WO2006088884A1

WO2006088884A1 - Methods of making syrups

Info

Publication number: WO2006088884A1
Application number: PCT/US2006/005210
Authority: WO
Inventors: Ting L. Carlson; Anton Woo; Guo-Hua Zheng
Original assignee: Cargill, Incorporated
Priority date: 2005-02-15
Filing date: 2006-02-15
Publication date: 2006-08-24
Also published as: EP1856270A4; US20090123603A1; EP1856270B1; BRPI0608080A2; CA2597886A1; AU2006214433A1; EA200701742A1; CN101258248A; CN101258248B; BRPI0608080B1; EP1856270A1; CA2597886C; ES2444847T3; JP2008529534A; MX2007009899A; AU2006214433B2; JP5094419B2

Abstract

Provided herein are methods of making a substantially clear syrup comprising reacting one or more substrates at a concentration of at least 40 % w/w with at least one alternan sucrase enzyme at a temperature of greater than 45°C.

Description

Methods of Making Syrups

Background

Corn syrups for use in the production of beverages (e.g., sports drinks) and other food applications are known. It would be desirable, however, to have available for use in beverages and other food applications, as required, a product having sweetness and functionality that is similar to corn syrup, yet having a lower glycemic index.

Summary

Provided herein are efficient methods of making substantially clear low-glycemic syrups (LGS) that comprise alteman oligosaccharides. These syrups have a relatively low glycemic index and are additionally useful in applications where increased clarity are desired. These qualities are particularly beneficial in food and beverage formulations.

In some embodiments the methods of making the substantially clear LGS involve reacting one or more substrates (initial sucrose and one or more initial acceptors selected from a sugar or sugar alcohol having free hydroxyl groups at one or more of carbon positions numbers 2, 3 and 6 that can accept a glucose unit from sucrose) at a concentration of at least about 40 % w/w with at least one alternan sucrase enzyme at temperatures of greater than 45⁰C. In additional embodiments the substrate is at a concentration of at least about 41, 42, 43, 44, 45, 46, 47, 48, 49, 50, 51, 52, 53, 54, or 55% w/w. In additional embodiments that substrate and enzyme can be reacted at temperatures of greater than 46, 47, 48, 49, 50, or 51°C.

In some embodiments the methods involve reacting one or more of the alternan sucrases with the substrate for relatively short period of time, such as less than 12 hours, or less than 11, 10, 9, 8, or 7 hours.

Substantially clear LGS made at temperatures greater than 45°C and substrate concentrations of at least 40 %w/w are typically visually clearer when compared to syrups made at lower temperatures and lower substrate concentration. Clarity can also be determined using the test procedure described herein. In some embodiments the substantially clear LGS when adjusted to a concentration of 20 % w/w will display a transmittance at 650 nm of greater than 93%, or greater than 94, 95, 96, 97, 98, or 99%.

In some embodiments the substantially clear LGS comprises less than 0.5% alternan that is greater than DP 12 (degree of polymerization of glucose units).

In some embodiments the methods provide substantially clear LGS that have low viscosity, such as a viscosity of less than 14,000 cps at 80⁰F and 77% dry solid concentration. In other embodiments the substantially clear LGS when measured at 80⁰F and 77% dry solid concentration will display a viscosity of less than 10000, 9000, 8000, 7000, 6000, 5000 or 4,000 cps.

In some embodiments the alternan sucrase enzyme used can be made from recombinant methods such as those described in US6,570,065. In additional embodiments the recombinant enzyme will be smaller or truncated when compared to the full-length enzyme "Characterization of alternansucrase from Leuconostoc mesenteroides NNElL B- 1355: rational and random approach to design of novel glucansucrase" Gilles Joucla, Doctroal Dissertation, Ingenier INSA, Toulouse, France, 2003.

In another aspect, the invention provides a method of making a food or beverage comprising mixing one or more ingredients with a substantially clear syrup made by contacting one or more substrates at a concentration of at least 40 % w/w with at least one alternan sucrase enzyme at a temperature of greater than 45°C.

These and other objects and advantages of the present invention will be apparent to those skilled in the art from the following detailed description and claims.

Detailed Description I. Methods of making syrups

The substantially clear LGS described herein display a variety of physical characteristics. More specifically, alternan oligosaccharides can be produced from an acceptor and sucrose that are reacted with one or more alternan sucrase enzymes that will transfer glucose units from sucrose to an acceptor carbohydrate and will release fructose and glucose oligosaccarides of various lengths. The resultant product may have a level of sweetness similar to that of a corn syrup, and a mouth-feel and functionality similar to that of corn syrup. In addition, and more significantly for the present methods, the resulting product may be characterized in some embodiments by having a lower glycemic index as compared to the combination of the substrates (sucrose and acceptors) that are not reacted with enzyme. These syrups are referred to as substantially clear low-glycemic syrups (LGS).

The acceptor can be selected from the group consisting of a sugar or a sugar alcohol having free hydroxyl groups at one or more carbon positions numbers 2, 3 and 6 that can accept a glucose unit from sucrose. The acceptor can be in the form of syrup or syrup solids. Exemplary of the syrups or syrup solids suitable for use herein are maltose, maltotriose, panose, high maltose (over 40%) corn syrup, medium to low DE (dextrose equivalent) corn syrup, raffinose, cellobiose, maltitol, maltotriose, maltotetrose, glucose, isomaltose, isomaltitol, barley syrup and syrup solids, rice syrup and syrup solids, lactose, whey permeate, tapioca starch syrup and syrup solids, nigerose, kojibiose, isomaltooligosaccharide, hydrogenated starch syrup, potato starch syrup and syrup solids, corn syrup and syrup solids, and the like. Exemplary of the syrups that are suitable for use in the blends are, but not limited to, SATINSWEET™, available from Cargill, Incorporated, that contains minimal 55 to 70 weight % maltose and 45 to 30% weight % of glucose and other glucose-containing oligomers. In one embodiment, the syrup or syrup solids used comprise an amount of from about 2 to about 99% by weight of maltose.

The alternansucrase enzymes that can be used in the reaction to produce the LGS include, but not limited to, Leuconostoc Mesenteroides (LM) strains NRRL B 1355,23185, 23186, 23188, 23311, 21297, 30821, 30894 and other enzymes provided herein. These enzymes can be additionally cloned and expressed recombinantly, such as described in Gilles Joucla, Doctroal Dissertation, Ingenier INSA, Toulouse, France, 2003. These strains can be cultured and the enzymes can be isolated using any method known in the art, such as the methods provided below.

The physical characteristics of the syrups produced can be altered by using different reaction conditions. For example, a substantially clear LGS can be produced by reacting one or more of the alternan sucrase enzymes in a reaction with relatively high concentration of sucrose and acceptor. Moreover, the efficiency of the reaction can be increased by reacting at a temperature of greater that 45°C. This allows for less enzyme to be needed in order to achieve completion (when the remaining substrate is <2% of the total carbohydrates w/w basis) of the reaction, and the reaction can be completed in a shorter period of time. For example, the reaction, can be carried out at a temperature of greater than 45° C for a period of less than 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, or less than 20 hours. The increased temperature may also lessen the risk of microbial contamination in some embodiments.

The characteristics of LGS can be altered by controlling the ratio of sucrose to acceptor. Generally, the glycemic index of the substantially clear LGS will decrease as the ratio of sucrose to acceptor increases up to a ratio of about 12:1. For example, it is expected that a product made using a ratio of 1: 1 (sucrose to acceptor) will have a higher glycemic index than that of a product made using a ratio of 4:1 (sucrose to acceptor). In some embodiments a ratio of from about 8:1 to about 11:1 are used. In other embodiments, the methods comprise making LGS using ratios of sucrose to acceptor of at least 4:1, 5:1, 6:1, 7:1, 8:1, 9:1, and 10:1. Accordingly, the invention also provides food and beverage products made by such methods.

The LGS can also be characterized by the linkages between the glucose molecules in the glucose oligosaccaride. In some embodiments the glucose oligosaccaride has both alpha 1,3 and alpha 1,6 linkages. In some embodiments, the glucose oligosaccaride also contains other linkages such as alpha 1,4. In some embodiments that LGS will have at least 20% alpha 1,3 linkages. In other embodiments the LGS will have at least 20% alpha 1,3 linkages and at least 20% alpha 1,6 linkages.

In some embodiments, the substantially clear LGS is subsequently processed to remove a portion of, or all of, the fructose, thus yielding a LGS that is fructose depleted. Fructose can be removed from the LGS using any method known in the art, for example by using column chromatography. Generally, the LGS contains less than 50% fructose.

The substantially clear LGS and/or the fructose depleted LGS can further be hydrogenated to make a non-reducing syrup.

In other embodiments an oligoalteran with a degree of polymerization of 7 to 12 is provided that is a slowly but fully digestible carbohydrate which makes LGS a unique sweetener that offers a low glycemic response and sustained energy without any intestinal discomfort or side effects. Strains NRRL B 30821 and NRRL B 30894 are constitutive mutants of strain NRRL B 21297 (Leathers et al, 1997) generated by chemical mutagenesis. Hence, sucrose is no longer required to induce the maximal production of alternan sucrase in strain NRRL B 30821.

II Products and Blends including a substantially clear low-glycemic syrup (LGS) The substantially clear LGS described herein can be blended with one or more of a variety of other ingredients and can be sold to formulators as blends, or the components for the blends can be provided to the formulator separately and the formulator can blend them while making a final food product. Substantially clear LGS can be blended with one or more other ingredients such as vitamins, minerals, sugar alcohols, high intensity sweeteners, flavors, flavor enhancers, and other conventional sweeteners to provide the desired nutritional impact as well as the desired flavor. The creation of blends with substantially clear LGS is expected to improve the homogeneity of the end products. Vitamins that can be blended with substantially clear LGS include any of a group of organic substances other than proteins, carbohydrates, fats, minerals, and organic salts wllich are essential for normal metabolism, growth, and development of the body. Vitamins include compounds such as A, D, E, I, biotin, choline, folic acid, and nicotinic acid. Mineral compounds that can be blended with substantially clear LGS include inorganic compounds of mineral elements, which constitute the mineral constituents of the body. Mineral salts and water are excreted daily from the body and, therefore, need to be replenished. These must be replaced through food or supplement intake. Examples of minerals include Ca, Fe, P. Na, Cu, K, and Mg. Flavors and/or flavor enhancers can be also blended with LGS. For example dihydroxybenzoic acid (DHB, including all isomers) as well as flavors such as peppermint, cocoa, and vanilla.

Sugar alcohols can be blended with LGS and used to impart sweetness to a particular food product and in many instances the sugar alcohol will not contribute as greatly to the caloric content of the product when compared to conventional sweeteners. Sugar alcohols are characterized by the presence of a hydroxyl group on a ketose sugar or hexose sugar. Examples of sugar alcohols that can be blended with the LGS sweeteners described herein include sorbitol, Io manitol, xylitol, lactitol, maltitol, isomalt, hydrogenated starch hydrolysate, and erythritol.

LGS disclosed herein can also be blended with high-intensity sweeteners. High- intensity sweeteners are agents that exhibit sweetening powers at very low concentrations. Examples of high-intensity sweeteners that can be blended with the LGS compositions described herein include saccharin, cyclamate, aspartame, monatin, alitame, acesulfame potassium, sucralose, thaumatin, stevioside, and glycynhizin.

Additional examples of uses and products that can be made using substantially clear LGS are included in WO2004023894A1 and WO2005089483A2, which are herein incorporated by reference.

The following examples provide specific embodiments and one of ordinary skill in the art will recognize that these examples are given for the purpose of illustration only not to be construed as limiting the scope of what is claimed any way.

Examples

Example 1, Method of making enzyme solution

Enzyme preparations were generated by growing Leuconostoc Mesenteroides NRRL B 30821 or NRRL B 30894, on media containing 10 g/L yeast extract, 5 g/L potassium phosphate, 0.2 g/L magnesium sulfate (heptahydrate), 0.1 g/L manganese sulfate (monohydrate), 0.02 g/L calcium chloride, 0.01 g/L sodium chloride, 0.01 g/L ferrous sulfate (heptahydrate) and 20-40 g/L glucose from various sources. Leuconostoc Mesenteroides NRRL B 21297 culture was grown in the same medium except with 2% sucrose and 2% high maltose corn syrup (65% maltose) as the carbon source. Cultures were grown at 27-30°C and with pH control at 6.0 (with 10% NaOH) until carbohydrate was consumed. Once the carbon source was depleted, cells were removed by centrifugation at 12,200 x g at 4°C for 30 minutes. The clarified culture supernatant was concentrated by ultrafiltration through a 50,000 molecular weight cutoff (50 kD MWCO) membrane to obtain a 10-fold enzyme concentrate by volume. Both strains NRRL B 30821 and NRRL B 30894 were derived from Leuconostoc Mesenteroides NRRL B 21297 by chemical mutagenesis and express alternan sucrase constitutively when grown on glucose medium. Example 2, Assay to determine digestibility

The digestibility of the resulting syrup was determined by an in vitro digestion assay. 2 mL of 8% testing syrup was mixed with 10 μL of glucoamylase (Optidex L-400 from Genencor International, Palo Alto, CA), and 2 mL of 0.019 M acetate buffer, pH=4.5, and incubated at 60°C for 16-20 hours. After the digestion, 2 mL of the syrup was withdrawn and mixed with 2 mL of 0.05 M phosphate buffer, pH=6.5, 0.1 mL of 1% NaN3, and 0.1 g of rat intestinal powder (Catalog* 1-1630, Sigma-Aldrich Fine Chemicals, St. Louis, MO, USA) and incubated at 37°C for up to 24 hours. At each time point, 0.5 mL of the mixture was mixed with 1 mL of 1.2 N HCl to stop further reaction. The amount of glucose release by glucoamylase and rat intestinal enzyme hydrolysis was determined by HPLC using an Aminex HPX-87H column, available from Bio-Rad Laboratories (Hercules, CA), with 0.01N (normal) sulfuric acid as the mobile phase at 0.6 ml/min and 60°C. Digestibility was expressed as % glucose released from the total gluco- oligosaccharides and is calculated by the following equation:

% Theoretical glucose release = [glucose]/[fructose]*0.45/0.55*100

Alternatively, the initial glucoamylase treatment step can be omitted.

Example 3, Enzyme assay and unit definition

To 2.5 mL of 40% (w/v) sucrose to maltose at a 9:1 ratio and 0.1 ml of 1.5 M citrate buffer, pH 5.5, 0.1 to 2.4 mL of concentrated enzyme was added. The volume was brought up to 5.0 ml with nanopure water and the reactions were incubated at 37°C. After 1 hour, 0.5 mL of each reaction was placed in a 90-100°C water bath for 5 minutes. After a short cooling period, 1.0 mL of nanopure water was added to the 0.5 mL samples and 0.05-0.1 g of an ion exchange mixture consisting of Dowex 66 and Dowex 88 (Dow Chemical Co., Midland, MI) was added. The samples were inverted for 2-3 minutes and were filtered through 0.45 μm nylon filter (Whatman, Clifton, NJ) into HPLC vials.

Samples were run on an HPLC through an HPX-87C carbohydrate column (300mm X 7.8 mm) (Bio-Rad, Hercules, CA) at 85°C with water as the mobile phase at 0.9 mL/min. Calculations were based upon the percent area of fructose relative to the area of total sugars. The calculation is as follows: Percent fructose * 1 g total sugar in 5 mL reaction/ 1 h/ volume of enzyme broth used = g fructose/h/mL of activity.

Values are then converted to μmole fructose/min/ml using the formula weight of fructose and metric conversions. One unit is defined as the release of 1 μmol of fructose/minute at 37°C and values are reported in U/mL.

Example 4: Low glycemic syrup sugar profile analysis

The oligosaccharide profile of low glycemic syrup is analyzed by a HPLC method as described below. A sample of low glycemic syrup is diluted with deionized water to 5- 10% dry solids, de-ashed with ion exchange resins (Dowex 66/Dowex 88, Dow Chemical Co., Midland, MI), and filtered through a 0.45 micron filter before injection into the HPLC for sugar analysis. The oligosaccharide separation is accomplished by using two BioRad Aminex HPX-42A, 300-7.8 mm, columns (Hercules, CA) in series at 65°C and with a refractive index detector. Water is used as the eluent at a flow rate of 0.2 ml/min. The chromatogram of a typical low glycemic syrup sample (PDF8) is shown in Fig. 1. The sequential peaks shown on the chromatogram are assigned as oligomers of increasing degree of polymerization (DP). For example, DP3 is a trisaccharide and DP4 is a tetrasaccharide.

The peak that elutes in the shortest time at the far left is assigned as a polymer peak with a molecular weight of at least 250,000.

Example 5, Enzymatic conversion of sucrose/maltose substrate (sucrose:maltose ratio = 9:1) to specialty clear syrup at high temperatures

Substantially clear LGS with slow digestibility and low viscosity can be made at temperatures higher than 45° C. At the elevated temperatures, the rate of converting sugar substrates to the clear syrup is greatly increased. Because of increased reaction rates at high temperatures, the enzyme usage, conversion time length and the risk of microbial contamination during processing are greatly reduced. This is of particular importance in commercial production, offering economic advantages for production of the substantially clear LGS. An enzyme preparation was obtained from Leuconostoc Mesenteroides NRRL B 30821 as described in Example 1. The enzyme preparation had an activity of 92.5 Units/mL as defined in Example 3. The specific gravity of the enzyme preparation and the water was assumed at 1 g/mL. Crystalline sucrose and maltose, both purchased from Sigma-Aldrich Fine Chemicals (St. Louis, MO, USA), were dry mixed at sucrose:maltose ratio of 9:1 on a dry weight basis and ground in a coffee grinder to obtain a homogenous powdery substrate mixture, referred to as the substrate hereafter. The sugar substrate was dissolved in de-ionized water to final concentrations of 20, 30, 40 and 50% weight-by- weight including the addition of the enzyme preparation in 50-mL capped polypropylene test tubes. An aliquot of 0.17 mL of the enzyme preparation was added to each test tube, to yield varying enzyme dosages (Table 1). The total weight of the substrate, water and the enzyme was 8.50 g in each test tube. The test tubes were placed in water baths set at 37 ° C, 45 ° C, 50 ° C and 55 ° C for 30 min for the substrate solution to be equilibrated to respective temperatures before enzyme addition.

Table 1. Substrate concentration, enzyme dosage and the amounts of substrate and water contained in each test tube. 0.17 mL of enzyme was added to each test tube (equivalent to 15.7 total units).

After the addition of enzyme preparation, the test tubes were placed back into their respective water baths at 37 ° C, 45 ° C, 50° C and 55 ° C. After 20 hours of incubation, a small sample was drawn from each test tube. The remaining substrate in the samples was analyzed by HPLC as described in example 3 except the percent area of substrate was calculated against the total sugar areas. The average reaction rate during the 20 hr reaction was calculated as μmols of substrate depleted per hour per unit of enzyme (μmols substr ate/hr/unit) .

Table 2, below, provides the results of the reaction and shows that reactions at higher temperature and higher substrate concentration showed higher substrate conversion and higher reaction rate. As a result, one of ordinary skill in the art will appreciate that less enzyme is needed to complete the reaction in less time at high temperatures and high substrate concentrations than at lower substrate concentrations and lower temperatures. For example, 97% substrate utilization was achieved at 50% substrate concentration and 5O ⁰C with 3.7 U/g enzyme, 98% substrate completion at 40% concentration and 45⁰C with 4.63 U/g enzyme as compared to 98% substrate depletion at 30% concentration, 37 ° C with 6.17 U/g enzyme within 20 hours. It required 9.25 U/g enzyme to complete a 20% concentration reaction at 37⁰C. From an industrial operation standpoint, reactions at high substrate concentration also offer the benefits of reduced usage of water and energy. From this experiment, one of ordinary skill in the art will also appreciate that a much longer time will be required to complete the reactions at high substrate concentration and low temperature (e.g. 37⁰C), due to a slow reaction rate.

Table 2. Effects of substrate concentration and temperature on substrate conversion and reaction rate

Example 5, Chemical and physiological properties of clear syrups made at high temperatures

An enzyme preparation was obtained from Leuconostoc Mesenteroides NRRL B 30821 as described in Example 1. The enzyme preparation had activity of 92.5 Units/mL as defined in Example 3. The specific gravity of the enzyme preparation and the water was assumed at ig/mL. Crystalline sucrose and maltose, both purchased from Sigma- Aldrich Fine Chemicals (St. Louis, MO, USA), were dry mixed at sucrose : maltose ratio of 9:1 on dry weight basis and ground in a coffee grinder to obtain a homogeneous powdery substrate mixture, refereed as the substrate hereafter. The sugar substrate was dissolved in de-ionized water to final concentrations of 50 and 60% weight-by- weight including the addition of the enzyme preparation in 50-mL capped polypropylene test tubes. Aliquots of the enzyme preparation were added to each test tube to obtain final enzyme dosages of 2U/g, 5U/g and 8U/g. The total weight of the substrate, water and the enzyme was 20 g in each test tube. The test tubes were placed in water baths set at 50 ° C for 30 min for the substrate solution to be equilibrated to respective temperatures before enzyme addition.

After 48 hours at 50 ° C, the samples were analyzed for their sugar composition using dual Aminex HPX-42A HPLC column described in Example 3. Digestibility of the samples were determined my method described in Example 2.

In general, syrups made at high temperature and high substrate concentration contained less polymer and more leucrose, but similar amounts of gluco-oligosaccharides (Table 3). Because the in vitro digestion rate was largely attributable to the contents of oligosaccharides, syrups made at high temperature and high substrate concentration showed similar in vitro digestibility as that made at a low temperature and low substrate concentration. The in vitro digestion rate results showed similar digestion rates among the samples tested. Under the same digestion condition, maltose or malto-oligosaccharides is 100% digested within 8 hours (data not shown).

Table 3. Sugar profile and in vitro digestibility of clear syrup made at high temperatures in comparison with that made at a low temperature

Example 6, Clarity of syrups made at high temperatures

Because of reduced polymer concentrations, syrups made at high temperatures exhibited another important characteristic, in that they are clear.

Syrup samples produced at 20% (w/w) substrate concentration and 37 ⁰C at the Cargill Process Development Facility in Savage (MN, USA), PDF03, PDF04, PDF06, PDF08, and PDFlO, were compared to those produced at 50% (w/w) substrate concentration and 5O⁰C. A sample produced from PDF07 by ultrafiltration (5OkD MWCO) to remove alternan polymer was also included in the comparison. All samples were diluted with de-ionized water from -80 % dry solid to 50, 40, 30, 20, 10 and 5 % dry solid and light transmittance measured with a spectrophotometer (Hewlett Packard, Model 8453) at 650 nm using a 1-cm cell. Prior to measuring the transmittance of the test samples the spectrophotometer was calibrated with de-ionized water. As shown in Table 4, all the samples made at 20% substrate concentration and 37⁰C except PDF07 with the polymer removed by ultrafiltration had light transmittance of less than 96.1% and looked opaque at concentrations of 40 % dry solid or below. Conversely, the sample made at high temperature was as clear as that with polymer removed by ultrafiltration throughout the entire concentration range (from 0.5 % dry solid to 85 % dry solid).

Table 4. Light transmittance of a syrup made at high temperature as compared with those made at low temperature with or without polymer removed by ultrafiltration.

Example 7, Syrup made with NRRL B 30894 at high temperature

Enzyme preparation from strain Leuconostoc Mesenteroides NRRL B 30821 and strain NRRL B 30894 was done according to Example 1. Syrup batch-PDF12 was made with 3 U/g substrate of enzyme from Leuconostoc Mesenteroides NRRL B 30894 at 50⁰C and 50% total sugar at a sucrose to maltose ratio of 9. Syrup batches PDF6 and PDF7 were made with NRRL B 30821 enzyme at a dosage of 6 U/g substrate at 37⁰C and 20% total sugar with a sucrose to maltose ratio of 9. The digestion assay was done as described in Example 2 without the glucoamylase pretreatment step. The viscosity measurement was performed at various temperatures with two different lots of syrup at 77% dry solid using a Brookfield DV-E Viscometer (Brookfield Engineering Labs, Inc., Middleboro, MA).

Syrup batches PDF6 and PDF7 were opaque and syrup batch PDF12 was a clear syrup. The sugar profile of the two types of syrups made at low (PDF7) and high temperature (PDF12) is shown in Table 6 and showed there was no polymer present in syrup PDF12. The clear syrup had a significantly lower viscosity as compared to the opaque syrup at the same dry solid levels (Table 7) and is digested by rat intestinal powder at a similar rate as the opaque syrup (Table 8).

Table 6: Sugar profile of clear and opaque syrup (in % of total sugar)

Table 7: Viscosity comparison of clear vs. opaque syrup (in centipois per second) at 77% dry solid 1st sample 7530 3722 2166 1363 864 drum 1 1744 1053 686 455 312 drum 2 3478 1973 1195 756 503 drum 3 1313 801 506 347 240 drum 4b 1856 1134 713 474 309 drum 5 3366 1898 1175 759 509 drum 6 1263 766 499 344 237 bucket 1 3225 1856 1150 857 586

8O⁰F 90⁰F 100⁰F 110⁰F 120⁰F

Sample Viscosity (in Viscosity Viscosity (in Viscosity (in Viscosity cps) (in cps) cps) cps) (in cps)

PDF12 3853 2133 1297 827 553

PDF7 15010 10690 7740 5870 4460

Table 8: The digestion rates of clear vs. opaque syrup (in % of glucose released after 0-24 hours)

Example 8, Clear syrups made at high temperatures with enzyme preparations from various Leuconostoc strains

- is - Enzyme preparations were obtained from 3 different Leuconostoc strains using methods described in Example 1. A total of 3 kg sugar substrate (sucrose:maltose=9:l) was dissolved in city water to final concentrations of 50% dry solid w/w or 52% dry solid w/w including enzyme addition. Reactions were carried out at 50 ° C or 52 ° C (Table 9 below). Aliquots were drawn at the end of each reaction and their sugar profiles and in vitro digestibility were determined as described.

As shown in Table 9, all enzyme preparations completed the reactions. The resulting syrup exhibited similar chemical composition and in vitro digestion rates.

Table 9. Reaction condition, sugar profile and in vitro digestibility of syrups made at high temperatures

Claims

What is claimed is:

I . A method of making a substantially clear syrup comprising reacting one or more substrates at a concentration of at least 40 % w/w with at least one alternan sucrase enzyme at a temperature of greater than 45⁰C to form a substantially clear syrup.

2. The method according to claim 1, wherein the at least one alternan sucrase and one or more substrates are held greater than 45°C for less than 12 hours.

3. The method according to claim 1, wherein the enzyme has a concentration of less than 8 units/gram substrate.

4. The method according to claim 1, wherein the syrup at a concentration of 20% w/w has a transmittance at 650 nm of greater than 93%.

5. The method according to claim 1, wherein the syrup comprises less that 0.5% alternan that is greater than DP 12.

6. The method according to claim 1, wherein the syrup has a viscosity of less than 14000 cps at 8O⁰F and 77% dry solid concentration.

7. The method according to claim 1 wherein the at least one alternan sucrase enzyme is obtained from lactic acid bacteria.

8. The method according to Claim 1 wherein the at least one alternan sucrase enzyme is obtained from Leuconostoc mesenteroides.

9. The method according to Claim 1 wherein the at least one alternan sucrase enzyme is obtained from a strain selected from the group consisting of Leuconostoc mesenteroides strains NRRL B 1355, 23185, 23186, 23188, 23311, 21297, 30821, 30894.

10. The method according to Claim 1 wherein the at least one alternan sucrase enzyme is produced recombinantly.

II. A syrup made according to the method of claim 1.

12. A food or beverage composition comprising the syrup of claim 11.

13. A method of making a food or beverage comprising mixing one or more ingredients with a substantially clear syrup made by reacting one or more substrates at a concentration of at least 40 % w/w with at least one alternan sucrase enzyme at a temperature of greater than 45°C.

14. The method according to Claim 13 wherein the beverage is a sports drink.

15. The method according to claim 13 wherein the at least one alternan sucrase enzyme is obtained from lactic acid bacteria.

16. The method according to Claim 13 wherein the at least one alternan sucrase enzyme is obtained from Leuconostoc mesenteroides.

17. The method according to Claim 13 wherein the glucansucrase enzyme is obtained from a strain selected from the group consisting of Leuconostoc mesenteroides strains NRRL B 1355, 23185, 23186, 23188, 23311, 21297, 30821, 30894.

18. The method according to Claim 13 wherein the at least one alternan sucrase enzyme is produced recombinantly.

19. The method according to claim 13, wherein at least one of the ingredients is a vitamin.

20. The process according to claim 13, wherein at least one of the ingredients is a high intensity sweetener.

21. A food made by the method according to claim 13.

22. A beverage made by the method according to claim 13.