Process for conversion of citrus peels into fiber, juice, naringin, and oil
View Patent ↗Processes for converting by-products of citrus, such as peels and juice from juice sacs attached to the peel after hand or mechanical peeling into high quality dietary fiber, naringin, juice, and oil. The processes involve pressing peels to release juice from vesicles and then grinding peels in water to create a slurry. Peel color and oil is removed by a flotation technique. Decolorized citrus peel particles—or pulp—are debittered with water in steps of boiling and washing. Dietary fiber obtained after debittering is dried and packaged for commercial use. The process promotes environmental responsibility by reducing standard citrus waste—a high BOD waste product, by overcoming discharging problems with industrial waste, by converting an environmentally undesirable product—peels, juice, and oils—into a value-added ingredient, by drastically reducing discharge and penalty cost of waste, and by eliminating the use of solvents that generate pollution.
1. A process for converting citrus peel waste into citrus oil, citrus fiber, and naringin comprising:
pressing citrus peels having residual vesicles attached thereto with sufficient pressure to release citrus juice from within the vesicles;
removing the citrus juice from the pressed citrus peels;
pulverizing the citrus peels in water to create a slurry of particles;
separating the slurry of particles into citrus peel puree and a first supernatant, wherein the first supernatant comprises solubilized naringin and citrus oil; and
collecting debittered citrus pulp from the citrus peel puree using a washing process, wherein the washing process comprises creating a suspension of the citrus peel puree in water, heating the suspension to a temperature ranging from about 150° F. to about 230° F. and then separating the suspension into debittered citrus pulp and a second supernatant.
2. The process of claim 1 wherein the pressing comprises applying force to the citrus peels in a range of about 5 psig to about 15 psig.
3. The process of claim 1 wherein the slurry of particles comprises peel particles in a range from about 0.1 mm to about 10 mm in size.
4. The process of claim 1 wherein the slurry of particles comprises a ratio of water to peel particles ranging from about 0.1:1 to about 200:1 by weight.
5. The process of claim 1 comprising combining a macerating enzyme with the slurry of particles to liquefy the particles.
6. The process of claim 1 wherein the step of separating the slurry of particles into citrus peel puree and a first supernatant comprises decanting, centrifuging, pressing, or filtering.
7. The process of claim 1 comprising separating the first supernatant into citrus oil and soluble citrus components comprising naringin using centrifugation or gravity separation.
8. The process of claim 7 comprising refining the citrus oil.
9. The process of claim 7 comprising filtering the soluble citrus components and then passing the filtered soluble citrus components comprising naringin over an adsorbent resin, wherein the naringin is adsorbed to the resin and removed from the filtered soluble citrus components.
10. The process of claim 9 comprising desorbing naringin adsorbed to the resin with a solvent and eluting the naringin in a solution.
11. The process of claim 10 wherein the naringin in the solution is crystallized.
12. The process of claim 1 comprising recycling the second supernatant into the slurry of particles.
13. The process of claim 1 wherein the washing process is repeated at least one time.
14. The process of claim 1 wherein the washing process is repeated 3 times.
15. The process of claim 1 comprising drying the debittered citrus pulp into a fiber granulate.
16. The process of claim 15 wherein the fiber granulate comprises a moisture content in a range of about 0.5% to about 20% by weight.
17. The process of claim 15 wherein the drying of the debittered citrus pulp can occur with or without heat at atmospheric pressure or in a vacuum.
18. The process of claim 15 wherein the fiber granulate has a total dietary content ranging from about 5% to about 95% by weight.
19. The process of claim 15 wherein the fiber granulate has a crude dietary fiber content ranging from about 5% to about 95% by weight.
20. The process of claim 15 wherein the fiber granulate has a soluble fiber content ranging from about 5% to about 10% by weight.
21. The process of claim 15 comprising pulverizing the fiber granulate into sizes ranging from about 4 mesh Tyler to about 200 mesh Tyler.
22. The process of claim 1 comprising converting the citrus juice into a debittered juice by using a non-enzymatic process or an enzymatic process.
23. The process of claim 22 wherein the non-enzymatic process comprises passing the citrus juice over a resin and collecting debittered juice, wherein the resin adsorbs naringin thereby removing naringin from the citrus juice.
24. The process of claim 23 comprising desorbing naringin adsorbed to the resin with a solvent and eluting the naringin in a solution.
25. The process of claim 24 wherein the naringin in the solution is crystallized.
26. The process of claim 23 comprising flowing the debittered juice over decolorizing resin, wherein the decolorizing resin adsorbs unwanted colors and color precursors.
27. The process of claim 22 wherein the enzymatic process comprises converting the citrus juice into debittered juice by hydrolyzing soluble naringin with an enzyme.
28. The process of claim 27 wherein the enzyme is added to the citrus juice at a rate of about 0.001% to about 1.00% by weight of the citrus juice for about 5 minutes to about 5 hours, wherein the temperature of the citrus juice is about 35° F. to about 150° F.
29. The process of claim 27 comprising inactivating the enzyme after soluble naringin is hydrolyzed by heating the debittered juice with enzyme added thereto to a temperature ranging from about 165° F. to about 220° F.
30. The process of claim 29 comprising filtering the debittered juice through a filtration membrane and then flowing the filtered, debittered juice over decolorizing resin, wherein the decolorizing resin adsorbs unwanted colors and color precursors.
31. The process of claim 29 comprising centrifuging the debittered juice, removing a supernatant from the centrifuged, debittered juice, and then flowing the supernatant comprising naringin over decolorizing resin, wherein the decolorizing resin adsorbs unwanted colors and color precursors.
32. A process for extracting citrus oil, naringin, juice, and citrus fiber from citrus peel waste comprising:
pressing citrus peels having residual vesicles attached thereto with sufficient pressure to release citrus juice from within the vesicles, wherein the citrus juice is removed from the citrus peels;
pulverizing the citrus peels in water to create a slurry of particles;
separating the slurry of particles into citrus peel puree and a first supernatant, wherein the first supernatant comprises solubilized naringin and citrus oil;
collecting debittered citrus pulp from the citrus peel puree using a washing process, wherein the washing process comprises creating a suspension of the citrus peel puree in water, heating the suspension to a temperature ranging from about 150° F. to about 230° F. and then separating the suspension into the debittered citrus pulp and a second supernatant; and
separating the first supernatant into citrus oil and soluble citrus components comprising naringin.
33. The process of claim 32 wherein the slurry of particles comprises a ratio of water to peel particles ranging from about 0.1:1 to about 200:1 by weight.
34. The process of claim 32 wherein the slurry of particles comprises peel particles in a range from about 0.1 mm to about 10 mm in size.
35. The process of claim 32 wherein the process comprises adding a macerating enzyme to the slurry of particles to liquefy the particles.
36. The process of claim 32 wherein the step of separating the slurry of particles into citrus peel puree and a first supernatant comprises decanting, centrifuging, pressing, or filtering.
37. The process of claim 32 wherein the step of separating the first supernatant into citrus oil and soluble citrus components comprises using centrifugation or gravity separation.
38. The process of claim 37 comprising filtering the soluble citrus components and passing the filtered soluble citrus components comprising naringin over an adsorbent resin, wherein the naringin is adsorbed to the resin.
39. The process of claim 38 comprising desorbing naringin adsorbed to the resin with a solvent and eluting the naringin in a solution.
40. The process of claim 38 wherein the naringin in the solution is crystallized.
41. The process of claim 32 comprising drying the debittered citrus pulp into fiber granulate.
42. The process of claim 32 comprising passing the citrus juice over a resin, wherein the resin adsorbs naringin thereby removing naringin from the citrus juice.
43. The process of claim 42 comprising desorbing naringin adsorbed to the resin with a solvent and eluting the naringin in a solution.
44. The process of claim 43 wherein the naringin in the solution is crystallized.
45. A process for reducing citrus peel waste from citrus juice or segmenting processing comprising:
pressing citrus peels having residual vesicles attached thereto with sufficient pressure to release citrus juice from within the vesicles, wherein the citrus juice is removed from the citrus peels;
pulverizing the citrus peels in water to create a slurry of particles;
separating the slurry of particles into citrus peel puree and a first supernatant, wherein the first supernatant comprises solubilized naringin and citrus oil;
collecting a debittered citrus pulp comprising dietary fiber using a washing process, wherein the washing process comprises creating a suspension of the citrus peel puree in water, heating the suspension to a temperature ranging from about 150° F. to about 230° F. and then removing a second supernatant from the debittered citrus pulp, and wherein the second supernatant is recycled into the slurry of particles; and
separating the first supernatant into citrus oil and soluble citrus components comprising naringin.
46. A process for eliminating pollution generating solvents from processing citrus peel waste comprising:
pressing citrus peels having residual vesicles attached thereto with sufficient pressure to release citrus juice from within the vesicles, wherein the citrus juice is removed from the citrus peels;
pulverizing the citrus peels in water to create a slurry of particles;
separating the slurry of particles into citrus peel puree and a first supernatant, wherein the first supernatant comprises solubilized naringin and citrus oil;
collecting a debittered citrus pulp comprising dietary fiber from the citrus peel puree using a washing process, wherein the washing process comprises creating a suspension of citrus peel puree in water, heating the suspension to a temperature ranging from about 150° F. to about 230° F. and then removing a second supernatant from the debittered citrus pulp, and wherein the second supernatant is recycled into the slurry of particles; and
separating the first supernatant into citrus oil and soluble citrus components comprising naringin.
47. A process for extracting citrus oil from citrus peel waste produced from juicing or segmenting operations comprising:
pressing citrus peels with mechanical force ranging from about 5 psig to about 15 psig to extract citrus juice from vesicles attached to the citrus peels;
grinding the citrus peels in water to create a slurry of peel particles;
combining a macerating enzyme with the slurry of peel particles to liquefy the peel particles;
removing a liquid from the slurry peel particles by pressing, centrifuging, or filtering the slurry of peel particles, wherein the liquid comprises citrus oil and soluble flavanoids;
separating the liquid into a water soluble phase and a water-insoluble phase comprising citrus oil; and
removing the water-insoluble phase from the water soluble phase and refining the water-insoluble phase into citrus oil.