に横方向にもうけられ、こ れらの開口は内側壁面27およびらせんスクリューコンベヤ28を形成する搬送 装置に面する中空の案内部50によシ半径方向に延びている。The microwave generator 13.14.15 is connected to a wire 48 passing through the lower end of the shaft 12. Power is supplied. An aperture 49 is provided laterally in the shaft 12 facing each generator; These openings form an inner wall 27 and a conveying screw conveyor 28. It extends radially through a hollow guide 50 facing the device.
本発明の装置の作用は次の通りである。即ち、処理しようとする混合物を処理槽 の円錐形部分17により形成された容器に連続的に送り込みながら処理槽11を 回転させマイクロ波発生器に通電する。遠心力により混合物は搬送装置28の底 部へ連続的に移動する。らせんスクリューコンベヤの働きによシこの混合物はマ イクロ波発生器13.14.15のまわりに比較的薄い層となって分散されなが ら処理槽の上部へゆっくりと移動する。混合物が絶えず砕かれながら上昇し同時 に内側壁面27の近くでは薄い層に維持されるので発生器により維持される熱は 最大限の効率をもって混合物に作用する。発生した水蒸気はダクト46と吸引装 置47とにより開口45を通って吸引され排出される。乾燥した製品は容器38 に入シノシイプ39によシ排出される。The operation of the device of the invention is as follows. In other words, the mixture to be treated is placed in a treatment tank. The processing tank 11 is continuously fed into the container formed by the conical part 17 of the Rotate and energize the microwave generator. Centrifugal force forces the mixture to the bottom of the conveyor 28. Continuously move to the next section. Due to the action of the helical screw conveyor, this mixture It is not dispersed in a relatively thin layer around the microwave generator 13.14.15. slowly move it to the top of the treatment tank. The mixture rises while being constantly broken down and at the same time Since the heat maintained by the generator is maintained in a thin layer near the inner wall surface 27, Act on the mixture with maximum efficiency. The generated water vapor is transferred to the duct 46 and the suction device. It is sucked through the opening 45 by the holder 47 and discharged. Dry product is in container 38 It enters and is discharged by the pipe 39.
第3図は第1図の装置の一変形を示し、これによればマイクロ波の作用が処理槽 の内面全体におよび、それによシ、遠心力とマイクロ波との共同作用が最良の脱 水効果を上げることができる。FIG. 3 shows a modification of the device shown in FIG. 1, according to which the action of microwaves is The joint action of centrifugal force and microwaves is the best way to remove You can increase the water effect.
この目的のために、マイクロ波発生器に面して配置されたそれぞれの中空の案内 部が三角の断面を有する仕切環により分離された複数の傾斜した案内管を有する 。For this purpose, each hollow guide placed facing the microwave generator having a plurality of inclined guide tubes separated by partition rings with triangular cross-sections; .
この図に関し、第1図の部品と同じ部品は同一の参照番号に100を加えた番号 で示す。これにより参照が容易になるであろう。Regarding this figure, parts that are the same as those in Figure 1 have the same reference numbers plus 100. Indicated by This will make reference easier.
第3図に示すように、それぞれの中空案内部150は軸方向に拡がった形状を有 し、三角形断面の仕切環151によりよシ分離された数本の案内管150 a、 150 b、 150 cを有する。さらに、2個の軸方向に隣接した案内管 の間には、軸112の周縁にもうけられた、たとえば六角形の断面を有する横部 材152がもうけられる。分散用ブレード153.154が放射アンテナの近く で、案内部150の上下に配列される。As shown in FIG. 3, each hollow guide portion 150 has a shape that expands in the axial direction. However, several guide tubes 150a separated by a partition ring 151 with a triangular cross section, It has 150 b and 150 c. Furthermore, two axially adjacent guide tubes For example, a lateral part having a hexagonal cross section is formed on the periphery of the shaft 112 between the parts. Material 152 is produced. Dispersion blades 153, 154 near the radiating antenna and are arranged above and below the guide part 150.
このようにして、ハウジング111の壁127、横材152およびマイクロ波案 内部150に隣接する壁との間に共振室155が形成される。この包囲部155 を画定する表面部分は、アンテナ113および114から放射されるマイクロ波 を反射する材料で作ることが最も望ましい。アンテナから放射されたマイクロ波 はこのようにして案内管の出口150a、150b。In this way, the wall 127 of the housing 111, the cross member 152 and the microwave A resonant chamber 155 is formed between the interior 150 and an adjacent wall. This surrounding part 155 The surface portion defining the microwaves radiated from antennas 113 and 114 It is most desirable to make it from a reflective material. microwave radiated from antenna In this way, the exits 150a, 150b of the guide tubes.
150cにおいて多数の反射路に分れ、内壁127、横材152および案内部1 50の外壁に反射ししかもその強度が減少しない。その結果、処理槽の内周面に おいて遠心力の作用を受ける混合物に対しより均一にかつ広範囲に作用する。The inner wall 127, the cross member 152 and the guide part 1 are divided into a number of reflection paths at 150c. 50, and its intensity does not decrease. As a result, the inner peripheral surface of the treatment tank It acts more uniformly and over a wide range on the mixture that is subjected to centrifugal force.
三角形仕切環151は、放射されたマイクロ波をそれらが当ろうとする壁127 に関してはっきりとした傾斜方向を与えると共に、壁127とほぼ平行なその外 側面により、壁により反射されたマイクロ波を再び反射し、上記被処理混合物の 分散に参加することが判るであろう。The triangular partition ring 151 directs the emitted microwaves to the wall 127 that they are about to hit. giving a clear direction of inclination to The side surfaces re-reflect the microwaves reflected by the wall and cause the mixture to be treated. It will be seen that it participates in the distribution.
さらに、マイクロ波を反射するだめのすべての要素、特に案内部150、横材1 52および処理槽の内壁127は、ステンレス鋼のようなマイクロ波発生器即で 作られることが判るであろう。Furthermore, all the elements of the microwave reflecting vessel, in particular the guide part 150, the cross member 1 52 and the inner wall 127 of the treatment tank are made of microwave generator material such as stainless steel. You will see that it is made.
示された実施例において、マイクロ波発生器即ちマグネトロン113.114は 、中空軸112の中に入れられたガラス管156の中に固定されている。それら は、まだ、回転可能に取付けることも可能であり、その場合はその給電は回転接 点ユニット (図示しない)で行う。In the embodiment shown, the microwave generator or magnetron 113,114 is , is fixed in a glass tube 156 placed within the hollow shaft 112. those can still be rotatably mounted, in which case its power supply can be connected to a rotating connection. This is done using a point unit (not shown).
マイクロ波発生器により発生されたマイクロ波が無用に外部に放散しないように 、遮蔽板157をもうけマイクロ波を装置内に密閉する。それはガラス管156 の内部に、かつ中空軸112の遠方端部143に横方向に配置される。To prevent the microwaves generated by the microwave generator from being dissipated to the outside unnecessarily. , a shielding plate 157 is provided to seal the microwave inside the device. It is glass tube 156 and laterally disposed within the distal end 143 of the hollow shaft 112 .
第4図はへどろや液状混合物を濃縮、乾燥するだめの工程における本発明の脱水 装置の利用を示す。未処理の製品はパイプ202を通って貯蔵タンクまたは緩衝 装置203に送られ、その底部から排出されてポンプ204により遠心力および 超音波作用を有する分離濃縮装置205へ送られる。この装置において分離され た組成水はパイプ207により排出されて再使用゛される。この装置205の濃 縮物出口からポンプ206により本発明の脱水装置208に濃縮物が送られる。Figure 4 shows the dehydration process of the present invention in the process of concentrating and drying sludge and liquid mixtures. Indicates the use of the device. Unprocessed product passes through pipe 202 to a storage tank or buffer. It is sent to the device 203 and discharged from the bottom of the device and is subjected to centrifugal force and by the pump 204. It is sent to a separation/concentration device 205 that has an ultrasonic effect. This device separates The composed water is discharged through a pipe 207 and reused. The concentration of this device 205 From the condensate outlet, a pump 206 sends the concentrate to a dewatering device 208 of the present invention.
乾燥された製品は、その終端がコンベヤベルト210において終っている傾斜パ イプ209から出てくる。水蒸気はもう一つのパイプ211によって排出される 。コンベヤベル)210は乾燥製品の状態次第によりらせんスクリューコンベヤ に代えることができる。The dried product is transferred to an inclined track terminating in a conveyor belt 210. It comes out from Ip209. Water vapor is exhausted by another pipe 211 . Conveyor Bell) 210 is a helical screw conveyor depending on the condition of the dried product. It can be replaced by
上に説明した装置は多くの用途に有利に使用することができる。まず、食料品産 業においては、屠殺場において血液の回収に利用することができる。特にたんば く質に富む原材料となる粉末を調製するためである。同じ装置はまた酪農業にお いて乳精(「脱脂乳」という名の方が良く知られている)の加工に使用される。The device described above can be used advantageously in many applications. First, food products In industry, it can be used to collect blood at slaughterhouses. Especially Tamba This is to prepare a powder that is a raw material rich in texture. The same equipment is also used in dairy farming. It is used in the processing of whey (better known as 'skimmed milk').
汚物処理工場においては、へどろをこの装置によシ処理することにより応用生物 学肥料およびまたは応用生物学ガスの製造のだめの原料が供給される。廿菜の工 業的処理から生じる廃棄物の乾燥もこのような装置により可能になるであろう。At sewage treatment plants, sludge is treated with this device to produce applied biological materials. The raw materials for the production of biological fertilizers and/or applied biological gases are supplied. Haruna's work Drying of wastes resulting from industrial processing would also be possible with such a device.
最後に、本発明の装置のうち処理能力の小さいものは、製菓業および実験室にお ける多数の需量に応じることができるであろう0 本発明は上記に説明した実施例に限定されるものではなく、当業者が自己の通常 の知識の範囲内で行うことが出来る変更を含むものである。Finally, the low throughput devices of the invention are suitable for confectionery industries and laboratories. 0 The present invention is not limited to the embodiments described above, and those skilled in the art will It includes such changes as may be made within the knowledge of the person concerned.
第3図 第4図 手続補正書(自発) 配j ill 59手6月IS″日 PCT/FR83100202 事件との関係 特許出願人 7、補正の対象 (1)明細書の翻訳文および請求の範囲の翻訳文& M正の内容 9、添付書類の目録 (1)明細書の翻訳文 1 通 (2)請求の範囲の翻訳文 1 通 特許出願代理人 手続補正書(方式) %式% 3、 補正をする者 事件との関係 特許出願人 、補正命令の日付 昭和59年8月2日 (発送日・昭和59年8月7日)、 補正により増加する発明の数 (1)図面の翻訳文の浄書(内容に変更なし)。Figure 3 Figure 4 Procedural amendment (voluntary) Ill 59 moves June IS'' day PCT/FR83100202 Relationship to the incident: Patent applicant 7. Subject of correction (1) Translation of the specification, translation of the scope of claims & contents of the original statement 9. List of attached documents (1) Translation of the specification: 1 copy (2) Translation of the scope of claims: 1 copy patent application agent Procedural amendment (formality) %formula% 3. Person making the amendment Relationship to the incident: Patent applicant , Date of amendment order: August 2, 1980 (Shipping date: August 7, 1980), Number of inventions increased by amendment (1) Engraving of the translation of the drawing (no changes to the content).
(2)委任状および同訳文の補充。(2) Supplementation of power of attorney and its translation.
9、添付書類の目録 (1)図面の翻訳文 1 通 (2)委任状および同訳文 各 1 連取上 国際調沓卸失9. List of attached documents (1) One translation of the drawing (2) Power of attorney and the same translation (one series each) Loss of international training
Claims (1)
Applications Claiming Priority (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR8216647A FR2534009B1 (en) | 1982-10-05 | 1982-10-05 | PROCESS FOR DRYING A LIQUID OR PASTY MIXTURE AND APPARATUS FOR CARRYING OUT SAID METHOD |
FR8315729A FR2552864B2 (en) | 1982-10-05 | 1983-10-03 | PROCESS FOR DRYING A LIQUID OR PASTY MIXTURE AND APPARATUS FOR CARRYING OUT SAID METHOD |
FR83/15729DK | 1983-10-03 | ||
FR82/16647DK | 1983-10-03 | ||
PCT/FR1983/000202 WO1984001307A1 (en) | 1982-10-05 | 1983-10-05 | Method and apparatus for drying a liquid or pasty mixture |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS59501939A true JPS59501939A (en) | 1984-11-22 |
Family
ID=26223089
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP83503147A Pending JPS59501939A (en) | 1982-10-05 | 1983-10-05 | Method and equipment for dehydrating liquid or pasty mixtures |
Country Status (7)
Country | Link |
---|---|
JP (1) | JPS59501939A (en) |
CH (1) | CH658902A5 (en) |
DE (1) | DE3390232T1 (en) |
FR (1) | FR2552864B2 (en) |
NL (1) | NL8320304A (en) |
SE (1) | SE452055B (en) |
WO (1) | WO1984001307A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108975557A (en) * | 2018-08-15 | 2018-12-11 | 王晓勇 | A kind of sewage disposal device |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0306563B1 (en) * | 1987-09-10 | 1991-03-06 | Hosokawa Micron Europe B.V. | Apparatus for drying material which is mixed with a solvent |
FR2638660B1 (en) * | 1988-11-10 | 1990-12-21 | Armorique Sa Const Meca | MIXER, PARTICULARLY FOR THE TREATMENT OF POWDER PRODUCTS |
WO2008155775A2 (en) * | 2007-06-20 | 2008-12-24 | Microcoal Inc. | Method and system for water vaporization |
US9925694B2 (en) * | 2009-02-24 | 2018-03-27 | Gala Industries, Inc. | Continuous bagging processes and systems |
CN106556216B (en) * | 2016-10-17 | 2019-01-04 | 无锡市日升化工有限公司 | A kind of PVC auxiliary agent dryer integrating microwave drying and gas drying |
EP3480542A1 (en) * | 2017-11-03 | 2019-05-08 | Nordson Corporation | Separator for separating a mixture of a solid substance and a fluid |
CN108285261B (en) * | 2018-03-20 | 2024-02-06 | 中国石油大学(北京) | Device for treating oily sludge by microwaves and treatment method thereof |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1034585B (en) * | 1955-09-27 | 1958-07-24 | Justus Theegarten O H G | Process and device for evaporation of liquids |
DE2409502B2 (en) * | 1974-02-28 | 1976-09-02 | Feres, Vaclav, Dipl.-Ing., 7500 Karlsruhe | THIN FILM EVAPORATOR |
FR2375046A1 (en) * | 1976-12-21 | 1978-07-21 | Controle Automation | Elimination of water from printing ink - by passing thin film of ink through a high frequency electromagnetic field |
US4313786A (en) * | 1979-07-23 | 1982-02-02 | Smith Jerold B | Magnetron solvent recovery system |
US4313798A (en) * | 1980-06-17 | 1982-02-02 | Lakehurst Galleries, Ltd. | Micro-wave powered distillation unit |
-
1983
- 1983-10-03 FR FR8315729A patent/FR2552864B2/en not_active Expired
- 1983-10-05 CH CH281784A patent/CH658902A5/en not_active IP Right Cessation
- 1983-10-05 WO PCT/FR1983/000202 patent/WO1984001307A1/en active Application Filing
- 1983-10-05 DE DE19833390232 patent/DE3390232T1/en not_active Withdrawn
- 1983-10-05 JP JP83503147A patent/JPS59501939A/en active Pending
- 1983-10-05 NL NL8320304A patent/NL8320304A/en unknown
-
1984
- 1984-06-05 SE SE8403023A patent/SE452055B/en not_active IP Right Cessation
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108975557A (en) * | 2018-08-15 | 2018-12-11 | 王晓勇 | A kind of sewage disposal device |
CN108975557B (en) * | 2018-08-15 | 2021-05-21 | 山西科润得生态环境科技有限公司 | Sewage treatment equipment |
Also Published As
Publication number | Publication date |
---|---|
CH658902A5 (en) | 1986-12-15 |
SE8403023L (en) | 1984-06-05 |
NL8320304A (en) | 1984-09-03 |
SE452055B (en) | 1987-11-09 |
WO1984001307A1 (en) | 1984-04-12 |
SE8403023D0 (en) | 1984-06-05 |
DE3390232T1 (en) | 1985-06-13 |
FR2552864B2 (en) | 1987-06-12 |
FR2552864A2 (en) | 1985-04-05 |
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