Patent Application
20080075824
The present invention relates to the treatment of Brassicaceae products, particularly (but not limited to) red cabbage pigments for use in food products such as beverages, which prevents or significantly reduces the formation of off-flavors and off-odors during the shelf life of the product. These treatments include a resin treatment (cation and anion exchange resins), an enzyme treatment (galacturonases, esterases and cellulases), or a combination of those treatments. The means of using the resins and enzymes will be familiar to those skilled in the art. These processing steps, as well as optional additional steps which may be included in the processes of the present invention, are described below.
The resins which may be used to extract the myrosinase enzyme and remove nitrites and sulfur-containing compounds include strong acid cation exchange resins, weakly basic anion exchanges resins, and mixtures thereof. Preferred resins for myrosinase extraction include those composed of sulfonic acid exchange sites on crosslinked polystyrene with a particle size ranging from about 0.600 mm to about 0.800 mm. Preferred resins for sulfur-containing compound adsorption include resins composed of tertiary amine functionality on suitable matrices, for example, macroreticular styrene-divinylbenzene matrix with a particle size ranging from about 0.490 mm to about 0.690 mm. When cation exchange resins are used the preferred resin is Amberlite® FPC22 H (Rohm and Haas/Ion Exchange Resins, Philadelphia, Pa., USA). When anion exchange resins are used the preferred resin is Amberlite® FPA51 (Rohm and Haas/Ion Exchange Resins, Philadelphia, Pa., USA). The procedure removes all or substantially all of the myrosinase enzyme.
The columns containing packed beds of resin can be comprised of glass and/or stainless steel. The physical dimensions of the columns and resin beds are such that suitable flow rates and pressure drops are achieved. Columns are operated in series; preferably the cation exchanger first, followed by the anion exchanger, under conditions recommended by the manufacturer of the resin. The maximum operating temperature of the column is preferably about 60° C. Preferred operating temperature is from about 20° C. to about 27° C. The flow rate of liquid through the column can be from about 2 to about 12 bed volumes per hour. Preferred flow rate is from about 2 to about 4 bed volumes per hour.
The eluant liquid may comprise water, preferably deionized, mixture of water and water miscible organic liquids, such as ethanol and ethyl acetate, in a single phase, or solutions of acids or bases in water. Selection of the preferred eluant liquid is dependent on the plant material being processed and the resin in use. Frequently, deionized water is the preferred eluant liquid.
The enzymes which may be used to act on glucosinolates or products of myrosinase action include commercial sources of galacturonases, esterases and cellulases, and mixtures thereof, typically of microbal origin. Preferred enzymes include ferulic acid esterase from Humicola sp., cellulase with ferulic acid esterase from Trichoderma and Aspergillus sp., and endogalacturonase from Aspergillus sp. Sources of the preferred enzymes include, for example, Macer8™, Depol™ 740L, Depol™ 692L (Biocatalysts Ltd., Parc Nantgarw Wales, UK) and combinations thereof. Enzymes can be dosed at from about 250 ml per ton up to about 2% by weight. Optimum pH ranges are from about 3.0 to about 6.0; preferably from about 4.0 to about 5.0, or as specified by the enzyme manufacturer. Working temperature range is generally from about 40° C. to about 65° C., and the mixture is held for a maximum of from about 8 hours to about 16 hours. Preferred conditions are temperature of about 55° C. to about 60° C. held from about 1 hour to about 8 hours.
Additional processing steps can be performed to obtain the desired end product. The pigment, extract or juice can be concentrated by, for example, vacuum distillation using about 40 mm Hg to about 50 mm Hg and temperature from about 22° C. to about 50° C., or other conditions of pressure and temperature in suitable stills such as short path length stills, as known to those practiced in the art.
It may be desirable to alter the pH of the deodorized pigment, extract and juice, specifically when working with pigments, extracts, and juices containing, for example, red cabbage. The pH may be adjusted using a dilute food grade acidic or caustic solution.
Red cabbage pigment itself may be manufactured, for example, as follows: Macerate cabbage and add deionized water. Heat to from about 40° C. to about 50° C. Use dilute sulfuric acid to adjust the pH of the slurry to from about 2 to about 3. Processing enzymes, for example, pectinase can be added up to about 250 ppm to aid in the extraction of color from the plant material. The slurry is pressed to separate the liquid from the solid plant material. Further filtration is performed to clarify the pigment. The product may be concentrated if desired.
The following examples are provided to illustrate the invention and are not intended to limit the scope thereof in any manner.
After the manufacturing procedure described above, the following processing steps are performed using a red cabbage pigment. The cation exchange and anion exchange resins are loaded in two separate columns. The resin is activated according to manufacturer's instructions using a series of caustic and acidic rinses. The deodorization is carried out by introducing the aqueous red cabbage pigment into the chromatographic column including a cation exchange resin bed and continuing to pass the pigment solution through the chromatographic column until the discharge from the column outlet is of similar color to the feed entering the column, whereupon the feed is stopped. Elution of the pigment is carried out by passing deionized water into the chromatographic column including a cation exchange resin and the bound pigment and continuing to pass the deionized water through the column until at least one bed volume has been passed and the eluate is minimally colored. Red cabbage pigment that has passed through the column is considered “pretreated.”
Deodorization is completed by passing the aqueous “pretreated” pigment solution into the chromatographic column containing anion exchange resin and continuing to pass the pigment solution through the chromatographic column until the resin bed is saturated with color, as indicated by the discharge from the column outlet being of similar color intensity to that entering the column. Elution of the red cabbage pigment is carried out by passing deionized water through the chromatographic column including an anion exchange resin bed and the pigment and continuing to pass deionized water through the chromatographic column until at least one bed volume has been passed and the eluate is minimally colored. Pigment that has passed through the column is considered “treated.”
Treated pigment is acidified by, for example, adjusting the pH using a 10% w/v sulfuric acid solution to from about 1 to about 3. The red cabbage pigment is then concentrated to the desired color unit value by vacuum distillation using a Rotavapor at 40 mm Hg, and from about 40° C. to about 50° C.
Using the manufacturing procedure described above, the following processing steps are performed using a red cabbage pigment. The pH of the red cabbage pigment is increased to from about 4.0 to about 5.0 using a dilute food grade caustic solution. The pigment is dosed with Macer8™ and Depol™ 692L (cellulase and ferulic acid esterase from Trichoderma and Aspergillus sp. microorganisms). The enzyme is dosed at from about 1% to about 2% by weight and incubated for about 1 hour to about 2 hours at from about 55° C. to about 60° C. Pigment that has been incubated with enzyme is considered “enzyme treated.”
Enzyme treated red cabbage pigment is acidified by adjusting the pH using a 10% w/v sulfuric acid solution to from about 1 to about 3. The red cabbage pigment is then concentrated to the desired color unit value by vacuum distillation using a Rotavapor at 40 mm Hg, and from about 40° C. to about 50° C.
This application is related to and claims priority from U.S. Provisional Patent Application Ser. No. 60/826,818, filed Sep. 25, 2006, incorporated herein by reference.
| Number | Date | Country | |
|---|---|---|---|
| 60826818 | Sep 2006 | US |
