Article of manufacture and process

Claim 2

The process for drum drying a fruit puree on a drum dryer, which comprises the steps of: (a) applying said fruit puree at a rate of at least about 1.2 gal/ft 2 hr to said drum dryer forming a film in a controlled environment of cooling-dehumidified air; (b) drum drying said puree in said controlled environment of cooling-dehumidified air to form a drum dried product; and (c) flaking said drum dried product whereby the resultant flaked product has a moisture content of not more than about 1% and said flaked product is readily reconstitutible to natural consistency.

Claim 3

The process as in claim 1, wherein said puree is prepared from mature fruit using the steps of: (a) cooking by heating said fruit to a temperature to soften said fruit and in a manner which retains the integrity of said fruit; (b) screening said fruit to remove undesirable material in a manner which preserves its integrity; and (c) delivering said screened fruit to said drum dryer for drying.

Claim 4

The process as in claim 2, wherein said fruit is heated to a temperature of between about 190° F. and 200° F. prior to said screening step.

Claim 5

The process as in claim 1, wherein said puree, when dried, forms a sheet on the drum of said drum dryer which is doctored from said drum dryer; further comprising the step of drying said doctored drum in said controlled atmospheric environment of cooling-dehumified air prior to applying said fruit puree on said drum dryer.

Claim 6

The process as in claim 1, wherein step (a) is performed to form a first film, further comprising the step of forming a second film by applying said puree to said first film after said first film has remained in said controlled environment for a predetermined period of time.

Claim 7

The process as in claim 5, further comprising the step of press rolling the combined said first and second films in said controlled environment.

Claim 8

The process as in claim 1 wherein fresh fruit is utilized in said puree, which puree is prepared without the addition of extenders.

Claim 9

The process as in claim 7, further comprising the step of preparing said fresh fruit puree in a manner which preserves the natural integrity of the fruit.

Claim 10

The process as in claim 1, further comprising the step of evacuating the air from said controlled atmospheric environment.

Claim 11

The process as in claim 1, wherein said flaking step further comprises the steps of removing said puree from said drum dryer in a sheet and flaking said sheet, said removing and flaking steps, being conducted entirely within said controlled environment.

Claim 12

The process as in claim 10, further comprising the step of conveying said sheet in said controlled atmospheric environment prior to said flaking of said sheet.

Claim 13

The process as in claim 10, further comprising the step of breaking up said dried sheet in said controlled atmospheric environment prior to said flaking of said sheet.

Claim 14

The process as in claim 1, further comprising the steps of supplying said environment with said cooling-dehumidified air, and evacuating the air from said environment at a rate which is less than the rate said cooling-dehumidified air is supplied, whereby a positive pressure is maintained to prevent non-controlled air from outside said controlled environment from flowing into said controlled environment.

Claim 15

The process as in claim 13, wherein the evacuation of said air is performed in close proximity to said drum dryer.

Claim 16

The process as in claim 1, wherein said cooling-dehumidified air has a relative humidity of less than about 60% and a temperature of less than about 80° F.

Claim 17

The process as in claim 1, wherein said cooling-dehumidified air has a temperature of about 70° F. or less and the sum of said temperature and relative humidity is about 120 or less.

Claim 18

The process as in claim 16, wherien said sum is about 100 or less.

Claim 19

The process as in claim 1, wherein said cooling-dehumidified air preferably has a relative humidity of less than about 30%.

Claim 20

The process for forming a sheet from a fruit puree in an environment of cooling-dehumidified air by drum drying same wherein the drum drying apparatus is a single drum type dryer having a drying drum and at least one distribution/spreader roller, wherein said drum drying operation produces steam and moisture, comprising the steps of: (a) maintaining the condition of said air in said controlled environment; (b) applying said puree to said drying drum via said distribution/spreader roller at a rate of at least about 1.2 gal/ft 2 hr forming a film; (c) drying said puree, whereby said forming and drying steps are conducted entirely in said controlled environment of a cooling-dehumidified flow of air to form a drum dried product; and (d) flaking said drum dried product in said controlled environment, whereby the resultant flaked product has a moisture content of not more than about 1% and said flaked product is readily reconstitutible to natural consistency.

Claim 21

The process for forming a sheet from a fruit puree in an environment of cooling-dehumidified air by drum drying same wherein the drum drying apparatus is a single drum type dryer having a drying drum and at least one distribution/spreader roller, wherein said drum drying operation produces steam and moisture, comprising the steps of: (a) maintaining the condition of said air in said controlled environment; (b) applying said puree to said drying drum via said distribution/spreader roller at a rate of at least about 1.2 gal/ft 2 hr forming a film; (c) drying said puree, whereby said forming and drying steps are conducted entirely in said controlled environment of a cooling-dehumidified flow of air to form a drum dried product; and (d) flaking said drum dried product in said controlled environment, whereby the resultant flaked product has a moisture content of not more than about 1% and said flaked product is readily reconstitutible to natural consistency.

Claim 22

The process as in claim 19, wherein said sheet is formed from a plurality of films and distribution/spreader rollers, wherein said first distribution/spreader roller is operated to form a first film on said drying drum, further comprising the step of forming a plurality of films by applying said puree to said previously formed film via at least one subsequent distributor/spreader roller.

Claim 23

The process as in claim 20, further comprising the step of press rolling the combined said plurality of films.

Claim 24

The process for forming a sheet from a non-extended fruit puree by drum drying same wherein the drum drying apparatus is contained within a controlled environment of cooling-dehumidified air and is a single drum type dryer having a drum and at least three distribution/spreader rollers, comprising the steps of: (a) maintaining the condition of the air in said controlled atmospheric environment of cooling-dehumidified air and evacuating same from said environment in a manner which circulates a cooling-dehumidified flow of air in the vicinity of said drum dryer; (b) applying said puree to said drum via a first distribution/spreader roller; (c) applying said puree to the product of step (b) via a second distribution/spreader roller; (d) applying said puree to the product of step (c) via a third distribution/spreader roller, whereby the total feed rate of said puree ranges from about 1.2 to 7.2 gal/ft 2 hr; (e) press rolling the product of steps (b), (c), and (d), whereby the product of said applying steps is dried and said resultant product of said applying, drying, and press rolling steps is bathed in said cooling-dehumidified air; and (f) flaking the resultant product of step (e) forming a flaked product having a moisture content of not more than about 1%, whereby said flaked product is readily reconstitutible to natural consistency.

Claim 25

The process for forming a sheet from a non-extended fruit puree by drum drying same wherein the drum drying apparatus is contained within a controlled environment of cooling-dehumidified air and is a single drum type dryer having a drum and at least three distribution/spreader rollers, comprising the steps of: (a) maintaining the condition of the air in said controlled atmospheric environment of cooling-dehumidified air and evacuating same from said environment in a manner which circulates a cooling-dehumidified flow of air in the vicinity of said drum dryer; (b) applying said puree to said drum via a first distribution/spreader roller; (c) applying said puree to the product of step (b) via a second distribution/spreader roller; (d) applying said puree to the product of step (c) via a third distribution/spreader roller, whereby the total feed rate of said puree ranges from about 1.2 to 7.2 gal/ft 2 hr; (e) press rolling the product of steps (b), (c), and (d), whereby the product of said applying steps is dried and said resultant product of said applying, drying, and press rolling steps is bathed in said cooling-dehumidified air; and (f) flaking the resultant product of step (e) forming a flaked product having a moisture content of not more than about 1%, whereby said flaked product is readily reconstitutible to natural consistency.

Claim 26

The process of claim 22, wherein said feed rate is in the range of from about 3.6 to 5.8 gal/ft 2 hr.

Claim 27

The process for drum drying a fruit puree on a drum dryer which comprises the steps of: (a) applying said fruit puree to said drum dryer at a rate of at least about 1.2 gal/ft 2 hr; (b) forming a film in a controlled environment of cooling-dehumidified air wherein the sum of the temperature in degrees Fahrenheit and percentage relative humidity of said cooling-dehumidified air is less than about 100; (c) drying said puree in said controlled environment of cooling-dehumidified air to form a sheet; and (d) flaking said sheet whereby the resultant flaked product has a moisture content of not more than about 1% and said flaked product is readily reconstitutible to natural consistency.

Claim 28

The process for drum drying a fruit puree on a drum dryer which comprises the steps of: (a) applying said fruit puree to said drum dryer at a rate of at least about 1.2 gal/ft 2 hr; (b) forming a film in a controlled environment of cooling-dehumidified air wherein the sum of the temperature in degrees Fahrenheit and percentage relative humidity of said cooling-dehumidified air is less than about 100; (c) drying said puree in said controlled environment of cooling-dehumidified air to form a sheet; and (d) flaking said sheet whereby the resultant flaked product has a moisture content of not more than about 1% and said flaked product is readily reconstitutible to natural consistency.

Claim 29

The process as in claim 24, wherein the drying drum of said drum dryer rotates at from about 2 to 11 rpm.

Claim 30

The process as in claim 24, wherein said feed rate is in the range of from about 1.2 to 14.4 gal/ft 2 hr.

Claim 31

The process as in claim 24, wherein said feed rate is in the range of from about 1.2 to 7.2 gal/ft 2 hr.

Claim 32

The process as in claim 25, wherein said feed rate is in the range of from about 1.2 to 5.8 gal/ft 2 hr.