USRE34237E - Banana processing - Google Patents
Banana processing Download PDFInfo
- Publication number
- USRE34237E USRE34237E US07/777,195 US77719591A USRE34237E US RE34237 E USRE34237 E US RE34237E US 77719591 A US77719591 A US 77719591A US RE34237 E USRE34237 E US RE34237E
- Authority
- US
- United States
- Prior art keywords
- banana
- pulp
- parenchyma
- chlorenchyma
- peel
- 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
Links
- 241000234295 Musa Species 0.000 title claims abstract description 190
- 235000018290 Musa x paradisiaca Nutrition 0.000 title claims abstract description 153
- 238000012545 processing Methods 0.000 title description 2
- 239000000686 essence Substances 0.000 claims abstract description 59
- 235000011389 fruit/vegetable juice Nutrition 0.000 claims abstract description 47
- 238000000034 method Methods 0.000 claims abstract description 39
- 235000021015 bananas Nutrition 0.000 claims abstract description 37
- 210000002615 epidermis Anatomy 0.000 claims description 38
- 239000007788 liquid Substances 0.000 claims description 36
- 239000007787 solid Substances 0.000 claims description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 19
- 108090000790 Enzymes Proteins 0.000 claims description 16
- 102000004190 Enzymes Human genes 0.000 claims description 16
- 238000009833 condensation Methods 0.000 claims description 10
- 230000005494 condensation Effects 0.000 claims description 10
- 230000029087 digestion Effects 0.000 claims description 10
- 238000001704 evaporation Methods 0.000 claims description 2
- 230000008020 evaporation Effects 0.000 claims description 2
- 238000007738 vacuum evaporation Methods 0.000 claims 1
- 239000000203 mixture Substances 0.000 description 16
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 7
- 239000012530 fluid Substances 0.000 description 6
- 238000011084 recovery Methods 0.000 description 5
- 239000012809 cooling fluid Substances 0.000 description 3
- 239000000796 flavoring agent Substances 0.000 description 3
- 235000019634 flavors Nutrition 0.000 description 3
- 239000002002 slurry Substances 0.000 description 3
- 235000000346 sugar Nutrition 0.000 description 3
- 150000008163 sugars Chemical class 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000001976 enzyme digestion Methods 0.000 description 2
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000002910 solid waste Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 206010014970 Ephelides Diseases 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- 102000010029 Homer Scaffolding Proteins Human genes 0.000 description 1
- 108010077223 Homer Scaffolding Proteins Proteins 0.000 description 1
- 239000005909 Kieselgur Substances 0.000 description 1
- 208000003351 Melanosis Diseases 0.000 description 1
- 108010059820 Polygalacturonase Proteins 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 241000317530 Typhonodorum lindleyanum Species 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 108010093305 exopolygalacturonase Proteins 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 238000003801 milling Methods 0.000 description 1
- 238000005498 polishing Methods 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 230000005070 ripening Effects 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 238000005201 scrubbing Methods 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
- 238000013022 venting Methods 0.000 description 1
- 239000003039 volatile agent Substances 0.000 description 1
Images
Classifications
-
- 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
- A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
- A23L2/02—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation containing fruit or vegetable juices
-
- 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
- A23L27/00—Spices; Flavouring agents or condiments; Artificial sweetening agents; Table salts; Dietetic salt substitutes; Preparation or treatment thereof
- A23L27/10—Natural spices, flavouring agents or condiments; Extracts thereof
- A23L27/12—Natural spices, flavouring agents or condiments; Extracts thereof from fruit, e.g. essential oils
Definitions
- the invention relates to a method for obtaining banana juice and banana essences from bananas.
- Bananas consist of a pulp covered by a peel.
- the pulp includes water, sugars, cellulosic constituents, residual starch, and flavor and aroma components which include, in general, a variety of alcohols, aldehydes, esters, and ketones.
- the peel of a ripe banana consists of an outer epidermis, a yellow colored layer (chlorenchyma) and a white inner layer (parenchyma). Mixtures of aroma components essentially free of sugars and other solid constituents of the pulp are known as banana essences.
- banana essences can be obtained from ripened bananas, after the peels are manually removed and discarded, by homogenizing the pulp and recovering volatile components from the homogenized pulp by drawing off the volatile components under vacuum.
- banana juice can be obtained from ripened bananas, after the peels are manually removed and discarded, by homogenizing the pulp; digesting the homogenized pulp with an enzyme to cause the pulp to evolve into a solid and a liquid portion (the banana juice); and separating the liquid portion from the solid portion.
- banana juice refers to a solution including the water and sugars from the banana pulp, essentially free of any components of the pulp that are insoluble in water.
- de-flavored banana juice means banana juice that is essentially free of the volatile flavor and aroma components of the pulp.
- concentrated de flavored banana juice is the de flavored banana juice concentrated removing part of the water by evaporation.
- the invention features, in one aspect, an improved process for obtaining banana juice from a banana, the method including placing a quantity of whole ripe bananas into a mechanical peeling device that separates banana pulp from the outer epidermis and chlorenchyma of banana peels; digesting the pulp with an enzyme to cause the pulp to evolve into a solid portion and a liquid portion, the liquid portion including the banana juice; and separating the liquid portion from the solid portion.
- the mechanical peeling device separates the pulp and parenchyma from the other peel components and a mixture of pulp and parenchyma are digested with the enzyme.
- the invention features, in another aspect, a process for obtaining a banana essence from the outer epidermis and the chlorenchyma of banana peels, the method including peeling the outer epidermis and chlorenchyma from whole, ripe bananas, homogenizing the outer epidermis and chlorenchyma, and recovering from the homogenized material volatile components that include the banana essence.
- the invention features, in another aspect, a process for obtaining a banana essence from banana pulp, the method including peeling the outer epidermis and chlorenchyma from whole ripe bananas to isolate the banana pulp; digesting the pulp with an enzyme to cause the pulp to evolve into a liquid portion and a solid portion; and, during the digestion, recovering, from the pulp, volatile components that include banana essence.
- a mechanical peeling device is used for separation of the parenchyma and pulp from the other peel components, both the pulp and parenchyma being digested with the enzyme to cause the pulp and parenchyma to evolve into a liquid and a solid portion; and during the digestion the banana essence is recovered from the pulp-parenchyma mixture.
- the invention features, in another aspect, an improved process for obtaining a banana essence from a banana, the method including placing a quantity of whole ripe bananas into a mechanical peeling device that separates banana pulp from the outer epidermis and chlorenchyma of banana peels; homogenizing the pulp and parenchyma; and recovering from the homogenized pulp and parenchyma volatile components including a banana essence.
- the invention features, in another aspect, a process for obtaining banana essences and de-flavored banana juice from a banana, the method including placing a quantity of whole, ripe bananas into a mechanical peeling device; within the device, separating banana pulp and the parenchyma of banana peels from the outer epidermis and chlorenchyma of banana peels; homogenizing the pulp and parenchyma; recovering from the homogenized pulp and parenchyma volatile components including a first banana essence; digesting the pulp and parenchyma, with an enzyme to cause the pulp and parenchyma to evolve into a solid portion and a liquid portion, the liquid portion including banana juice; during the digestion, recovering from the pulp and parenchyma volatile components including a second banana essence; separating the solid portion from the liquid portion; and removing from the liquid portion, volatile components including a third banana essence, thereby concentrating the liquid portion, the concentrated liquid portion including the concentrated, de-flavored banana juice.
- the invention also features methods of peeling bananas using mechanical peeling devices.
- the preferred mechanical peeling device is a pulper that includes a screen having openings (preferably 0.25 inch or less in diameter) that preclude the outer epidermis and chlorenchyma of the peels from passing through, but allows the pulp and parenchyma to pass through.
- the use of a mechanical peeling device provides a very efficient method of separating the outer epidermis and chlorenchyma from banana pulp.
- the device allows the parenchyma, which also contains banana juice and essence, to be separated from the other peel components. Together, the pulp and parenchyma generally constitute 90-95% of the weight of the banana, and accordingly, the recovery of the essences and juice is high. Large quantities of bananas are readily peeled using the device, with a minimum of waste.
- banana essences from the banana peels, enzyme digested pulp, and from the banana juice while being concentrated increases the total yield of banana essences. Moreover, each type of essence has its own distinct properties.
- the clarified banana juice obtained can be mixed with other types of juices to obtain a good tasting product.
- FIG. 1 is a block diagram of the steps in the banana juice and banana essence recovery process.
- FIG. 2 is a sectional view of a pulper and a finisher used as a mechanical banana peeler.
- FIG. 3 is a partially sectional view of a homogenizer.
- FIG. 4 is a sectional view of a deaerator and holding tank.
- FIG. 5 is a perspective view, partially in section, of banana essence recovery apparatus.
- FIG. 6 is a perspective view of an apparatus for grinding, screening, and homogenizing prior to obtaining banana essence from banana peels.
- FIG. 7 is a perspective view, partially in section, of an apparatus for enzyme digestion of banana pulp.
- FIG. 8 is a perspective view, partially in section, of an apparatus for recovery of banana essences.
- FIG. 9 is a sectional view of an apparatus for concentrating banana juice.
- FIG. 10 is an apparatus for recovering banana essences.
- FIG. 11 is a perspective view of a banana juice collection apparatus.
- FIGS. .[.12.]. .Iadd.12a .Iaddend.and 12b are sectional views of alternate embodiments of mechanical banana peelers.
- Bananas are sorted and ripened (200). Selected bananas are peeled mechanically (300). The outer epidermis and chlorenchyma of the peels are homogenized by milling (400), and a peel essence recovered from the homogenized mixture (600). Solid wastes are discarded (1000). The pulp and parenchyma from the peeling step (300) are homogenized and deaerated at a vacuum holding station (500). A first banana essence is recovered from the volatile components (700). The homogenized pulp-parenchyma mixture is subjected to enzyme digestion and filtration (800), and a second banana essence is recovered from the volatile components (900).
- Solid wastes from step 800 are discarded (1000).
- the clarified banana juice from step 800 is concentrated (1100) to a de flavored, concentrated banana juice.
- a third banana essence is recovered (1200) from the evaporated volatiles.
- the concentrated banana juice is collected and frozen (1300) and stored (1400) for future use.
- acceptable bananas are ripened (using ethylene gas to trigger the ripening) and stored under conventional temperature and air circulation conditions.
- the best yield of essences and juice is achieved from bananas ripened to have a peel color index of at least 5, more preferably of about 7.
- a peel color index of 5 means the peel is all yellow with some traces of green at the tips.
- a peel color index of 7 means the peel is completely yellowed and is covered with brown freckles.
- the bananas are washed with fresh water, and moldy, overripe, or otherwise unacceptable bananas are removed.
- the bananas 10 are fed into the feeder hopper 12 of mechanical peeling device 14.
- the device includes, in series, a screen 16 having 0.125 to 0.25 inch diameter openings and a screen 18 having 0.027 to 0.045 inch diameter openings.
- the rotating paddles or brushes 17 force a mixture 20 of the banana pulp and the parenchyma of the peels through the screens, while the outer epidermis and chlorenchyma of the peels (mixture 22) and other wastes are carried along the screen to a discharge outlet 23.
- the process is preferably carried out under an atmosphere without oxygen (e.g., under steam) to avoid darkening that occurs when oxygen contacts the banana pulp in the presence of enzymes contained in the pulp.
- FIG. 2 Devices of the type shown in FIG. 2 are available, e.g., from FMC Corp., of Homer City, Pa., (Model No. 100) or from Brown Machine, of Beaverton, Mich.
- the pulp and parenchyma mixture 20 from the mechanical peeling device is passed through a homogenizer 24.
- Pistons 26 homogenize the mixture 20 by forcing it through small openings 28, e.g., 0.125 inch diameter, at high pressure, e.g., 1,000 psi.
- the homogenized pulp parenchyma mixture (puree) is next pumped into a perforated basket 31 within the chamber of a deaerator 30.
- a vacuum pump 32 (FIG. 5) maintains the pressure inside the deaerator below about 5 in. Hg. This low pressure is maintained in the holding tank as well.
- Rotation of basket 31 disperses the puree into fine particles as it is passed through the perforations to form a film along the walls of the internal surface of the deaerator.
- Volatile components including flavor and aroma components, are drawn off through vacuum line 36.
- the deaerated pulp then drops by gravity into vacuum holding tank 34, which is also connected to the pump 32 through line 36. Further volatile components are drawn off from the puree in the holding tank for about one half hour.
- the pump 32 pulls the volatile components in the tube 36 through concentric tube heat exchanger 38.
- the exchanger 38 has three concentric tubes; a cooling fluid (e.g., a water and ethylene glycol mixture) circulates inside the innermost tube and between the two outer tubes.
- the volatile components flow through the exchanger and are partially condensed.
- the remaining vapors and the condensate flow into the pump 32, where they are brought into contact with a cold water/essence solution that is the working fluid of the vacuum pump.
- the essence present in the condensed vapors is absorbed by the working fluid. Uncondensed vapors and working fluid are pumped through the discharge tube 39 into the jacketed tank 40, which is also cooled by a circulating cooling fluid.
- the water/essence solution is recirculated, by means of a pump 44, through a plate heat exchanger 46, which is also cooled by a circulating cooling fluid. Finally the water/essence solution is recirculated to the pump 32 through the return line 48.
- the condensation of the volatile components increases the volume of the water/essence solution in the system. After the volume reaches a previously determined level, the solution overflows into a collection tube 50 in the jacketed tank 40. An additional collection tube 52 in the tube 41 drains condensates in the tube 41 into the collection tube 50.
- the product that flows from the tube 50 is a high quality banana essence.
- the outer epidermis-chlorenchyma mixture 22 is combined with water and fed to an attrition mill 54.
- the resulting slurry passes into a finisher 58.
- the fine portion of slurry 56 is passed by pump 60 into an homogenizer 62; the coarse remainder of the mixture 22 is discarded at the end of the finisher.
- the fine slurry is homogenized and discharged into a deaerator holding tank arrangement of the same design as described above with reference to FIG. 4.
- the volatile components are passed to a pump of the same design as described above with reference to FIG. 5 to recover a banana essence.
- the deaerated banana puree is drawn off from the bottom of the tank 34 (FIG. 4) by means of a pump (not shown), and is fed to one of several digestion tanks 64 (FIG. 7) to be treated with a pectinase (e.g., CLAREX L, a trademark of Miles Laboratories, Inc.) to facilitate the separation of the solid portion of the puree from the liquid portion (the banana juice).
- a pectinase e.g., CLAREX L, a trademark of Miles Laboratories, Inc.
- Tanks 64 are equipped with rotary coils 66 to adjust the temperature inside the vat to the optimum for the activity of the enzyme.
- Tanks 64 also are fitted with covers 68 and venting means 70.
- the digestion is carried out at 120° F. for 2 hours, at which time the digested puree is passed from the tanks through a screw press 72 to remove the bulk of the banana juice.
- the cloudy juice from the screw press passes to a rotary vacuum filter 74 that has been precoated with diatomaceous earth (the earth suspension tank, agitator, and pump are not shown).
- the de-flavored banana juice from the filter 74 is passed through a plate heat exchanger 76 for coagulation of any proteins present.
- the pasteurized juice is passed through a polishing filter 78 and finally to a surge tank 80.
- the clarified banana juice enters (83) from surge tank 80 is fed to an evaporator consisting of a plate heat exchanger 86 and an evaporator body 88.
- the more volatile components of the juice, plus some water, are vaporized and flow to a partial condenser 90, which condenses most of the water vapor while not condensing the more volatile components that include a banana essence.
- the vapors from the condenser 90 are fed to a second condenser 92, which is cooled with a water glycol mixture. Condensates and remaining vapors are drawn into a liquid ring vacuum pump 94, whose working fluid is a water banana essence mixture.
- a pump 96 forces the working fluid to flow through a plate heat exchanger 98 and through the pump 94.
- the discharge from the pump 94 passes to a liquid vapor separator 100.
- the vapor stream from the separator is fed to a scrubber 102, where the vapors are scrubbed with chilled water and vented.
- the liquid in the separator is pumped to the bottom of the scrubber and collected, mixed with the scrubbing water, as a banana essence product.
- the concentrated, de-flavored banana juice pumped from the bottom of evaporator body 88 is passed through a glycol-cooled swept surface exchanger 104 and then through an ammonia-cooled swept surface exchanger 106, where the juice is cooled to a temperature of 32° to 40° F.
- FIG. 12A One such device 106 is shown in FIG. 12A.
- whole clusters or hands of ripe bananas are fed to the machine.
- Pre-breaker fingers 108 mounted in a slowly rotating axis 110 prevent the bridging of the clusters in the throat 112 of the device.
- the clusters fall into a space formed between a strong but flexible belt 114 and a perforated drum 116 having 3 to 5 mm diameter openings.
- the belt forces the banana pulp and the parenchyma through the perforations into the drum 116.
- the mixture is removed by a stationary hanger 118.
- a device 106 is available from, e.g., Baader, of West Germany (Model No. 896).
- a breaking mechanism 122 In a second alternative peeling device 120, shown in FIG. 12B, clusters of bananas are fed to a breaking mechanism 122, then, by positive displacement pump 124, e.g., a MOYNO® pump from Robbins & Myers, Inc. of Springfield, Ohio, to an extruding-type screw conveyor 126.
- This conveyor operates inside a tapered cone 128 provided with a multiplicity of small (0.5 mm) holes.
- the pulp and parenchyma of the bananas are forced through the holes in the cone to the outside.
- the outer epidermis and chlorenchyma of the peels travel to the end of the cone and are discarded against an inverted back-pressure cone 130 which can be adjusted to vary the pressure inside the perforated cone.
- An advantage of device 120 is that the pulp may be deseeded during the operation.
- a device 120 is available, e.g., from Beehive Machinery, Inc. (RSTD-06 Food Processing Machine).
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- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Nutrition Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Preparation Of Fruits And Vegetables (AREA)
Abstract
Description
Claims (15)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US07/777,195 USRE34237E (en) | 1987-12-04 | 1991-10-16 | Banana processing |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US07/128,633 US4874617A (en) | 1987-12-04 | 1987-12-04 | Banana processing |
US07/777,195 USRE34237E (en) | 1987-12-04 | 1991-10-16 | Banana processing |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US07/128,633 Reissue US4874617A (en) | 1987-12-04 | 1987-12-04 | Banana processing |
Publications (1)
Publication Number | Publication Date |
---|---|
USRE34237E true USRE34237E (en) | 1993-04-27 |
Family
ID=26826783
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US07/777,195 Expired - Lifetime USRE34237E (en) | 1987-12-04 | 1991-10-16 | Banana processing |
Country Status (1)
Country | Link |
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US (1) | USRE34237E (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1997023652A1 (en) * | 1995-12-22 | 1997-07-03 | Pepe International, Inc. | Process for conversion of bananas to sugar syrup |
US20070184157A1 (en) * | 2006-02-07 | 2007-08-09 | Citrus World, Inc. | Hot fill and quick chill process for premium quality juice |
EP2227970A1 (en) * | 2009-03-09 | 2010-09-15 | CFT S.p.A. | A process for producing fruit juices. |
WO2011018700A1 (en) | 2009-08-12 | 2011-02-17 | Munisekhar Medasani | Natural extract from whole banana fruit (musa spp.) |
US8752480B1 (en) | 2005-08-31 | 2014-06-17 | Milne Fruit Products, Inc. | Apparatus for preparing melon juice concentrate |
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US1053955A (en) * | 1912-05-01 | 1913-02-18 | James Barry | Manufacture of purified banana-flour. |
US1138888A (en) * | 1914-06-06 | 1915-05-11 | Us Tropical Food Company | Banana food and process of making same. |
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-
1991
- 1991-10-16 US US07/777,195 patent/USRE34237E/en not_active Expired - Lifetime
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US8752480B1 (en) | 2005-08-31 | 2014-06-17 | Milne Fruit Products, Inc. | Apparatus for preparing melon juice concentrate |
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US20070184157A1 (en) * | 2006-02-07 | 2007-08-09 | Citrus World, Inc. | Hot fill and quick chill process for premium quality juice |
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