Recipient Organization
UNIV OF MINNESOTA
(N/A)
ST PAUL,MN 55108
Performing Department
Food Science & Nutrition
Non Technical Summary
In food systems large macromolecules contribute to the overall quality and acceptability of the food. Included in this group are dairy macromolecules. These dairy-derived molecules primarily proteins and triglycerides, interact with various molecules found in food systems, e.g. carbohydrates, proteins, stabilizers, and emulsifiers. Unfortunately, how these interactions affect various physico chemical properties of the food systems is not well understood. Some of the properties of concern are rheological characteristics, emulsifying ability, and extent of protein denaturation and interactions, and carbohydrate-protein interactions. An understanding of these complex interactions is critical in that the distinctive characteristics of many foods are influenced by these interactions. Among these characteristics are the texture or mouth feel of ice cream, the emulsifying properties of various milk protein fractions, as well as their water holding behavior.A better understanding of such macromolecule effects in foods would help insure the production of desirable food products. This understanding would allow for better prediction of overall product quality, e.g. the effects different amounts of denaturation will have on altering the gelling properties of milk proteins, or the effect of various carbohydrates on the smoothness of ice cream. Additionally, basic knowledge of the interaction of macromolecules would be obtained and aid the understanding of their behavior in aqueous systems other than just foods.The overall benefit will be higher quality food products. Characteristics such as the smoothness of products like ice cream and thickness of salad dressing will be better controlled. The stability of oil and water emulsions will be enhanced by information gained from this project.
Animal Health Component
60%
Research Effort Categories
Basic
20%
Applied
60%
Developmental
20%
Goals / Objectives
Number 1Hypothesis: Addition of citrates and phosphates to concentarted milk products will produce products with modified physical properties.Objectives:Deterime the extent of casein micelle disintergration in various concentrated milk products (concentrated skim and whole milks as well as at various concentartions of protein in milk protein concentrates) with additon of various amounts and types of citrates and phosphates.Determine the gelling, emulsifying and foaming characteristics of theses modified milk products.Determine the impact drying has the characteristics of these modified milk products.Determine the impact these modified product will have in food products that contain the non modified counter part of these products.Number 2Hypothesis:Barley β Glucan will interact with casein to produce unique gelling properties in fluid milk.Objectives:Determine the chemical nature of the interaction between barley β glucan and milk. 2. Determine the impact of casein amount, β glucan amount, and homogenization pressure on the gelling time of a β glucan-milk system. 3. Determine the impact of casein amount, β glucan amount, and homogenization pressure on the gel strength of a β glucan-milk system.
Project Methods
For Hypothesis and Objectives 1:Raw whole milk will be separated into cream and skim or used as received. Following pasteurization the milks (skim and whole) will be processed in two general ways. The first will be to use reverse osmosis to concentrate the milks to various levels (in the 1 to 4 fold range). The second general means of processing will be to concentrate and fractionate the milks by means of ultra filtration. The target concentrations will in the range of initial protein concentration up to a fivefold concentration. Products will then are either used in the liquid form or spray dried.General Evaluation of the Products Proximate analysis of the products will be carried out using standard techniques currently used in the dairy industry. The protein profile (both casein and whey proteins) of the samples will be determined by Urea PAGE gel electrophoresis and other techniques. Quantification of the individual proteins will be done using HPLC.Emulsion Stability StudiesEmulsion stability will be conducted by first producing emulsions by combining various oils, e.g., butter, corn, soy and canola, in 5% v/v oil in water system and adding solutions of the various concentrated milk products to give protein concentrations of 0.1 to 1.0 %. The samples will then be homogenized using a single stage homogenizer (Manton Gaulin).The samples will be evaluated over time using two techniques as follows:The first will be a modified homogenization index protocol. Samples of the emulsion will be placed in graduated cylinders. Daily for a one-week period samples will be evaluated for the amount of lipid in the top 10% and the bottom 90% of the cylinder. The determination will be done by the Mojonnier ether extraction method. Based on these data it will be possible to calculate the rate of separation of the various samples. These data will be statistically analyzed to determine if there are any differences present among the samples and how these differences might relate to whey source.The second technique to be used will monitor turbidity difference over time. A sample of the emulsion immediately after preparation will be placed in a spectrophotometer and the rate of clearing in the sample will be monitored.Also, confocal laser light microscopy coupled with image analysis will be used to determine the particle size distribution of the droplets in the emulsion. This data will then be used to calculate the total interfacial area per unit mass of emulsion as well as volume to surface ratio.Foaming PropertiesProtein stabilized foam will be made by sparging air through a protein solution. For this purpose, a jacketed graduated glass column, open at the top and blocked at the bottom by a sintered glass disk will be used. With this device foam volume and rate of foam decay will be determined for various protein concentrations.Gelation and Rheological StudiesProtein solutions (8-10% by weight) will be heated, at temperatures of 85-100C, in glass tubes (of fixed diameter and wall thickness) plugged on either side by silicone rubber stoppers. After cooling gels will be cut to the required height and gel properties will be studied using an Instron. This instrument measures force versus displacement (under either extension or compression).Gel and rheological properties will also be studied using a Controlled Stress Dynamic Rheometer. The sample will be subjected to rotational strain between parallel plates or between a cone and plate. This instrument measures viscosity versus rate of shear, creep, stress relaxation, and oscillation, bulk modulus and storage modulus, etc.The above experiments with the Dynamic Rheometer will be repeated, but with the addition of chymosin to the sample. This approach was previously used by Kameswaran (1994).For Hypothesis and Objectives 2:Experimental DesignUnderstanding the interaction of barley β-glucan (BBG) with other food components and gaining knowledge about how processing affects functionality can lead to greater use of BBG in food systems. A central composite rotatable design (Neter et al 1996) has been chosen as a tool for gaining such knowledge and understanding. Three factors have been chosen which leads to a total of 20 treatments (α = 1.682) for the design. The three variables include BBG concentration (1% - 2%), NDM concentration (1% - 9%) and homogenization temperature (5ºC - 40ºC). The dependant variable is gel time (Tg).Analysis of data will be performed using SAS® software and the PROC RSREG procedure (SAS® Institute, Cary, NC).Sample PreparationGlucagel™ (81% β-glucan, 52,000 kD) is the barley β-glucan source for this experiment and was obtained from PolyCell Technologies, Crookston, MN. (Later experiments will utilize different β-glucan sources.) Low heat nonfat dry milk (NDM) was obtained from Dairy America, Fresno, CA. Glucagel™ and NDM are weighed out according to the factor levels for each treatment and dry blended together. This blend is then added slowly to deionized water with stirring until dispersed. Small agglomerates would form occasionally but are kept to a minimum by controlling the addition of the dry blend to the water (from preliminary trial). Stirring is held to a minimum to avoid excessive formation of foam. The mixture is heated on a double boiler with stirring to 70ºC and transferred to an ice water bath after 15 seconds for cooling. The mixture is cooled in an ice water bath to the shear temperature prescribed for the treatment and transferred to a homogenizer (Microfluidics™ HC-8000/3A, Newton, MA). The homogenizer serves as the shear apparatus and the mixture is sheared at 620,000 s-1 (2000 psi through a Microfuidics™ E230Z chamber). A sample is collected from the homogenizer and returned to the ice water bath for further cooling to 5ºC.Gel MeasurementOnce sheared and cooled, the sample is transferred immediately to an AR 1000 rheometer (TA Instruments, New Castle, DE) with 60mm acrylic flat plate geometry. The geometry is equipped with a solvent trap that was filled with water. Approx. 1.5 ml of sample is loaded onto the plate and the geometry is lowered to within 750 µm (gap) of the plate. The plate temperature is set at 5ºC. The solvent trap cover is placed over the geometry for the duration of the test to slow the rate of evaporation or condensation. Each sample is pre-sheared prior to the start of the time sweep. The time sweep is conducted at a frequency of 0.1000 Hz and controlled oscillatory stress of 0.05 Pa. The stress and frequency setting's for the time sweep were established from stress sweeps conducted previously and is in the linear viscoelastic region (LVR) of the treatments in the design. G' and G'' are measured during the time sweep and the time recorded from the start of the sweep to when TAN δ = 1.0. Once Tg is established, gel formation will be allowed to continue until TAN δ = 0.07. This is the gel strength provided by Steffe (1996) as being typical of a gel in a dilute system. A stress sweep will be conducted after time sweep data has been collected to confirm the LVR for that treatment.