US3228454A - Process of drying mixtures on drying drums - Google Patents
Process of drying mixtures on drying drums Download PDFInfo
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- US3228454A US3228454A US296953A US29695363A US3228454A US 3228454 A US3228454 A US 3228454A US 296953 A US296953 A US 296953A US 29695363 A US29695363 A US 29695363A US 3228454 A US3228454 A US 3228454A
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- roller
- drying
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- dried
- layers
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Links
- 239000000203 mixture Substances 0.000 title description 23
- 238000001035 drying Methods 0.000 title description 22
- 238000000034 method Methods 0.000 title description 12
- 239000010410 layer Substances 0.000 description 53
- 239000002002 slurry Substances 0.000 description 17
- 239000000470 constituent Substances 0.000 description 16
- 239000000463 material Substances 0.000 description 10
- 241000209140 Triticum Species 0.000 description 7
- 235000021307 Triticum Nutrition 0.000 description 7
- 235000013312 flour Nutrition 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 235000013339 cereals Nutrition 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
- 244000299461 Theobroma cacao Species 0.000 description 4
- 235000009470 Theobroma cacao Nutrition 0.000 description 4
- 230000002411 adverse Effects 0.000 description 4
- 235000012907 honey Nutrition 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 235000013336 milk Nutrition 0.000 description 3
- 239000008267 milk Substances 0.000 description 3
- 210000004080 milk Anatomy 0.000 description 3
- 235000013311 vegetables Nutrition 0.000 description 3
- 229910001018 Cast iron Inorganic materials 0.000 description 2
- 229910001209 Low-carbon steel Inorganic materials 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 210000002969 egg yolk Anatomy 0.000 description 2
- 235000013601 eggs Nutrition 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 239000003925 fat Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000007790 scraping Methods 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 239000000341 volatile oil Substances 0.000 description 2
- VQJMAIZOEPPELO-KYGIZGOZSA-N (1S,2S,6R,14R,15R,16R)-5-(cyclopropylmethyl)-16-(2-hydroxy-5-methylhexan-2-yl)-15-methoxy-13-oxa-5-azahexacyclo[13.2.2.12,8.01,6.02,14.012,20]icosa-8(20),9,11-trien-11-ol hydrochloride Chemical compound Cl.CO[C@]12CC[C@@]3(C[C@@H]1C(C)(O)CCC(C)C)[C@H]1Cc4ccc(O)c5O[C@@H]2[C@]3(CCN1CC1CC1)c45 VQJMAIZOEPPELO-KYGIZGOZSA-N 0.000 description 1
- 241000251468 Actinopterygii Species 0.000 description 1
- 235000007319 Avena orientalis Nutrition 0.000 description 1
- 241000209763 Avena sativa Species 0.000 description 1
- 235000007558 Avena sp Nutrition 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- 240000007154 Coffea arabica Species 0.000 description 1
- 239000004278 EU approved seasoning Substances 0.000 description 1
- 240000005979 Hordeum vulgare Species 0.000 description 1
- 235000007340 Hordeum vulgare Nutrition 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 244000269722 Thea sinensis Species 0.000 description 1
- 235000008452 baby food Nutrition 0.000 description 1
- 235000012837 bread mixes Nutrition 0.000 description 1
- 235000013351 cheese Nutrition 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 235000016213 coffee Nutrition 0.000 description 1
- 235000013353 coffee beverage Nutrition 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 239000007857 degradation product Substances 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 235000019688 fish Nutrition 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 235000011194 food seasoning agent Nutrition 0.000 description 1
- 235000015203 fruit juice Nutrition 0.000 description 1
- 235000011389 fruit/vegetable juice Nutrition 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000012212 insulator Substances 0.000 description 1
- 235000021374 legumes Nutrition 0.000 description 1
- 235000013372 meat Nutrition 0.000 description 1
- 150000002736 metal compounds Chemical class 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000011241 protective layer Substances 0.000 description 1
- 235000015067 sauces Nutrition 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 235000014347 soups Nutrition 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 235000013616 tea Nutrition 0.000 description 1
- 238000009827 uniform distribution Methods 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
- 235000008939 whole milk Nutrition 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B17/00—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
- F26B17/28—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by rollers or discs with material passing over or between them, e.g. suction drum, sieve, the axis of rotation being in fixed position
- F26B17/284—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by rollers or discs with material passing over or between them, e.g. suction drum, sieve, the axis of rotation being in fixed position the materials being dried on the non-perforated surface of heated rollers or drums
- F26B17/286—Arrangements for application of materials to be dried onto the drums or rollers; Arrangements for removing dried materials from the drums or rollers, e.g. doctor blades
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B3/00—Drying solid materials or objects by processes involving the application of heat
-
- Y—GENERAL 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S159/00—Concentrating evaporators
- Y10S159/09—Two liquids dried simultaneously
Definitions
- This invention relates to an improved method of roller drying of mixtures, for example edible or pharmaceutical mixtures, containing one or more components which, in conventional methods of roller drying, may be adversely affected, for example, they may be subject to discolouration, decomposition or metallic contamination and hence liable to changes and loss of flavour and/or colour during the drying process.
- the rollers on which the mixtures are dried are usually of steel or cast iron but some of the difiiculties mentioned above occur irrespective of the metal of which the rollers are made. Once dried, the mixtures are removed from the surface of the roller usually by scraping with a doctor blade.
- the mixture to be dried contains one or more acids, then these frequently tend to react with the surface of the roller and thus the dried mix is contaminated with traces of metal compounds.
- Essential oils are frequently partially decomposed by direct heating and so if they are heated in direct contact with a hot metal surface their degradation products are frequently present in the dried material. This also occurs if the material to be dried contains some edible fat.
- roller drying causes a large surface area of the mix to be exposed to the atmosphere and if any component of the mix is oxi-dizable, then oxidation may occur.
- the material to be dried contains one or more volatile components then, in the processes of the prior art, there has frequently been loss of these components due to evaporation.
- the method according to the invention for producing, by roller drying, a dried mix containing one or more constituents liable to be adversely affected during the roller drying comprises forming a plurality of separate layers comprising the constituents of the mixture on the roller, allowing the layers to dry on the roller and removing the dried layers as a single film from the roller, and the method is characterised in that the constituents of the layers are chosen so that constituents liable to be affected adversely during the roller drying are shielded from conditions which would cause this to occur by one of the layers.
- each layer is formed on the roller by applying a slurry of the constituent or constituents of which it is composed and allowing the slurry to dry to form a layer impervious to the next layer being applied.
- the first layer should not be completely dry before the next layer is applied to it as, if it is, the heat of the roller transfers very rapidly to the layers being applied, with possible adverse etfects, such as volatile components evaporating rapidly.
- the first layers should act as an insulator. If, however, it was not dried appreciably, then it would not be impervious so that the layers would diffuse.
- a typical slurry being applied may have a water content of about 66% and in this case we find it satisfactory to dry the layer of it to a water content of about 25% before applying the next layer.
- the first layer will be of an inert material which substantially does not react with, or in the presence of, the surface of the roller under the conditions at which the process is carried and it is usually applied in the form of a solution or suspension in a carrier medium such as water.
- Suitable materials include, ground cereals, for example wheat, oat or barley flour. Vegetable tubers may sometimes be used, as they have a high starch content.
- the choice of the inert material depends largely upon what the other components of the resultant mix are. Apart from acting as a protective layer, this first layer must be, when dried, easily removable from the surface of the roller by, for example, scraping.
- this constituent my be applied in a second layer.
- Such constituents may also include, for example, juices, extracts or fine particles of fruit, vegetables, (for example tubers and legumes), meat, fish or cheese, or tea, coffee or cocoa.
- Other materials such as sugar, honey, essential oils, or seasonings may be added as desired.
- This second layer also frequently and advantageously contains an inert material such as that which comprises the first layer.
- the mix contains two or more constituents which would deteriorate if in contact before drying then these constituents are applied in separate layers which are kept apart by a layer to which both constituents are inert.
- fruit juice containing powders cakes and bread mixes
- omelette mixes vegetable powders as found in purees, for exam le for baby foods, soups, and sauces
- various pharmaceutical powdered mixes which may then be tabletted or capsulated.
- Apparatus for carrying out the process of the inven tion comprises a rotatable roller, which may be of, for example, steel or cast iron, and means for applying two or more separate layers to the roller, means for drying the layers on the roller and means for removing the dried layers from the roller.
- the means for applying the layers may comprise, for example, sprays, pumps, non-corrodible applicator rollers or combinations of these; alterna tively the roller may pass through a trough containing the material which is to comprise the first layer and then be coated with further layers by either of the previous means mentioned.
- twin rollers may be used in which case it is often convenient to feed the material which is to comprise the first layer between the rollers and then to apply the second or succeeding layers by any of the methods mentioned above which are suitable.
- the separation between the means for applying the separate layers may be adjusted to give the desired degree of drying of one layer before the next is applied.
- a means for controlling the thickness of one or more of the layers may conveniently be done by applying the layers by means of an applicator roller which is adjustable with a micrometer control to control its distance from the roller on which the layer is applied.
- the means for drying the layers on the roller preferably comprises means for passing steam through the roller.
- the means for removing the dried layers from the roller preferably comprises a doctor blade.
- Example 1 Steam is passed at a pressure of 50 lbs. p.s.i. through a roller of diameter 18 inches rotating at a speed of 3 r.p.m. A first layer 0.001 inch thick was applied by one applicator roll and a second layer, 0.006 inch thick,
- the slurry from which the first layer is derived is composed of 56% water and 44% wheatfiour and the slurry from which the second layer is derived is composed of 23.8% orange concentrate (73.8% solids), 14.2% honey (82% solids), 44.3% fresh eggs (yolk and white combined) (26.6% solids) and 17.7% Wheat flour. After drying for approximately 18 seconds the resultant dried mix was scraped oil by the doctor blade. Calculated on the dry solids, this mix contained 21.4% comminuted orange, 14.3% honey, 14.3% egg (yolk and white combined) and 50% wheat flour. This is used as a baby cereal.
- Example 2 An apparatus similar to that described in Example 1 is used with the modification that three applicator rollers are used, each spaced six inches apart.
- the first layer which consists of wheat flour is formed to a thickness of 0.001 inch by applying a wheat flour slurry containing 43% wheat flour and 57% water;
- the second layer which consists of cocoa is formed to a depth of approximately 0.003 inch by applying a slurry comprising 45% cocoa and 55% water
- the third layer, which consists of milk is formed to a depth of 0.002 inch by applying a milk concentrate comprising 53% milk solids and 47% water.
- the layers are dried for eighteen seconds and scraped off by a doctor blade.
- the resultant dried mix which is used as a baby-milk-cocoa cereal, contained 15% wheat flour, 45 cocoa and 40% whole milk.
- any suitable mixture for example pharmaceutical mixtures, may be dried in similar manner.
- a rotating drying roller 1 is heated by steam entering through pipe 2 and leaving by pipe 3.
- a layer is applied in contact with the roller by an applicator roll 4, which picks up slurry from a trough 5.
- a second layer is applied over this layer, after it has dried to some extent, by an applicator roll 6 which picks up slurry from a trough 7.
- the resultant film is removed by a scraper blade 8.
- a method of producing by roller drying a dried cereal mixture containing at least one constituent from the group consisting of acids and fats which is liable to deterioration by contact with a heated metal roller which comprises applying a first slurry of ground cereal substantially free of such constituents to a heated roller, drying said first slurry at least partly, and applying to the layer of said first slurry additional slurry containing such constituents to form at least one further layer, said first slurry being dried to a sufficient degree to form a distinct insulating layer indififusable with the additional slurry when such additional slurry is applied, allowing all of the layers to dry on the roller and removing the dried layers as a single film from the roller.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Microbiology (AREA)
- Drying Of Solid Materials (AREA)
- General Preparation And Processing Of Foods (AREA)
- Confectionery (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Description
Jan. 11, 1966 G. KETT 3,228,454
PROCESS OF DRYING MIXTURES ON DRYING DRUMS Filed July 23, 1965 A Horn e United States Patent 3,228,454 PROCESS OF DRYING MIXTURES ON DRYING DRUMS George Kett, Norwich, Norfolk, England, asslgnor to Reckitt & Colman (Overseas) Limited, Hull, England, a British company Filed July 23, 1963, Ser. No. 296,953 Claims priority, application Great Britain, July 25, 1962, 28,624/ 62 1 Claim. (Cl. 159-49) This invention relates to an improved method of roller drying of mixtures, for example edible or pharmaceutical mixtures, containing one or more components which, in conventional methods of roller drying, may be adversely affected, for example, they may be subject to discolouration, decomposition or metallic contamination and hence liable to changes and loss of flavour and/or colour during the drying process. The rollers on which the mixtures are dried are usually of steel or cast iron but some of the difiiculties mentioned above occur irrespective of the metal of which the rollers are made. Once dried, the mixtures are removed from the surface of the roller usually by scraping with a doctor blade.
If the mixture to be dried contains one or more acids, then these frequently tend to react with the surface of the roller and thus the dried mix is contaminated with traces of metal compounds. Essential oils are frequently partially decomposed by direct heating and so if they are heated in direct contact with a hot metal surface their degradation products are frequently present in the dried material. This also occurs if the material to be dried contains some edible fat.
The very nature of roller drying causes a large surface area of the mix to be exposed to the atmosphere and if any component of the mix is oxi-dizable, then oxidation may occur.
If the material to be dried contains one or more volatile components then, in the processes of the prior art, there has frequently been loss of these components due to evaporation.
The method according to the invention for producing, by roller drying, a dried mix containing one or more constituents liable to be adversely affected during the roller drying, comprises forming a plurality of separate layers comprising the constituents of the mixture on the roller, allowing the layers to dry on the roller and removing the dried layers as a single film from the roller, and the method is characterised in that the constituents of the layers are chosen so that constituents liable to be affected adversely during the roller drying are shielded from conditions which would cause this to occur by one of the layers.
Generally, in order to obtain uniform distribution, the constituents are applied to the roller in the form of slurries, generally in waters, it is preferred, therefore, that each layer is formed on the roller by applying a slurry of the constituent or constituents of which it is composed and allowing the slurry to dry to form a layer impervious to the next layer being applied.
It is desirable that the first layer should not be completely dry before the next layer is applied to it as, if it is, the heat of the roller transfers very rapidly to the layers being applied, with possible adverse etfects, such as volatile components evaporating rapidly. In other words, the first layers should act as an insulator. If, however, it was not dried appreciably, then it would not be impervious so that the layers would diffuse. For example, a typical slurry being applied may have a water content of about 66% and in this case we find it satisfactory to dry the layer of it to a water content of about 25% before applying the next layer.
The first layer will be of an inert material which substantially does not react with, or in the presence of, the surface of the roller under the conditions at which the process is carried and it is usually applied in the form of a solution or suspension in a carrier medium such as water. Suitable materials include, ground cereals, for example wheat, oat or barley flour. Vegetable tubers may sometimes be used, as they have a high starch content. The choice of the inert material depends largely upon what the other components of the resultant mix are. Apart from acting as a protective layer, this first layer must be, when dried, easily removable from the surface of the roller by, for example, scraping.
If the mix contains a constituent which would deteriorate if in contact with the roller, this constituent my be applied in a second layer. Such constituents may also include, for example, juices, extracts or fine particles of fruit, vegetables, (for example tubers and legumes), meat, fish or cheese, or tea, coffee or cocoa. Other materials, such as sugar, honey, essential oils, or seasonings may be added as desired. This second layer also frequently and advantageously contains an inert material such as that which comprises the first layer.
It the mix contains two or more constituents which would deteriorate if in contact before drying then these constituents are applied in separate layers which are kept apart by a layer to which both constituents are inert.
Among the many dried mixes which may result from the process of this invention may be mentioned fruit juice containing powders, cakes and bread mixes, omelette mixes, vegetable powders as found in purees, for exam le for baby foods, soups, and sauces, and various pharmaceutical powdered mixes, which may then be tabletted or capsulated.
Apparatus for carrying out the process of the inven tion comprises a rotatable roller, which may be of, for example, steel or cast iron, and means for applying two or more separate layers to the roller, means for drying the layers on the roller and means for removing the dried layers from the roller. The means for applying the layers may comprise, for example, sprays, pumps, non-corrodible applicator rollers or combinations of these; alterna tively the roller may pass through a trough containing the material which is to comprise the first layer and then be coated with further layers by either of the previous means mentioned. In a modification of this apparatus twin rollers may be used in which case it is often convenient to feed the material which is to comprise the first layer between the rollers and then to apply the second or succeeding layers by any of the methods mentioned above which are suitable. The separation between the means for applying the separate layers may be adjusted to give the desired degree of drying of one layer before the next is applied.
It is sometimes preferable to incorporate a means for controlling the thickness of one or more of the layers. This may conveniently be done by applying the layers by means of an applicator roller which is adjustable with a micrometer control to control its distance from the roller on which the layer is applied.
The means for drying the layers on the roller preferably comprises means for passing steam through the roller. The means for removing the dried layers from the roller preferably comprises a doctor blade.
The following examples illustrate some aspects of the invention.
Example 1 Steam is passed at a pressure of 50 lbs. p.s.i. through a roller of diameter 18 inches rotating at a speed of 3 r.p.m. A first layer 0.001 inch thick was applied by one applicator roll and a second layer, 0.006 inch thick,
was applied by a. second applicator roll, the two applicator rolls being 6 inches apart. The main roller, is of mild steel Whereas the applicator rolls are, for example, of fescolized or chromium plated mild steel. The slurry from which the first layer is derived is composed of 56% water and 44% wheatfiour and the slurry from which the second layer is derived is composed of 23.8% orange concentrate (73.8% solids), 14.2% honey (82% solids), 44.3% fresh eggs (yolk and white combined) (26.6% solids) and 17.7% Wheat flour. After drying for approximately 18 seconds the resultant dried mix was scraped oil by the doctor blade. Calculated on the dry solids, this mix contained 21.4% comminuted orange, 14.3% honey, 14.3% egg (yolk and white combined) and 50% wheat flour. This is used as a baby cereal.
Example 2 An apparatus similar to that described in Example 1 is used with the modification that three applicator rollers are used, each spaced six inches apart. The first layer, which consists of wheat flour is formed to a thickness of 0.001 inch by applying a wheat flour slurry containing 43% wheat flour and 57% water; the second layer which consists of cocoa is formed to a depth of approximately 0.003 inch by applying a slurry comprising 45% cocoa and 55% water and the third layer, which consists of milk, is formed to a depth of 0.002 inch by applying a milk concentrate comprising 53% milk solids and 47% water. The layers are dried for eighteen seconds and scraped off by a doctor blade. The resultant dried mix, which is used as a baby-milk-cocoa cereal, contained 15% wheat flour, 45 cocoa and 40% whole milk.
Although there has only been described in detail the drying of edible mixtures, any suitable mixture, for example pharmaceutical mixtures, may be dried in similar manner.
Typical apparatus, of the type used in Example 2, is
shown in the accompanying drawing. In this a rotating drying roller 1 is heated by steam entering through pipe 2 and leaving by pipe 3. A layer is applied in contact with the roller by an applicator roll 4, which picks up slurry from a trough 5. A second layer is applied over this layer, after it has dried to some extent, by an applicator roll 6 which picks up slurry from a trough 7. After being dried on the roller 1, the resultant film is removed by a scraper blade 8.
I claim:
A method of producing by roller drying a dried cereal mixture containing at least one constituent from the group consisting of acids and fats which is liable to deterioration by contact with a heated metal roller, which comprises applying a first slurry of ground cereal substantially free of such constituents to a heated roller, drying said first slurry at least partly, and applying to the layer of said first slurry additional slurry containing such constituents to form at least one further layer, said first slurry being dried to a sufficient degree to form a distinct insulating layer indififusable with the additional slurry when such additional slurry is applied, allowing all of the layers to dry on the roller and removing the dried layers as a single film from the roller.
References Cited by the Examiner UNITED STATES PATENTS 866,586 9/1907 Hussey 159-8 X 1,079,673 11/ 1913 Stieller 15911 1,200,116 10/1916 Johnson et al. 15912 X 1,519,561 12/1924 Sucharipa 15811 X 2,119,615 6/1938 Wendeborn 1598 X &92,041 2/ 1940 Headland 99204 2,879,163 3/1959 Anson et a1.
NORMAN YUDKOFF, Primary Examiner.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB28624/62A GB1047715A (en) | 1962-07-25 | 1962-07-25 | Improvements in the roller drying of mixtures |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3228454A true US3228454A (en) | 1966-01-11 |
Family
ID=10278540
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US296953A Expired - Lifetime US3228454A (en) | 1962-07-25 | 1963-07-23 | Process of drying mixtures on drying drums |
Country Status (2)
| Country | Link |
|---|---|
| US (1) | US3228454A (en) |
| GB (1) | GB1047715A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3494050A (en) * | 1967-12-14 | 1970-02-10 | Us Agriculture | Device and method for controlling bulk density of dehydrated foodstuffs |
| US3506447A (en) * | 1965-07-21 | 1970-04-14 | Gerber Prod | Method for preparing a fruit cereal product |
| US4654268A (en) * | 1984-03-15 | 1987-03-31 | Glaverbel | Transparent fire screening panels and their manufacture |
| US20080152760A1 (en) * | 2006-12-12 | 2008-06-26 | Spadaregrant Victoria | Grain-Based Powder |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US866586A (en) * | 1907-03-08 | 1907-09-17 | John M Hussey | Method of desiccating eggs. |
| US1079673A (en) * | 1912-12-28 | 1913-11-25 | Franz Friedrich Willy Stieler | Drying apparatus. |
| US1200116A (en) * | 1915-03-08 | 1916-10-03 | Mead Johnson & Co | Method for drying liquids. |
| US1519561A (en) * | 1923-06-28 | 1924-12-16 | Sucharipa Rudolph | Method and apparatus for drying alpha substance carried in alpha liquid |
| US2119615A (en) * | 1935-07-30 | 1938-06-07 | American Lurgi Corp | Process for drying substances in the condition of sludge and for evaporating solutions |
| US2192041A (en) * | 1938-06-07 | 1940-02-27 | Headland Olga | Method of treating and preparing vegetables |
| US2879163A (en) * | 1954-12-13 | 1959-03-24 | Lever Brothers Ltd | Method for preparing a meat-like product |
-
1962
- 1962-07-25 GB GB28624/62A patent/GB1047715A/en not_active Expired
-
1963
- 1963-07-23 US US296953A patent/US3228454A/en not_active Expired - Lifetime
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US866586A (en) * | 1907-03-08 | 1907-09-17 | John M Hussey | Method of desiccating eggs. |
| US1079673A (en) * | 1912-12-28 | 1913-11-25 | Franz Friedrich Willy Stieler | Drying apparatus. |
| US1200116A (en) * | 1915-03-08 | 1916-10-03 | Mead Johnson & Co | Method for drying liquids. |
| US1519561A (en) * | 1923-06-28 | 1924-12-16 | Sucharipa Rudolph | Method and apparatus for drying alpha substance carried in alpha liquid |
| US2119615A (en) * | 1935-07-30 | 1938-06-07 | American Lurgi Corp | Process for drying substances in the condition of sludge and for evaporating solutions |
| US2192041A (en) * | 1938-06-07 | 1940-02-27 | Headland Olga | Method of treating and preparing vegetables |
| US2879163A (en) * | 1954-12-13 | 1959-03-24 | Lever Brothers Ltd | Method for preparing a meat-like product |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3506447A (en) * | 1965-07-21 | 1970-04-14 | Gerber Prod | Method for preparing a fruit cereal product |
| US3494050A (en) * | 1967-12-14 | 1970-02-10 | Us Agriculture | Device and method for controlling bulk density of dehydrated foodstuffs |
| US4654268A (en) * | 1984-03-15 | 1987-03-31 | Glaverbel | Transparent fire screening panels and their manufacture |
| US20080152760A1 (en) * | 2006-12-12 | 2008-06-26 | Spadaregrant Victoria | Grain-Based Powder |
| US20110111114A1 (en) * | 2006-12-12 | 2011-05-12 | The Quaker Oats Company | Grain-Based Powder |
Also Published As
| Publication number | Publication date |
|---|---|
| GB1047715A (en) | 1966-11-09 |
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