JPS5912260B2 - Method for removing pest control agents from vegetable solids used in food - Google Patents

Method for removing pest control agents from vegetable solids used in food

Info

Publication number
JPS5912260B2
JPS5912260B2 JP49076232A JP7623274A JPS5912260B2 JP S5912260 B2 JPS5912260 B2 JP S5912260B2 JP 49076232 A JP49076232 A JP 49076232A JP 7623274 A JP7623274 A JP 7623274A JP S5912260 B2 JPS5912260 B2 JP S5912260B2
Authority
JP
Japan
Prior art keywords
zone
pest control
fluid
solid
control agents
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
Application number
JP49076232A
Other languages
Japanese (ja)
Other versions
JPS5036654A (en
Inventor
レオンハルト ミヒアエル
フロ−リン ゲルト
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.)
Sulzer Escher Wyss AG
Original Assignee
Escher Wyss AG
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 Escher Wyss AG filed Critical Escher Wyss AG
Publication of JPS5036654A publication Critical patent/JPS5036654A/ja
Publication of JPS5912260B2 publication Critical patent/JPS5912260B2/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • B01J8/36Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed through which there is an essentially horizontal flow of particles
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, 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
    • A23L5/00Preparation or treatment of foods or foodstuffs, in general; Food or foodstuffs obtained thereby; Materials therefor
    • A23L5/20Removal of unwanted matter, e.g. deodorisation or detoxification
    • A23L5/21Removal of unwanted matter, e.g. deodorisation or detoxification by heating without chemical treatment, e.g. steam treatment, cooking
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/90Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in food processing or handling, e.g. food conservation
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P60/00Technologies relating to agriculture, livestock or agroalimentary industries
    • Y02P60/80Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
    • Y02P60/87Re-use of by-products of food processing for fodder production

Description

【発明の詳細な説明】 本発明は有害生物防除剤たとえば殺虫剤および農薬を食
料に使用される固体たとえば穀類、ふすま、落花生の殻
から除去する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for removing pest control agents such as insecticides and pesticides from solids used in food such as cereals, bran and peanut shells.

とくにふすま、落花生の殻などは農業で家畜の食料にい
わゆる添加飼料として添加される。
In particular, bran and peanut shells are added to livestock food as additive feed in agriculture.

食料への要求が高い限り、たとえば牛の飼料の場合、固
体に残る有害生物防除剤は許容されない。
As long as food demands are high, for example in the case of cattle feed, pesticides that remain in solid form are not tolerated.

本発明の目的は有害生物防除剤を確実に、簡単に固体か
ら除去する方法を得ることである。
The object of the present invention is to provide a method for reliably and easily removing pest control agents from solids.

この目的は本発明により流動状態の固体を通して、有害
生物防除剤が固体から蒸発され、かつ(または)蒸り流
によって運び去られる温度および水分を有する蒸気を流
すことによって解決される。
This object is solved according to the invention by flowing a steam through the solid in a fluidized state at a temperature and moisture such that the pesticidal agent is evaporated from the solid and/or carried away by the steam stream.

とくに有利な方法は流動状態の固体を前進させ、前進方
向に相接する2つのゾーン内で蒸気を貫流させ、2つの
ゾーンのうちの第1ゾーンのキャリヤ流体としてガスお
よび蒸気を使用し、その際固体は固体に凝縮する蒸気に
よって加熱され、ガスによって浮遊状態に保持され、か
つ第2ゾーンのキャリヤ流体として蒸気を使用すること
よりなる。
A particularly advantageous method advances a solid in a fluidized state, with steam flowing through it in two adjoining zones in the direction of advancement, using gas and steam as carrier fluids in the first of the two zones, and The solid is heated by the vapor condensing into a solid, kept in suspension by the gas, and the vapor is used as a carrier fluid in the second zone.

第2ゾーンのキャリヤ流体の少なくとも1部を循環的に
使用するのが有利である。
Advantageously, at least a portion of the carrier fluid of the second zone is used cyclically.

さらに第2ゾーンを去るキャリヤ流体の1部を第1ゾー
ンに導き、その際第2ゾーンを去るキャリヤ流体の1部
が第1ゾーンのキャリヤ流体の蒸気部分を形成するのが
有利である。
Furthermore, it is advantageous if a part of the carrier fluid leaving the second zone is conducted into the first zone, with the part of the carrier fluid leaving the second zone forming the vapor part of the carrier fluid of the first zone.

第2ゾーンのキャリヤ流体の温度および水分を、第2ゾ
ーンを去る固体が所望の水分を有するように制御するの
が有利である。
Advantageously, the temperature and moisture content of the carrier fluid in the second zone is controlled such that the solids leaving the second zone have the desired moisture content.

これらすべての手段はキャリヤ流体の通過孔を有する少
なくともはぼ水平の底板および底板の下にあるキャリヤ
流体の供給ボックスを有する水平の流動床装置によって
流動状態を発生させることによってとくに有利に実施す
ることができる。
All these measures are carried out particularly advantageously by generating the fluidized conditions by means of a horizontal fluidized bed device having at least a semi-horizontal bottom plate with passage holes for the carrier fluid and a supply box for the carrier fluid below the bottom plate. Can be done.

次に本発明を図面により説明する。Next, the present invention will be explained with reference to the drawings.

図示の装置により固体は蒸気処理の間流動状態に保持さ
れる。
The illustrated apparatus maintains the solids in a fluid state during steam processing.

固体を流動状態にするため装置は流動床装置1を有し、
この装置は流体の通過孔2を有する水平の底板3および
底板3の下にあるキャリヤ流体の供給ボックス4を備え
る。
For bringing the solid into a fluidized state, the device has a fluidized bed device 1;
The device comprises a horizontal bottom plate 3 with fluid passage holes 2 and a carrier fluid supply box 4 below the bottom plate 3.

処理する固体は流動床装置1に入口シュート5から供給
され、通過孔2から出る流体の作用によって底板3の上
に流動体6が形成され、ここで固定は浮遊状態に保たれ
、出口シュート7から流動床装置1を去る。
The solids to be treated are fed into the fluidized bed apparatus 1 through an inlet chute 5, and by the action of the fluid exiting from the passage holes 2 a fluid 6 is formed on the bottom plate 3, where the fixings are kept in suspension, and an outlet chute 7 It leaves the fluidized bed apparatus 1 from.

流動床6の上には流動床を去る流体のための吸出しフー
ド8がある。
Above the fluidized bed 6 is a suction hood 8 for the fluid leaving the fluidized bed.

供給ボックス4に配置された壁9および吸出しフード8
に配置された壁10によって流動床装置1は固体の前進
方向に相前後する2つのゾーン11および12に分割さ
れる。
Walls 9 and suction hood 8 arranged in supply box 4
The fluidized bed apparatus 1 is divided into two zones 11 and 12 one after the other in the direction of advancement of the solids by a wall 10 arranged at .

2つのゾーンのうちの第1のゾーン11は供給ボックス
4に開口する流体導入管13を有し、第2ゾーン12は
供給ボックス4に開口する流体導入管14を有する。
The first zone 11 of the two zones has a fluid introduction pipe 13 opening into the supply box 4 , and the second zone 12 has a fluid introduction pipe 14 opening into the supply box 4 .

第1ゾーン11から吸出しフード8を去る流体の導出管
15が、第2シー712から吸出しフード8を去る流体
の導出管16が出る。
From the first zone 11 there is a conduit 15 for the fluid leaving the suction hood 8, and from the second sea 712 there is a conduit 16 for the fluid leaving the suction hood 8.

流体導入管13へ空気管17および蒸気管18が開口す
る。
An air pipe 17 and a steam pipe 18 open into the fluid introduction pipe 13 .

流体導入管13にブロア19および加熱器20が配置さ
れる。
A blower 19 and a heater 20 are arranged in the fluid introduction pipe 13 .

流体導出管15にダスト分離器21が備えられ、そのダ
スト導出管22は入口シュート5に開口し、さらに流体
導出管15には流体の吸出しブロア23が配置される。
The fluid outlet pipe 15 is equipped with a dust separator 21, the dust outlet pipe 22 of which opens into the inlet chute 5, and the fluid outlet pipe 15 is further provided with a fluid suction blower 23.

第2ゾーン12の流体導出管16にはダスト分離器24
が備えられ、そのダスト導出管25は出口シュート7へ
開口する。
A dust separator 24 is provided in the fluid outlet pipe 16 of the second zone 12.
is provided, and its dust outlet pipe 25 opens to the outlet chute 7.

流体導出管16は流体導入管14へ開口し、この導管は
圧縮器26および加熱器27を備える。
The fluid outlet conduit 16 opens into the fluid inlet conduit 14, which conduit is equipped with a compressor 26 and a heater 27.

流体導出管16へ蒸気管28が開口する。A steam pipe 28 opens into the fluid outlet pipe 16 .

流体導入管14から蒸気管18が分岐する。A steam pipe 18 branches from the fluid introduction pipe 14 .

図示の装置において有害生物防除剤たとえば殺虫剤およ
び農薬を食料に使用する植物性固体たとえば穀類、ふす
ま、落花生の殻から除去する方法は下記のとおり行われ
る:流動床装置1内で固体を通して、有害生物防除剤が
固体から蒸発され、かつ(または)蒸気流によって運び
去られる温度および水分を有する蒸気が導かれる。
The method of removing pest control agents, such as insecticides and pesticides, from vegetable solids used in food, such as cereals, bran, peanut shells, in the illustrated apparatus is carried out as follows: in a fluidized bed apparatus 1, the solids are passed through the The biocontrol agent is evaporated from the solid and/or a vapor is introduced having a temperature and moisture that is carried away by the vapor stream.

この場合固体は蒸気処理の間流動床装置1の流動床6で
流動状態に保たれる。
In this case, the solids are kept in a fluidized state in the fluidized bed 6 of the fluidized bed apparatus 1 during the steam treatment.

固体は流動状態で流動床6内を前進し、固体の前進方向
に相前後する2つのゾーン11および12内で蒸気によ
って貫流される。
The solids advance in a fluidized state in the fluidized bed 6 and are passed through by steam in two zones 11 and 12 one behind the other in the direction of solids advancement.

第1ゾーン11のキャリヤ流体はガスおよび蒸気であり
、固体は固体に凝縮する蒸気によって加熱され、ガスに
よって浮遊状態に保たれる。
The carrier fluids in the first zone 11 are gas and vapor, and the solids are heated by the vapor which condenses into solids and are kept suspended by the gas.

第2ゾーン12のキャリヤ流体は蒸気である。The carrier fluid in second zone 12 is steam.

流動床6内で流動状態にある固体の蒸気凝縮による加熱
はきわめて迅速で正確な、固体の全粒子に均一に分布す
る加熱を可能にする。
Heating of the solid in fluidized state in the fluidized bed 6 by vapor condensation allows a very rapid, precise and uniformly distributed heating of all particles of the solid.

第1ゾーン11内のこの加熱の後、次の第2ゾーン12
内の蒸気処理も流動床6内の固体の流動状態のため固体
の全粒子にわたって均一に分布する。
After this heating in the first zone 11, the next second zone 12
The steam treatment within the fluidized bed 6 also results in uniform distribution over all particles of the solid due to the fluidized state of the solid within the fluidized bed 6.

固体の全粒子が確実に均一に処理されるため蒸気消費量
が小さくなり、処理時間が短縮される。
It ensures uniform treatment of all solid particles, resulting in lower steam consumption and shorter processing times.

第2ゾーン12のキャリヤ流体の大部分は導管16およ
び14により循環的に導かれる。
The majority of the carrier fluid in second zone 12 is conducted cyclically by conduits 16 and 14.

第2ゾーン12を流体導出管16から去る流体の1樹は
回路から取出され、蒸気管18により第1ゾーン11に
送られる。
The stream of fluid leaving the second zone 12 through the fluid outlet pipe 16 is taken out of the circuit and sent to the first zone 11 by the steam pipe 18.

第2ゾーン12のキャリヤ流体から分岐した部分は第1
ゾーン11内で第1ゾーン11のキャリヤ流体の蒸気部
分を形成する。
The portion of the second zone 12 branching off from the carrier fluid is
A vapor portion of the carrier fluid of the first zone 11 is formed within the zone 11 .

それによって装置は1つの蒸気入口すなわち蒸気管28
および1つの蒸気出口すなわち流体導出管15しか必要
としない。
Thereby the device has one steam inlet or steam pipe 28
and only one vapor outlet or fluid outlet tube 15 is required.

装置から出る蒸気は非常に少量である。Very little steam exits the device.

この量はもちろんすべての除去される有害生物防除剤を
連行しうる大きさでなければならない。
This amount must of course be large enough to entrain all of the pest control agent to be removed.

有害生物防除剤を有効に除去するにもかかわらず、装置
は非常に経済的に作動する。
Despite the effective removal of pest control agents, the device operates very economically.

次に本発明の思想および実施態様を列記する:1)有害
生物防除剤たとえば殺虫剤および農薬を食料に使用され
る植物性固体たとえば穀類、ふすま、落花生の殻から除
去する方法において、有害生物防除剤を固体から蒸発さ
せ、かつ(または)蒸気流によって運び出す温度および
水分を有する蒸気を、流動状態にある固体を通して流す
ことを特徴とする食料に使用する植物性固体から有害生
物防除剤を除去する方法。
The ideas and embodiments of the present invention are listed below: 1) A method for removing pest control agents, such as insecticides and pesticides, from vegetable solids used in food, such as grains, bran, and peanut shells. removing pest control agents from vegetable solids for use in foodstuffs, characterized in that a vapor having a temperature and moisture is passed through the solids in a fluid state to evaporate the agent from the solids and/or to carry them away by a vapor stream; Method.

2)固体を流動状態で前進運動させ、前進方向に相前後
する2つのゾーン内で蒸気を貫流させ、2つのゾーンの
第1のゾーンのキャリヤ流体としてガスおよび蒸気を使
用し、その際固体は固体に凝縮する蒸気によって加熱さ
れ、ガスによって浮遊状態に保持され、かつ第2ゾーン
のキャリヤ流体として蒸気を使用する上記1項の方法。
2) The solid is moved forward in a fluid state, with steam flowing through it in two zones one after the other in the direction of advancement, and gas and steam are used as carrier fluids in the first of the two zones, with the solid being 2. The method of claim 1, wherein the steam is heated by condensing into a solid, kept in suspension by the gas, and the steam is used as the carrier fluid in the second zone.

3)第2ゾーンのキャリヤ流体の少なくとも1部・ が
循環的に導かれる上記2項の方法。
3) The method of item 2 above, wherein at least a portion of the carrier fluid in the second zone is guided cyclically.

4)第2ゾーンを去るキャリヤ流体の1部を第1ゾーン
に導く上記2項の方法。
4) The method of item 2 above, in which a portion of the carrier fluid leaving the second zone is directed into the first zone.

5)第2ゾーンを去るキャリヤ流体の1部が第1ゾーン
のキャリヤ流体の蒸気部分を形成する上記4項の方法。
5) The method of paragraph 4, wherein a portion of the carrier fluid leaving the second zone forms the vapor portion of the carrier fluid of the first zone.

6)第2ゾーンのキャリヤ流体の温度および水分を、第
2ゾーンを去る固体が所望の水分を有するように制御す
る上記2項の方法。
6) The method of item 2 above, wherein the temperature and moisture content of the carrier fluid in the second zone is controlled such that the solids leaving the second zone have a desired moisture content.

7)キャリヤ流体の通過孔を有する少なくともほぼ水平
の底板および底板の下にあるキャリヤ流体の供給ボック
スを有する水平の流動床装置により流動状態を発生させ
る上記1項の方法。
7) The method of claim 1, wherein the fluidized conditions are generated by a horizontal fluidized bed apparatus having at least a substantially horizontal bottom plate with passage holes for the carrier fluid and a supply box for the carrier fluid below the bottom plate.

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

図面は本発明の方法を実施する流動床装置の縦断面図で
ある。 1・・・・・・流動床装置、3・・・・・・底板、5・
・・・・・入口シュート、6・・・・・・流動床、7・
・・・・・出口シュート、11・・・・・・第1ゾーン
、12・・・・・・第2ゾーン、17・・・・・・空気
管、28・・・・・・蒸気管。
The drawing is a longitudinal sectional view of a fluidized bed apparatus implementing the method of the invention. 1...Fluidized bed device, 3...Bottom plate, 5.
...Inlet chute, 6...Fluidized bed, 7.
...Exit chute, 11...First zone, 12...Second zone, 17...Air pipe, 28...Steam pipe.

Claims (1)

【特許請求の範囲】[Claims] 1 有害生物防除剤たとえば殺虫剤および農薬を食料に
使用される植物性固体たとえば穀類、ふすま、落下生の
殻から除去する方法において、有害生物防除剤を固体か
ら蒸発させ、かつ蒸気流によって運び出す温度および水
分を有する蒸気を、流動状態にある固体を通して流し、
その際流動状態を、キャリヤ流体のだめの通過孔を備え
る少なくともほぼ水平の底板および底板の下にあるキャ
リヤ流体の供給ボックスを有する少なくとも1つの水平
の流動床装置により発生させることを特徴とする食料に
使用する植物性固体から有害生物防除剤を除去する方法
1. The temperature at which the pest control agent is evaporated from the solid and carried away by the vapor stream in a process for removing pest control agents, such as insecticides and pesticides, from vegetable solids used in food, such as cereals, bran, and the shells of fallen plants. and steam containing water, flowing through the solid in a fluidized state,
The food product is characterized in that the fluidized state is generated by at least one horizontal fluidized bed device having an at least approximately horizontal bottom plate with passage holes for a carrier fluid reservoir and a supply box for the carrier fluid below the bottom plate. A method of removing pest control agents from the vegetable solids used.
JP49076232A 1973-07-05 1974-07-03 Method for removing pest control agents from vegetable solids used in food Expired JPS5912260B2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CH983973 1973-07-05
CH983973A CH560020A5 (en) 1973-07-05 1973-07-05

Publications (2)

Publication Number Publication Date
JPS5036654A JPS5036654A (en) 1975-04-05
JPS5912260B2 true JPS5912260B2 (en) 1984-03-22

Family

ID=4356211

Family Applications (1)

Application Number Title Priority Date Filing Date
JP49076232A Expired JPS5912260B2 (en) 1973-07-05 1974-07-03 Method for removing pest control agents from vegetable solids used in food

Country Status (7)

Country Link
JP (1) JPS5912260B2 (en)
AR (1) AR208513A1 (en)
BE (1) BE817016A (en)
CH (1) CH560020A5 (en)
FR (1) FR2235651B1 (en)
GB (1) GB1463598A (en)
NL (1) NL7409138A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61174170U (en) * 1985-04-19 1986-10-29

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DK150716C (en) * 1976-12-01 1987-10-26 Niro Atomizer As PROCEDURE FOR TREATING A POWDER OR PARTICULATED PRODUCT AND APPARATUS FOR USE IN EXERCISING THE PROCEDURE
CA1103087A (en) * 1977-07-05 1981-06-16 Michael F. Campbell Bland vegetable protein products and method of manufacture
JPH024476A (en) * 1988-06-21 1990-01-09 Tsutsunaka Plast Ind Co Ltd Manufacture of outdoor-light-antireflection light-transmittable body of synthetic resin having scratch-proof property

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3619201A (en) * 1967-10-24 1971-11-09 Univ California Pesticide decontamination of animal feed and foods

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3619201A (en) * 1967-10-24 1971-11-09 Univ California Pesticide decontamination of animal feed and foods

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61174170U (en) * 1985-04-19 1986-10-29

Also Published As

Publication number Publication date
AR208513A1 (en) 1977-02-15
BE817016A (en) 1974-10-16
JPS5036654A (en) 1975-04-05
GB1463598A (en) 1977-02-02
FR2235651A1 (en) 1975-01-31
CH560020A5 (en) 1975-03-27
FR2235651B1 (en) 1980-01-04
NL7409138A (en) 1975-01-07

Similar Documents

Publication Publication Date Title
AU711922B2 (en) Method and apparatus for preventing agglomeration
US4253825A (en) Grain drier
US3744145A (en) Organic waste dryer apparatus
US3861058A (en) Fluidized bed grain processor
CS271459B2 (en) Equipment for brown coal drying with large water content
US5133137A (en) Method and apparatus for heat treating a particulate product
KR850000204A (en) Continuous method for raising the grain
US4358341A (en) Spray dryer
KR960704470A (en) METHOD AND APPARATUS FOR PROCESSING FOOD PRODUCTS
US2062025A (en) Method and apparatus for treating moisture-containing substances
US4766912A (en) Method and apparatus for puffing tobacco
US4045879A (en) Process for treating oil containing vegetable raw materials
JPS5832711A (en) Method and apparatus for treating food processing article
US1528995A (en) Method and means for treating material
JPS5912260B2 (en) Method for removing pest control agents from vegetable solids used in food
US6631567B1 (en) Apparatus for removing a fluid component from particulized solid materials
US2096176A (en) Apparatus for drying and destroying sewage
US705787A (en) Process of deodorizing.
US1751552A (en) Method of and apparatus for drying wood pulp and the like
US2957519A (en) Spray drying apparatus and method
GB1101821A (en) Method of cooking grain and beans in a continuous way
IL44162A (en) Process and apparatus for treating oil-containing vegetable raw materials
US1927313A (en) Apparatus for drying starch
US3386716A (en) Apparatus for prefoaming of expandable synthetic resin such as styrene polymer composition containing a volatile organic liquid
US4112836A (en) Apparatus for treating oil containing vegetable raw materials