Process for preparing a citrus fruit juice concentrate

Claim 2

A process for making a natural citrus fruit juice concentrate product which comprises: (1) extracting fruit juice from fruit, said fruit juice comprising a particulate solids portion and a serum portion; (2) passing said juice directly to a separating zone having an inert atmosphere wherein said particulate solids portion is separated and recovered, thereby forming a serum portion comprising about 7% to about 20% non-aqueous compounds, and about 80% to 93% water; (3) passing said serum portion containing non-aqueous compounds less than 80 microns in size to a freeze concentrating zone comprising an adiabatic recrystallizer wherein, under an inert atmosphere, substantially pure ice crystals are formed and recovered without removing substantial amounts of solids, whereby a concentrated fruit juice is formed comprising from about 20% to about 52% solids and from about 48% to about 80% water; (4) pasteurizing said concentrated fruit juice by heating in a closed system to a temperature in the range of about 80° C. to about 95° C. for from about 3 to about 15 seconds whereby microorganisms and enzymes present are substantially inactivated; thereby producing a natural citrus fruit juice concentrate product comprising: (A) substantially 100% of the nonvolatile compounds originally present in the solids portion of said serum; (B) at least 65% of the volatile compounds originally present in the solids portion of said serum.

Claim 3

A process according to claim 1 wherein the particulate solids separated in step (2) are pasteurized by heating in a closed system to a temperature in the range of about 80° C. to about 95° C. for from about 3 to about 15 seconds whereby microorganisms and enzymes present are inhibited substantially, and, thereafter, recombining about 9% to about 20% (V/V) of the particulate solids with the pasteurized fruit juice of step (4).

Claim 4

A process according to claim 1 wherein the separation step (2) is performed by centrifuging with a high speed centrifuge.

Claim 5

A process according to claim 1 wherein said juice entering the separation step (2) is at a temperature below 30° C.

Claim 6

A process for making a natural citrus fruit juice concentrate product which comprises: (1) extracting fruit juice from fruit, said fruit juice comprising a particulate solids portion and a serum portion; (2) pasteurizing said fruit juice by heating it in a closed system to a temperature in the range of about 80° C. to about 95° C. for from about 3 to about 15 seconds whereby microorganisms and enzymes present are substantially inactivated; (3) passing said juice directly to a separating zone having an inert atmosphere wherein said particulate solids portion is separated and recovered, thereby forming a serum portion comprising about 7% to about 20% non-aqueous compounds, and about 80% to 93% water; (4) passing said serum portion containing non-aqueous compounds less than 80 microns in size to a freeze concentrating zone comprising an adiabatic recrystallizer wherein, under an inert atmosphere, substantially pure ice crystals are formed and recovered without removing substantial amounts of solids, whereby a concentrated fruit juice is formed comprising from about 20% to about 52% solids and from about 48% to about 80% water; thereby producing a natural citrus fruit juice concentrate product comprising: (A) substantially 100% of the nonvolatile compounds originally present in the solids portion of said serum; (B) at least 65% of the volatile compounds originally present in the solids portion of said serum.

Claim 7

A process for making a natural citrus fruit juice concentrate product which comprises: (1) extracting fruit juice from fruit, said fruit juice comprising a particulate solids portion and a serum portion; (2) pasteurizing said fruit juice by heating it in a closed system to a temperature in the range of about 80° C. to about 95° C. for from about 3 to about 15 seconds whereby microorganisms and enzymes present are substantially inactivated; (3) passing said juice directly to a separating zone having an inert atmosphere wherein said particulate solids portion is separated and recovered, thereby forming a serum portion comprising about 7% to about 20% non-aqueous compounds, and about 80% to 93% water; (4) passing said serum portion containing non-aqueous compounds less than 80 microns in size to a freeze concentrating zone comprising an adiabatic recrystallizer wherein, under an inert atmosphere, substantially pure ice crystals are formed and recovered without removing substantial amounts of solids, whereby a concentrated fruit juice is formed comprising from about 20% to about 52% solids and from about 48% to about 80% water; thereby producing a natural citrus fruit juice concentrate product comprising: (A) substantially 100% of the nonvolatile compounds originally present in the solids portion of said serum; (B) at least 65% of the volatile compounds originally present in the solids portion of said serum.

Claim 8

A process according to claim 5 wherein about 7% to about 20% (V/V) of the particulate solids portion of the juice separated in step 3 is recombined with the concentrated fruit juice of step 4.

Claim 9

A process for making a natural citrus fruit juice concentrate product which comprises: (1) extracting fruit juice from fruit, said fruit juice comprising a particulate solids portion and a serum portion; (2) passing said juice directly to a separating zone having an inert atmosphere wherein said particulate solids portion is separated and recovered, thereby forming a serum portion comprising about 7% to about 20% non-aqueous compounds, and about 80% to 93% water; (3) passing said serum portion containing non-aqueous compounds less than 80 microns in size to a freeze concentrating zone comprising an adiabatic recrystallizer wherein, under an inert atmosphere, substantially pure ice crystals are formed and recovered without removing substantial amounts of solids, whereby a concentrated fruit juice is formed comprising from about 30% to about 60% solids and from about 40% to about 70% water; (4) recombining said concentrated fruit serum with about 9% to about 20% of the particulate solids separated in step (2); (5) pasteurizing the fruit juice concentrate of step (4) by heating it to a temperature in the range of about 80° C. to about 95° C. for from about 3 to about 15 seconds in a closed system whereby microorganisms and enzymes present are substantially inactivated; thereby producing a natural citrus fruit juice concentrate product comprising: (A) substantially 100% of the nonvolatile compounds originally present in the solids portion of said serum; (B) at least 65% of the volatile compounds originally present in the solids portion of said serum.

Claim 10

A process for making a natural citrus fruit juice concentrate product which comprises: (1) extracting fruit juice from fruit, said fruit juice comprising a particulate solids portion and a serum portion; (2) passing said juice directly to a separating zone having an inert atmosphere wherein said particulate solids portion is separated and recovered, thereby forming a serum portion comprising about 7% to about 20% non-aqueous compounds, and about 80% to 93% water; (3) passing said serum portion containing non-aqueous compounds less than 80 microns in size to a freeze concentrating zone comprising an adiabatic recrystallizer wherein, under an inert atmosphere, substantially pure ice crystals are formed and recovered without removing substantial amounts of solids, whereby a concentrated fruit juice is formed comprising from about 30% to about 60% solids and from about 40% to about 70% water; (4) recombining said concentrated fruit serum with about 9% to about 20% of the particulate solids separated in step (2); (5) pasteurizing the fruit juice concentrate of step (4) by heating it to a temperature in the range of about 80° C. to about 95° C. for from about 3 to about 15 seconds in a closed system whereby microorganisms and enzymes present are substantially inactivated; thereby producing a natural citrus fruit juice concentrate product comprising: (A) substantially 100% of the nonvolatile compounds originally present in the solids portion of said serum; (B) at least 65% of the volatile compounds originally present in the solids portion of said serum.

Claim 11

A process for making a natural citrus fruit juice concentrate which comprises: (1) extracting juice from fruit, said fruit juice comprising a particulate solids portion and a serum portion; (2) passing said juice directly to a separating zone having an inert atmosphere wherein said particulate solids portion is separated and recovered, thereby forming a serum portion comprising about 7% to about 20% non-aqueous compounds, and about 80% to 93% water; said non-aqueous compounds portion comprising nonvolatile compounds and volatile compounds; said volatile compounds comprising a lower boiling fraction containing ethyl butyrate and a higher boiling fraction containing limonene; (3) passing said serum portion to a sublimation concentrating zone wherein substantially pure water is removed without removing substantial amounts of solids and wherein the initial temperature is below the eutectic temperature of said serum, the surface temperature initially not exceeding -30° C. to about -25° C., at a pressure of less than 100 microns, whereby a concentrate fruit serum is formed comprising from about 30% to about 87% solids and from about 13% to about 70% water; thereby producing a natural citrus fruit juice concentrate product comprising: (A) substantially 100% of the nonvolatile compounds originally present in the solids portion of said serum; (B) at least 65% of the volatile compounds originally present in the volatiles portion of said serum.

Claim 12

A process for making a natural citrus fruit juice concentrate which comprises: (1) extracting juice from fruit, said fruit juice comprising a particulate solids portion and a serum portion; (2) passing said juice directly to a separating zone having an inert atmosphere wherein said particulate solids portion is separated and recovered, thereby forming a serum portion comprising about 7% to about 20% non-aqueous compounds, and about 80% to 93% water; said non-aqueous compounds portion comprising nonvolatile compounds and volatile compounds; said volatile compounds comprising a lower boiling fraction containing ethyl butyrate and a higher boiling fraction containing limonene; (3) passing said serum portion to a sublimation concentrating zone wherein substantially pure water is removed without removing substantial amounts of solids and wherein the initial temperature is below the eutectic temperature of said serum, the surface temperature initially not exceeding -30° C. to about -25° C., at a pressure of less than 100 microns, whereby a concentrate fruit serum is formed comprising from about 30% to about 87% solids and from about 13% to about 70% water; thereby producing a natural citrus fruit juice concentrate product comprising: (A) substantially 100% of the nonvolatile compounds originally present in the solids portion of said serum; (B) at least 65% of the volatile compounds originally present in the volatiles portion of said serum.

Claim 13

A process according to claim 8 wherein said concentrated fruit juice of step 4 is recombined with about 9% to about 20% of the particulate solids portion separated in step 2.

Claim 14

A process according to claim 8 which additionally comprises a step of pasteurizing said serum at temperatures of from 80° C. to 95° C. for from 3 to 15 seconds in a closed system before passing into the sublimation concentration zone of step (3).

Claim 15

A process according to claim 10 which additionally comprises a step of pasteurizing said concentrated serum at temperatures of from 80° C. to 95° C. for from 3 to 15 seconds in a closed system after said serum portion has been passed through a sublimation concentrating zone.

Claim 16

A process for making a natural citrus fruit juice concentrate product which comprises: (1)extracting juice from fruit, said fruit juice comprising a particulate solids portion and a serum portion; (2) passing said juice directly to a separating zone having an inert atmosphere wherein said particulate solids portion is separated and recovered, thereby forming a serum portion comprising about 7% to about 20% non-aqueous compounds, and about 80% to 93% water; said non-aqueous compounds portion comprising nonvolatile compounds and volatile compounds; said volatile compounds comprising a lower boiling fraction containing ethyl butyrate and a higher boiling fraction containing limonene; (3) passing said serum portion containing non-aqueous compounds less than 80 microns in size to a freeze concentrating zone comprising an adiabatic recrystallizer wherein substantially pure ice crystals are formed and recovered without removing substantial amounts of solids, whereby a concentrated fruit serum is formed comprising from about 30% to about 40% solids and from about 60% to about 70% water; (4) passing said concentrated serum to a sublimation concentration zone wherein substantially pure water is removed without removing a substantial amount of solids and wherein the initial temperature is below the eutectic temperature of said concentrated serum, whereby a concentrated fruit serum is formed comprising from about 60% to about 87% solids and from about 13% to about 40% water; thereby producing natural citrus fruit juice concentrate product comprising: (A) substantially 100% of the nonvolatile compounds originally present in the solids portion of said serum; (B) at least 65% of the volatile compounds originally present in the solids portion of said serum.

Claim 17

A process for making a natural citrus fruit juice concentrate product which comprises: (1)extracting juice from fruit, said fruit juice comprising a particulate solids portion and a serum portion; (2) passing said juice directly to a separating zone having an inert atmosphere wherein said particulate solids portion is separated and recovered, thereby forming a serum portion comprising about 7% to about 20% non-aqueous compounds, and about 80% to 93% water; said non-aqueous compounds portion comprising nonvolatile compounds and volatile compounds; said volatile compounds comprising a lower boiling fraction containing ethyl butyrate and a higher boiling fraction containing limonene; (3) passing said serum portion containing non-aqueous compounds less than 80 microns in size to a freeze concentrating zone comprising an adiabatic recrystallizer wherein substantially pure ice crystals are formed and recovered without removing substantial amounts of solids, whereby a concentrated fruit serum is formed comprising from about 30% to about 40% solids and from about 60% to about 70% water; (4) passing said concentrated serum to a sublimation concentration zone wherein substantially pure water is removed without removing a substantial amount of solids and wherein the initial temperature is below the eutectic temperature of said concentrated serum, whereby a concentrated fruit serum is formed comprising from about 60% to about 87% solids and from about 13% to about 40% water; thereby producing natural citrus fruit juice concentrate product comprising: (A) substantially 100% of the nonvolatile compounds originally present in the solids portion of said serum; (B) at least 65% of the volatile compounds originally present in the solids portion of said serum.

Claim 18

A process according to claim 12 wherein about 9% to about 20% of the particulate solids portion separated in step 2 is recombined with the concentrated fruit juice of step 4.

Claim 19

A process for making a natural citrus fruit juice concentrate product which comprises: (1) extracting juice from fruit, said fruit juice comprising a particulate solids portion and a serum portion; (2) passing said juice to a sublimation concentrating zone wherein the surface temperature of the serum does not initially exceed about -30° C. to about -25° C., and pressure of less than 100 microns, wherein substantially pure water is removed from said juice; thereby producing a natural citrus fruit juice concentrate product comprising: (A) substantially 100% of the non-volatile compounds originally present in the solids portion of said juice; (B) at least 65% of the volatile compounds originally present in the volatiles portion of said serum; (C) substantially 100% of the particulate solids originally present in the fruit juice.

Claim 20

A process for making a natural citrus fruit juice concentrate product which comprises: (1) extracting juice from fruit, said fruit juice comprising a particulate solids portion and a serum portion; (2) passing said juice to a sublimation concentrating zone wherein the surface temperature of the serum does not initially exceed about -30° C. to about -25° C., and pressure of less than 100 microns, wherein substantially pure water is removed from said juice; thereby producing a natural citrus fruit juice concentrate product comprising: (A) substantially 100% of the non-volatile compounds originally present in the solids portion of said juice; (B) at least 65% of the volatile compounds originally present in the volatiles portion of said serum; (C) substantially 100% of the particulate solids originally present in the fruit juice.

Claim 21

A process according to claim 14 which comprises an additional step wherein said juice is pasteurized at temperatures of from 80° C. to 95° C. for from 3 to 15 seconds in a closed system before passing into the sublimation concentrating zone.

Claim 22

A process according to claim 14 which comprises the additional step of pasteurizing said natural citrus fruit juice concentrate at temperatures of from 80° C. to 95° C. for from 3 to 15 seconds in a closed system.

Claim 23

A process for making a natural orange juice concentrate product which comprises: (1) extracting orange juice from oranges, said orange juice comprising a pulp portion and a serum portion; (2) passing said juice directly to a separating zone having an inert atmosphere wherein said pulp portion is separated and recovered, thereby forming a serum portion comprising about 7% to about 20% non-aqueous compounds, and about 80% to 93% water; (3) passing said serum portion containing non-aqueous compounds less than 80 microns in size to a freeze concentrating zone comprising an adiabatic recrystallizer wherein, under an inert atmosphere, substantially pure ice crystals are formed and recovered without removing substantial amounts of solids, whereby a concentrated orange juice is formed comprising from about 20% to about 52% solids and from about 48% to about 80% water; (4) pasteurizing said concentrated orange juice and said pulp by heating in a closed system to a temperature in the range of about 80° C. to about 95° C. for from about 3 to about 15 seconds whereby microorganisms and enzymes present are substantially inactivated; (5) recombining said pasteurized concentrated orange juice with about 30% to about 100% of the pulp portion separated in step (2); thereby producing a natural orange juice concentrate product comprising: (A) substantially 100% of the nonvolatile compounds originally present in the solids portion of said serum; (B) at least 65% of the volatile compounds originally present in the solids portion of said serum, two of said volatiles being ethyl butyrate and limonene; (C) at least 0.1% of said volatile compounds being ethyl butyrate; (D) the proportion of said ethyl butyrate to said limonene being in the range of about 0.0015:1 to about 0.6:1, the amounts and proportions of said volatile compounds are determined by a gas chromatographic analysis of the headspace volatiles released from a sample of orange juice, said sample having a temperature of 40° C.

Claim 24

A process for making a natural orange juice concentrate product which comprises: (1) extracting orange juice from oranges, said orange juice comprising a pulp portion and a serum portion; (2) passing said juice directly to a separating zone having an inert atmosphere wherein said pulp portion is separated and recovered, thereby forming a serum portion comprising about 7% to about 20% non-aqueous compounds, and about 80% to 93% water; (3) passing said serum portion containing non-aqueous compounds less than 80 microns in size to a freeze concentrating zone comprising an adiabatic recrystallizer wherein, under an inert atmosphere, substantially pure ice crystals are formed and recovered without removing substantial amounts of solids, whereby a concentrated orange juice is formed comprising from about 20% to about 52% solids and from about 48% to about 80% water; (4) pasteurizing said concentrated orange juice and said pulp by heating in a closed system to a temperature in the range of about 80° C. to about 95° C. for from about 3 to about 15 seconds whereby microorganisms and enzymes present are substantially inactivated; (5) recombining said pasteurized concentrated orange juice with about 30% to about 100% of the pulp portion separated in step (2); thereby producing a natural orange juice concentrate product comprising: (A) substantially 100% of the nonvolatile compounds originally present in the solids portion of said serum; (B) at least 65% of the volatile compounds originally present in the solids portion of said serum, two of said volatiles being ethyl butyrate and limonene; (C) at least 0.1% of said volatile compounds being ethyl butyrate; (D) the proportion of said ethyl butyrate to said limonene being in the range of about 0.0015:1 to about 0.6:1, the amounts and proportions of said volatile compounds are determined by a gas chromatographic analysis of the headspace volatiles released from a sample of orange juice, said sample having a temperature of 40° C.

Claim 25

A process according to claim 17 wherein the separation step (2) is performed by centrifuging with a high speed centrifuge.

Claim 26

A process according to claim 17 wherein said juice entering the separation step (2) is at a temperature below 30° C.

Claim 27

A process according to claim 17 which includes the step of pasteurizing the pulp recovered in step (2) by heating to a temperature in the range of about 80° C. to about 95° C. for from 3 to 15 seconds in a closed system and thereafter recombining the pasteurized pulp with the pasteurized concentrated orange juice from step (4).

Claim 28

A process for making a natural orange juice concentrate product which comprises: (1) extracting orange juice from oranges, said orange juice comprising a pulp portion and a serum portion; (2) pasteurizing said orange juice by heating it in a closed system to a temperature in the range of about 80° C. to about 95° C. for from about 3 to about 15 seconds whereby microorganisms and enzymes present are substantially inactivated; (3) passing said juice directly to a separating zone having an inert atmosphere wherein said pulp portion is separated and recovered, thereby forming a serum portion comprising about 7% to about 20% non-aqueous compounds, and about 80% to 93% water; (4) passing said serum portion to a freeze concentrating zone comprising an adiabatic recrystallizer wherein, under an inert atmosphere, substantially pure ice crystals are formed and recovered without removing substantial amounts of solids, whereby a concentrated orange juice is formed comprising from about 30% to about 60% solids and from about 40% to about 70% water; (5) and, thereafter, recombining said concentrated orange juice with about 7% to about 20% (V/V) of the pulp portion separated in step (2); thereby producing a natural orange juice concentrate product comprising: (A) substantially 100% of the nonvolatile compounds originally present in the solids portion of said serum; (B) at least 65% of the volatile compounds originally present in the solids portion of said serum, two of said volatiles being ethyl butyrate and limonene; (C) at least 0.1% of said volatile compounds being ethyl butyrate; (D) the proportion of said ethyl butyrate to said limonene being in the range of about 0.0015:1 to about 0.6:1, the amounts and proportions of said volatile compounds are determined by a gas chromatographic analysis of the headspace volatiles released from a sample of orange juice, said sample having a temperature of 40° C.

Claim 29

A process for making a natural orange juice concentrate product which comprises: (1) extracting orange juice from oranges, said orange juice comprising a pulp portion and a serum portion; (2) pasteurizing said orange juice by heating it in a closed system to a temperature in the range of about 80° C. to about 95° C. for from about 3 to about 15 seconds whereby microorganisms and enzymes present are substantially inactivated; (3) passing said juice directly to a separating zone having an inert atmosphere wherein said pulp portion is separated and recovered, thereby forming a serum portion comprising about 7% to about 20% non-aqueous compounds, and about 80% to 93% water; (4) passing said serum portion to a freeze concentrating zone comprising an adiabatic recrystallizer wherein, under an inert atmosphere, substantially pure ice crystals are formed and recovered without removing substantial amounts of solids, whereby a concentrated orange juice is formed comprising from about 30% to about 60% solids and from about 40% to about 70% water; (5) and, thereafter, recombining said concentrated orange juice with about 7% to about 20% (V/V) of the pulp portion separated in step (2); thereby producing a natural orange juice concentrate product comprising: (A) substantially 100% of the nonvolatile compounds originally present in the solids portion of said serum; (B) at least 65% of the volatile compounds originally present in the solids portion of said serum, two of said volatiles being ethyl butyrate and limonene; (C) at least 0.1% of said volatile compounds being ethyl butyrate; (D) the proportion of said ethyl butyrate to said limonene being in the range of about 0.0015:1 to about 0.6:1, the amounts and proportions of said volatile compounds are determined by a gas chromatographic analysis of the headspace volatiles released from a sample of orange juice, said sample having a temperature of 40° C.

Claim 30

A process for making a natural orange juice concentrate product which comprises: (1) extracting orange juice from oranges, said orange juice comprising a pulp portion and a serum portion; (2) passing said juice directly to a separating zone having an inert atmosphere wherein said pulp portion is separated and recovered, thereby forming a serum portion comprising about 7% to about 20% non-aqueous compounds, and about 80% to 93% water; (3) passing said serum portion to a freeze concentrating zone comprising an adiabatic recrystallizer wherein, under an inert atmosphere, substantially pure ice crystals are formed and recovered without removing substantial amounts of solids, whereby a concentrated orange juice is formed comprising from about 30% to about 60% solids and from about 40% to about 70% water; (4) and, thereafter, recombining said concentrated orange serum with about 9% to about 20% (V/V) of the pulp portion separated in step (2); (5) pasteurizing the orange juice concentrate of step (4) by heating it to a temperature in the range of about 80° C. to about 95° C. for from about 3 to about 15 seconds in a closed system whereby microorganisms and enzymes present are substantially inactivated; thereby producing a natural orange juice concentrate product comprising: (A) substantially 100% of the nonvolatile compounds originally present in the solids portion of said serum; (B) at least 65% of the volatile compounds originally present in the solids portion of said serum, two of said volatiles being ethyl butyrate and limonene; (C) at least 0.1% of said volatile compounds being ethyl butyrate; (D) the proportion of said ethyl butyrate to said limonene being in the range of about 0.0015:1 to about 0.6:1,the amounts and proportions of said volatile compounds are determined by a gas chromatographic analysis of the headspace volatiles released from a sample of an orange juice, said sample having a temperature of 40° C.

Claim 31

A process for making a natural orange juice concentrate product which comprises: (1) extracting orange juice from oranges, said orange juice comprising a pulp portion and a serum portion; (2) passing said juice directly to a separating zone having an inert atmosphere wherein said pulp portion is separated and recovered, thereby forming a serum portion comprising about 7% to about 20% non-aqueous compounds, and about 80% to 93% water; (3) passing said serum portion to a freeze concentrating zone comprising an adiabatic recrystallizer wherein, under an inert atmosphere, substantially pure ice crystals are formed and recovered without removing substantial amounts of solids, whereby a concentrated orange juice is formed comprising from about 30% to about 60% solids and from about 40% to about 70% water; (4) and, thereafter, recombining said concentrated orange serum with about 9% to about 20% (V/V) of the pulp portion separated in step (2); (5) pasteurizing the orange juice concentrate of step (4) by heating it to a temperature in the range of about 80° C. to about 95° C. for from about 3 to about 15 seconds in a closed system whereby microorganisms and enzymes present are substantially inactivated; thereby producing a natural orange juice concentrate product comprising: (A) substantially 100% of the nonvolatile compounds originally present in the solids portion of said serum; (B) at least 65% of the volatile compounds originally present in the solids portion of said serum, two of said volatiles being ethyl butyrate and limonene; (C) at least 0.1% of said volatile compounds being ethyl butyrate; (D) the proportion of said ethyl butyrate to said limonene being in the range of about 0.0015:1 to about 0.6:1,the amounts and proportions of said volatile compounds are determined by a gas chromatographic analysis of the headspace volatiles released from a sample of an orange juice, said sample having a temperature of 40° C.

Claim 32

A process for making a natural orange juice concentrate product which comprises: (1) extracting orange juice from oranges, said orange juice comprising a pulp portion and a serum portion; (2) passing said juice directly to a separating zone having aninert atmosphere wherein said pulp portion is separated and recovered, thereby forming a serum portion comprising about 7% to about 20% non-aqueous compounds, and about 80% to 93% water, said non-aqueous compounds portion comprising nonvolatile compounds and volatile compounds; said volatile compounds comprising a lower boiling fraction containing ethyl butyrate and a higher boiling fraction containing limonene; (3) passing said serum portion to a sublimation concentrating zone wherein substantially pure water is removed without removing substantial amounts of solids and wherein the initial temperature is below the eutectic temperature of said serum, whereby a concentrated orange serum is formed comprising from about 30% to about 87% solids and from about 13% to about 70% water; (4) and, thereafter, recombining said concentrated orange serum with about 9% to about 20% (V/V) of the pulp portion separated in step (2); thereby producing a natural orange juice concentrate product comprising: (A) substantially 100% of the nonvolatile compounds originally present in the solids portion of said serum; (B) at least 65% of the volatile compounds originally present in the solids portion of said serum, at least two of said volatiles being ethyl butyrate and limonene; (C) at least 0.1% of said volatile compounds being ethyl butyrate; (D) the proportion of said ethyl butyrate to said limonene being in the range of about .0015:1 to about 0.6:1, the amounts and proportions of said volatile compounds are determined by a gas chromatographic analysis of the headspace volatiles released from a sample of an orange juice, said sample having a temperature of 40° C.

Claim 33

A process for making a natural orange juice concentrate product which comprises: (1) extracting orange juice from oranges, said orange juice comprising a pulp portion and a serum portion; (2) passing said juice directly to a separating zone having aninert atmosphere wherein said pulp portion is separated and recovered, thereby forming a serum portion comprising about 7% to about 20% non-aqueous compounds, and about 80% to 93% water, said non-aqueous compounds portion comprising nonvolatile compounds and volatile compounds; said volatile compounds comprising a lower boiling fraction containing ethyl butyrate and a higher boiling fraction containing limonene; (3) passing said serum portion to a sublimation concentrating zone wherein substantially pure water is removed without removing substantial amounts of solids and wherein the initial temperature is below the eutectic temperature of said serum, whereby a concentrated orange serum is formed comprising from about 30% to about 87% solids and from about 13% to about 70% water; (4) and, thereafter, recombining said concentrated orange serum with about 9% to about 20% (V/V) of the pulp portion separated in step (2); thereby producing a natural orange juice concentrate product comprising: (A) substantially 100% of the nonvolatile compounds originally present in the solids portion of said serum; (B) at least 65% of the volatile compounds originally present in the solids portion of said serum, at least two of said volatiles being ethyl butyrate and limonene; (C) at least 0.1% of said volatile compounds being ethyl butyrate; (D) the proportion of said ethyl butyrate to said limonene being in the range of about .0015:1 to about 0.6:1, the amounts and proportions of said volatile compounds are determined by a gas chromatographic analysis of the headspace volatiles released from a sample of an orange juice, said sample having a temperature of 40° C.

Claim 34

A process according to claim 23 which additionally comprises a step of pasteurizing said serum at temperatures of from 80° C. to 95° C. for from 3 to 15 seconds in a closed system before passing into the sublimation concentration zone of step (3).

Claim 35

A process according to claim 24 which additionally comprises a step of pasteurizing said concentrated serum at temperatures of from 80° C. to 95° C. for from 3 to 15 seconds in a closed system before recombining said concentrated juice in step (4).

Claim 36

A process for making a natural orange juice concentrate product which comprises: (1) extracting orange juice from oranges, said orange juice comprising a pulp portion and a serum portion; (2) passing said juice directly to a separting zone having an inert atmosphere wherein said pulp portion is separated and recovered, thereby forming a serum portion comprising about 7% to about 20% non-aqueous compounds, and about 80% to 93% water; said non-aqueous compounds portion comprising nonvolatile compounds and volatile compounds; said volatile compounds comprising a lower boiling fraction containing ethyl butyrate and a higher boiling fraction containing limonene; (3) passing said serum portion to a freeze concentrating zone comprising an adiabatic recrystallizer wherein substantially pure ice crystals are formed and recovered without removing substantial amounts of solids, whereby a concentrated orange serum is formed comprising from about 30% to about 40% solids and from about 60% to about 70 % water; (4) passing said concentrated serum to a sublimation concentration zone wherein substantially pure water is removed without removing a substantial amount of solids and wherein the initial temperature is below the eutectic temperature of said concentrated serum, whereby a concentrated orange serum is formed comprising from about 60% to about 87% solids and from about 13% to about 40% water; (5) and, thereafter, recombining said concentrated orange juice with about 9% to about 20% (V/V) of the pulp portion separated in step (2); thereby producing a natural orange juice concentrate product comprising: (A) substantially 100% of the nonvolatile compounds originally present in the solids portion of said serum; (B) at least 65% of the volatile compounds originally present in the solids portion of said serum; (C) at least 0.1% of said volatile compounds being ethyl butyrate; (D) the proportion of said ethyl butyrate to said limonene being in the range of about 0.0015:1 to about 0.6:1, the amounts and proportions of said volatile compounds are determined by a gas chromatographic analysis of the headspace volatiles released from a sample of an orange juice, said sample having a temperature of 40° C.

Claim 37

A process for making a natural orange juice concentrate product which comprises: (1) extracting orange juice from oranges, said orange juice comprising a pulp portion and a serum portion; (2) passing said juice directly to a separting zone having an inert atmosphere wherein said pulp portion is separated and recovered, thereby forming a serum portion comprising about 7% to about 20% non-aqueous compounds, and about 80% to 93% water; said non-aqueous compounds portion comprising nonvolatile compounds and volatile compounds; said volatile compounds comprising a lower boiling fraction containing ethyl butyrate and a higher boiling fraction containing limonene; (3) passing said serum portion to a freeze concentrating zone comprising an adiabatic recrystallizer wherein substantially pure ice crystals are formed and recovered without removing substantial amounts of solids, whereby a concentrated orange serum is formed comprising from about 30% to about 40% solids and from about 60% to about 70 % water; (4) passing said concentrated serum to a sublimation concentration zone wherein substantially pure water is removed without removing a substantial amount of solids and wherein the initial temperature is below the eutectic temperature of said concentrated serum, whereby a concentrated orange serum is formed comprising from about 60% to about 87% solids and from about 13% to about 40% water; (5) and, thereafter, recombining said concentrated orange juice with about 9% to about 20% (V/V) of the pulp portion separated in step (2); thereby producing a natural orange juice concentrate product comprising: (A) substantially 100% of the nonvolatile compounds originally present in the solids portion of said serum; (B) at least 65% of the volatile compounds originally present in the solids portion of said serum; (C) at least 0.1% of said volatile compounds being ethyl butyrate; (D) the proportion of said ethyl butyrate to said limonene being in the range of about 0.0015:1 to about 0.6:1, the amounts and proportions of said volatile compounds are determined by a gas chromatographic analysis of the headspace volatiles released from a sample of an orange juice, said sample having a temperature of 40° C.

Claim 38

A process for making a natural orange juice concentrate product which comprises: (1) extracting orange juice from oranges, said orange juice comprising a pulp portion and a serum portion; (2) passing said juice to sublimation concentrating zone wherein substantially pure water is removed; the surface temperature of said juice initially not exceeding about -30° C. to about -25° C. at a pressure of less than 100 microns; thereby producing a natural orange juice concentrate product comprising: (A) substantially 100% of the non-volatile compounds originally present in the solids portion of said juice; (B) at least 65% of the volatile compounds originally present in the volatiles portion of said serum, two of said volatile compounds being ethyl butyrate and limonene; (C) at least 0.1% of said volatile compounds being ethyl butyrate; (D) the proportion of said ethyl butyrate to said limonene being in the range of about 0.0015:1 to about 0.6:1, the amounts and proportions of said volatile compounds are determined by a a gas chromatographic analysis of the headspace volatiles released from a sample of an orange juice, said sample having a temperature of 40° C.; (E) substantially 100% of the pulp originally present in the orange juice.

Claim 39

A process for making a natural orange juice concentrate product which comprises: (1) extracting orange juice from oranges, said orange juice comprising a pulp portion and a serum portion; (2) passing said juice to sublimation concentrating zone wherein substantially pure water is removed; the surface temperature of said juice initially not exceeding about -30° C. to about -25° C. at a pressure of less than 100 microns; thereby producing a natural orange juice concentrate product comprising: (A) substantially 100% of the non-volatile compounds originally present in the solids portion of said juice; (B) at least 65% of the volatile compounds originally present in the volatiles portion of said serum, two of said volatile compounds being ethyl butyrate and limonene; (C) at least 0.1% of said volatile compounds being ethyl butyrate; (D) the proportion of said ethyl butyrate to said limonene being in the range of about 0.0015:1 to about 0.6:1, the amounts and proportions of said volatile compounds are determined by a a gas chromatographic analysis of the headspace volatiles released from a sample of an orange juice, said sample having a temperature of 40° C.; (E) substantially 100% of the pulp originally present in the orange juice.

Claim 40

A process according to claim 27 wherein the pulp size is from 0.8 mm to 1.5 mm.

Claim 41

A process according to claim 28 which comprises an additional step wherein said juice is pasteurized at temperatures of from 80° C. to 95° C. for from 3 to 15 seconds in a closed system before passing into the sublimation concentrating zone.

Claim 42

A process according to claim 28 which comprises the additional step of pasteurizing said natural orange juice concentrate at temperatures of from 80° C. to 95° C. for from 3 to 15 seconds in a closed system.