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Manufacturing - Milk Powder - 2001 Production of milk powder continues to increase in the United States. To remain competitive in the global market, to maximize existing markets and to identify new markets and ingredient applications, powder quality must be outstanding and consistent. Flavor quality is an important parameter for milk powders because flavor influences consumer acceptability and can influence finished product quality when powders are used in ingredient applications. The development of a precise quantitative sensory language to describe and quantify all the flavors in milk powders will aid in research and marketing communication. The language can be used in marketing to more accurately supply the preferences of consumers and to monitor product consistency. In research applications, the language can be a powerful tool to determine the effects of processing and storage regimes on sensory perception of flavor. The language also can be used with chemical flavor analysis to identify the chemical compounds responsible for specific flavors. Linking powder end-product quality with the technology of powder production and storage will enable powder producers in California and throughout the United States to maximize powder sensory quality, and will provide a descriptive sensory language to identify and quantify flavors in milk powders. Particularly relevant to this work was the production and distribution of a buttermilk fraction enriched in milk fat globule membrane material (5-10 g)—in particular sphingomyelin—and sent to be tested by Bruce German at UC Davis. Results from this analysis precipitated the production of larger scale quantities (4kg) of this fraction to be sent to the Nestle Research Center in Switzerland. In addition, practical results from this work include the increase in commercial as well as research activities regarding buttermilk. The National Dairy Council and the California Agricultural Research Initiative have funded additional projects with expanded objectives to this initial work. Results from this work have opened the opportunity for researchers to obtain buttermilk fractions with potential biological activities. We are positioned at this point as suppliers for these ventures. Due to the opportunities generated from this work, much time was devoted to the construction, validation and optimization of a larger microfiltration system. Operation parameters, pumps and modes of operation had to be optimized to obtain desired results in a time frame appropriate for preventing microbial contamination. The system is now operational. Researchers at Cal Poly and UC Davis continue to work diligently to optimize the scientific endeavors and maximize the return on investment on research. Renewing valuable collaborations between these two institutions is a valuable asset for California. Focusing on the interaction among k-casein A (it was selected from homozigous milk k-casein AA) and b-Lactoglobulin, Lawrie Creamer and Mike Boland helped in the development of this project. To better understand the effects of processing on the functionality of milk powder, we characterized at the molecular level the protein-protein interactions after heating and drying. The powder sample was produced in the pilot plant of the Cal Poly DPTC in San Luis Obispo, Calif. A simplified milk system was created by mixing affinity-purified b-LG (b-LG genetic variant AB) to casein micelles obtained by filtration of raw milk (k-CN variant AA; b-LG variant BB) through a 0.1mm pore size ceramic membrane. The mixture was heated to 90oC for 15 minutes and spray dried. The high molecular weight molecules were segregated by size exclusion chromatography, identified by SDS-PAGE, and hydrolyzed by trypsin. The native and disulfide-bond-reduced hydrolysates were analyzed by HPLC-MS at the NZDRI Palmerston North facility in New Zealand. Our SDS-PAGE analysis shows that we isolated a disulfide-linked protein polymer that contained predominantly k-CN and b-LG. By comparing our mass spectroscopy results to tryptic digest data banks; we identified 42 peptide fragments, including 11 disulfide-linked peptides. We identified three different types of disulfide links: (1) the expected intermolecular bridges between two k-CN molecules connected k-CN Cys11 to k-CN Cys11 and k-CN Cys88 to k-CN Cys11, (2) the heat-induced association of two b-LG linked b-LG AA Cys66 to b-LG BB Cys106/119/121 and b-LG Cys160 to b-LG BB Cys106/119/121, and (3) the heat-induced covalent bonding between b-LG and k-CN involving k-CN Cys88 to b-LG Cys66, k-CN Cys11 to b-LG Cys160, and k-CN Cys11 to b-LG BB Cys106/119/121. These peptides aid in the elucidation of protein interactions in dried milk. This work results in a better understanding of the basis for several New Zealand patents granted in the United States, and in gaining a better strategy to obtain the same or better results using technology and genetic variants common in this country. The following handouts were developed and distributed as Technical Information Handouts for Skim Milk Powder: Technical information handouts provide timely and regular communication of useful information to manufacturers and users of skim milk powder. Such information helps to facilitate the successful use of dairy ingredients in many food applications. Based on the queries being received and answered, it appears that a real need is being met by the establishment of this program—both for the ingredient manufacturers and the end users. In some cases, we believe our assistance encouraged successful utilization of domestic sources of dairy ingredients by food manufacturers. In addition, technical support provided to dairy ingredient manufacturers continues to promote product/technology innovation to improve dairy ingredient product lines. The findings of this study have implications for formulations to be used in a dairy-juice beverage. The improved stability of certain beverages in the presence of hydrocolloids does not appear to be a result of viscosity changes alone but by an interaction between the hydrocolloid and the casein. Homogenization of the beverage prior to heating and/or the addition of a phosphate system may produce an improvement in the overall stability of these beverages at varying pH and processing temperatures and may be an area for future study. A total of 16 acid dairy-based gel formulas were evaluated. The starch and hydrocolloids were evaluated at two different usage levels and two pH levels. The viscosity of the dairy gel prior to freezing is not changed significantly with the addition of the hydrocolloid. The starch at the increased level showed the highest viscosity. The addition of the hydrocolloid did not appear to affect the pH. All the hydrocolloids tested functioned to improve mouth feel and texture during the freeze/thaw cycle period. Carrageenan did not appear to work as well as the starch and xanthan and guar gum. The texture and the mouth feel of the formulas produced with carrageenan were more rigid and much different than the fresh sample. Also, the xanthan gum at the higher usage level did not function as well compared to the evaluation of this gum at the lower usage level. This may be a result of an excessive percentage of gum in the system. This can cause syneresis, because it destabilizes the system. All samples showed some slight syneresis during some point in the freeze/thaw cycle. However, all hydrocolloids tested helped to reduce syneresis and minimize cracking to some extent. The samples without hydrocolloids experienced the most syneresis, as well as the sample of xanthan gum with the high usage level. An acid dairy gel formulated with xanthan gum (0.20 percent), pH 4.0 showed no cracking. The cracked product was formulated with carrageenan at .20 percent, pH 4.0. When the usage level of carrageenan was increased, the product did not crack. The high-usage xanthan gum formula was the only other formula to show cracking. The addition of the hydrocolloid appears to help bind water and decrease syneresis, as well as minimize cracking of the frozen/thawed acid dairy gel. The texture and mouth feel of the dairy-based gel, although very subjective, formulated with xanthan gum at a 0.20 usage level, produced a product with the best texture and mouth feel, as well as no cracking and syneresis. The results of this work provide quantitative information to answer questions related to the effect of reconstitution conditions for skim milk powder. Such information can be utilized by end-users of skim milk powder to guide them in making decisions about the tradeoffs between various options for reconstitution of skim milk powder and their specific effect on dispersibility and eventual solubility. To achieve good reconstitution conditions for dry milk powders in water, we recommend minimum water temperatures of 25–500C with high shear agitation or use of a powder horn mixing system. Minimum time for the incorporation of powder should not be less than 15 minutes. However, care should be taken to minimize inclusion of air into the reconstituted milk during reconstitution. Our results show that using PCR and amplifying a specific gene for endospores allow us to detect those endospore-former bacteria associated with milk powder production. This detection is possible by isolating the whole microbial community DNA and then analyzing the product of a specific gene with the primers designed for this work. The primer set is specific for the germination gene GerC3 in B. subtilis, and has been shown to correlate with several other Bacillus species. However, the results obtained have shown that the primers specific for the germination gene in Bacillus species were problematic in their inconsistency. Using those GerC3 primers to amplify the germination gene from B. licheniformis, the most common Bacillus species in milk, we sequenced this product and developed new primers to solve this problem. In a parallel study, this work also yielded a tool that can be used to study and analyze microbial populations at each step during milk powder production. For this objective, a more common gene is targeted. The 16SRNA gene, normally used for typing bacteria species, can be used for developing Terminal Restriction Fragments (TRFs) for the detection of different species of bacteria. Several studies were completed on the optimization of the technique and testing it for its use in dairy products. The ultimate validation has been made in commercial operations, in which samples were taken at each step of the milk powder process. The objectives were expanded due to matching funds from the California Agricultural Research Initiative (ARI). Deeper understanding was necessary to explain the relationship between the bacterial populations and the incidence of spore-formers that eventually contaminate the final product with spores. The ARI has supplemented funds to expand our experiments toward better understanding this phenomenon. This is a tangible result from the funding and activities in the microbial improvement of milk powder. Finally, due to the work developed at Cal Poly’s Dairy Products Technology Center, scientists at the Lawrence Livermore National Laboratory can use the spore collection generated by this work, thus helping in their efforts to prevent bio-terrorism. Plastic bags have been introduced recently as an alternative to multiwall Kraft paper bags in milk powder packaging, as it is believed that plastic bags are more durable and would better preserve the quality of milk powders during storage than paper bags. However, little scientific information is available on the performance of plastic bags for milk powder storage. The aim of this study was to compare the durability of paper and plastic bags in milk powder packaging, and to determine the effects of package type on the properties of milk powder during storage. Skim milk powder (SMP) packed in plastic or paper bags was obtained from commercial milk powder manufacturers. Both 25 kg plastic and paper bags containing SMP were evaluated by butt drop, side drop and shaker test to determine which bag type is more durable. Sets of bags of plastic and paper containing bags containing SMP were stored at 380C and 90 percent relative humidity. Duplicate bags of each type were removed after 0, 45, 90 and 135 days, and the powder samples were analyzed for moisture, water activity, percent lactic acid, pH, insolubility index, bulk density, flowability, dispersibility and particle size. Minimum damage was inflicted to the outer layer of plastic bags. The printed graphics and text were damaged more extensively in plastic bags; however, overall durability performance of plastic bags was better than paper bags. The magnitude of change in the majority of physical and chemical properties measured in powder samples during storage indicate that plastic bags are similar to paper bags in maintaining quality of SMP at high temperature and relative humidity. Skim milk, retentates, permeates and the treated permeates were analyzed for total solids, total ash, calcium and lactose content. Permeates and treated permeates were also analyzed for total nitrogen and permeate for the presence of protein. About 75 percent of the total lactose present in skim milk permeated through the membrane during ultrafiltration. About 50 percent of the expected free calcium in the skim milk also permeated through the membrane. The three treatments applied produced white precipitates and turned the clear permeates into turbid permeates. On refiltering the treated permeates, ~ 42 percent, ~ 50 percent and ~ 70 percent of the total calcium present could be recovered from (1) heat-treated, (2) pH-adjusted and (3) pH-adjusted and heat-treated permeates, respectively. Similar results were obtained for both lab scale and pilot scale experiments. Thus, the maximum calcium recovery was obtained by pH adjustment and heat treatment to the permeate followed by refiltration. No marked change occurred in the lactose content due to any of the three calcium precipitation treatments and subsequent refiltering of the treated permeates. About 75 percent of the total lactose present in skim milk permeated through the membrane during ultrafiltration. The calcium that permeates through the membrane in this process can be heat precipitated, refiltered and added back to the retentate to recover approximately 70 percent of the original calcium. This work demonstrates the technical feasibility for producing a new reduced-lactose protein stream with high natural milk calcium content for the food industry. A two-step membrane process results in significant lactose reduction but still maintains the naturally high calcium content of the original feed stream. Eight prototypes—food products that reflect current marketing trends using dairy ingredients—were formulated and produced. Formulation and technical sheets to accompany each prototype were completed. The prototype samples and fact sheets have been used for trade shows, presentations and demonstrations and will be used at upcoming events. Completed formulas include calcium-enriched hot cocoa, high-protein energy bars, smoothie mix, calcium-enriched scone mix, cream cheese filling, cappuccino mix, high-protein cookies and mocha dairy candy. The prototypes were developed to reinforce the concept to food product developers that dairy ingredients are versatile and functional in new product formulations. The prototypes have been shown at both national and local trade shows, as well as events at Cal Poly San Luis Obispo’s Dairy Products Technology Center. The food products that were demonstrated helped to show that Cal Poly’s Dairy Ingredients Applications Program can provide needed technical support to food product developers. A model system was developed to determine the difference between nonfat dry milk (NFDM, 36 percent protein), whey protein concentrate (WPC, 34 percent protein) or milk protein concentrate (MPC, 42 percent protein) as an ingredient (3 percent) in a baked system. The model system used for this evaluation was a plain type muffin formula, which is bland in flavor, light in color and has good volume and grain. All three dairy ingredients evaluated scored fair or above in the subjective evaluation. The NFDM and WPC muffins yielded a mild dairy flavor, contributing no off-flavors. The MPC muffin had a slightly stronger flavor and was not as well balanced. All three products formed an acceptable golden brown color. The NFDM product was slightly darker in brown color than the other formulations. The MPC product had the best texture—it was moist, had a smooth grain and had the most overall height compared to NFDM and WPC muffins. The texture and volume of the NFDM and WPC products were similar. All three dairy ingredients contributed to the flavor, texture, color and volume of the muffin. The perceived flavor difference in the NFDM and WPC formulas may result from the higher lactose content (52 percent lactose in both) compared to the MPC (16.5 percent lactose). The texture of the MPC muffin was rated slightly higher, probably as a result of the higher protein content. Milk proteins generally show good water-binding properties, which contribute to good moisture retention in the finished product. Phase 1 Phase 2 The two phases of this process have been successfully completed. The first one demonstrated that delipidation of whey was possible and efficient by using biosilicate filtration. Furthermore, the lipids recovered are mostly phospholipids. These substances are being actively sought in several laboratories today. An untapped resource has been identified, and a new area for innovation and value-added products for the dairy industry has been opened. The second phase was the focus on the isolation of native b-LG with a single step adsorption process. The work concentrated on scaling up the procedure of purification of native b-LG using several types of industrial approaches at the pilot plant. The process of affinity separation of b-LG in its native form using all-trans-retinal immobilized on Celite R-648TM was scaled up and applied to fractionate industrial sweet whey. Three different methods for mixing the Celite R-648TM and whey for the interaction between all-trans-retinal and b-LG were tried at pilot scale. The three methods used included: Adsorption and desorption of b-LG were carried out at pH 5.1 and 7.0, using 0.01 and 0.1M phosphate buffers, respectively. The phosphate buffer containing desorbed b-LG was concentrated 20 times using ultrafiltration and then freeze-dried. The packed column, stirred tank and fluidized bed column produced b-LG with purity of 80, >95 and >95 percent, respectively, and recovery of 0.65, 2.88 and 2.88g per kg of Celite R-648TM, respectively. The comparatively poor purity and recovery of b-LG in the case of the packed column was attributed to insufficient contact between the passing fluids and the Celite R-648TM during adsorption, desorption and intermittent washing. The fluidized bed column method, being a continuous operation with a gentle mixing action, was considered the best suited for further scale-up to the industrial level. Grease-barrier properties of whey protein-coated paperboard Sucrose-plasticized whey protein coatings on paperboard impart excellent grease resistance, similar to glycerol-plasticized coatings. A concern of possible plasticizer migration into the paperboard over time, with resulting cracking and flaking of the coating, was investigated by determining the effect of long-term storage at ambient temperature. Sucrose-plasticized whey protein coatings on paperboard retain excellent grease resistance after storage, in contrast to glycerol-plasticized coatings that lose their grease resistance. WPI plasticized with sucrose has good grease barrier property in accelerated (high temperature) testing. WPC-80 plasticized with lower levels of sucrose has better grease barrier property than WPI coating in accelerated testing. This may be due to the different protein concentrations in WPI and WPC, as well as the plasticizing effect of the indigenous lactose in WPC 80. WPC-80 with hydrolyzed lactose plasticized with sucrose has good grease-barrier property in accelerated testing. However, the grease barrier property was impaired with increased storage time at room temperature. This may be due to the hydrolysis of lactose in WPC-80 into smaller molecules (glucose and galactose). The migration of these small molecules likely occurred during ambient storage. Finally, WPC-80 with 10 percent degree of hydrolysis plasticized with sucrose does not have good grease-barrier property. Among all of the whey protein products, WPC-80 seems to give the best grease barrier property when coated on paperboard. The cost of whey protein material will be substantially reduced with utilization of WPC instead of WPI. Our studies have shown that whey protein coated on paperboard imparts excellent grease resistance. Gloss studies have shown that whey protein increases gloss of uncoated paperboard, and color studies have shown that low color and good transparency are maintained. Examples of commercial applications include donut boxes and pizza boxes, which require a significant level of grease barrier on their packaging to retard grease penetration and unsightly stains. Examples of applications that will benefit from a good oxygen barrier in addition to grease barrier are pet-food and coffee bean containers. The research on whey protein coating on paperboard is very timely because of the recent withdrawal of 3M’s fluorocarbon coating—industry’s most widely used grease barrier. Presently, manufacturers are eagerly seeking alternative coatings. Commercial implementation of whey protein for coating paper and paperboard can result in large-volume utilization of whey. Oxygen-barrier properties of whey protein-coated plastic The type of plasticizer used (0.6 M sorbitol, sucrose, propylene glycol or PEG) significantly influenced OP of the WPI-coated plastic films. WPI-coated films containing sucrose plasticizer had the best barrier to oxygen. OP of the WPI-coated LDPE film plasticized with sucrose was only 0.5 percent that of the uncoated LDPE film at the same conditions. This means that the oxygen barrier of the WPI-coated LDPE film was 200 times better than the uncoated LDPE film. Oxygen barrier property of the WPI-coated creased in order of sucrose, sorbitol, glycerol, propylene glycol and PEG 200. The gloss of the WPI-coated plastic films was affected by the type (sorbitol, sucrose, propylene glycol, PEG) and concentration (glycerol: 20%, 35%, 50%, 70%) of plasticizer used. The gloss units of the coated films with sucrose were even greater than normal base plastic films without coating. Coating haze was calculated as the difference in the gloss values measured at an angle of 60 degrees and 20 degrees from the normal to the coating surface, respectively. The haze index indicates a measure of the irregularity and heterogeneity of the surface. The results indicate that the WPI coating itself would not give any additional irregularity and heterogeneity to the surface of base films. A Hunter LabScan colorimeter was used to assess the color of the WPI-coated films. Regardless of the base plastic, the WPI coatings with various plasticizers of different concentrations did not affect significantly the color of the resulting WPI coated films. Any color differences between WPI-coated and uncoated films could not be observed with the human naked eye. Almost identical oxygen-barrier, gloss, haze and color results were obtained when substituting WPI with 80 percent WPC in the coating formulations. Thus, the less-expensive 80 percent WPC can likely be used for this application. Properties of whey protein-coated plastic It is possible to form coatings based on either WPI or WPC on common synthetic polymer films made from LDPE and PP. The LDPE and PP films must be treated with corona discharge to modify their surfaces in order to achieve well-adhering whey protein coatings. The resulting whey protein-coated films have excellent oxygen-barrier properties—much better than the uncoated LDPE or PP films, at low to intermediate RH. The whey-protein-coated films also have excellent gloss and low color. Results were almost identical for WPI- and WPC-based coatings, indicating that the lower-cost WPC could be used for this purpose. Thus, whey protein coatings have excellent potential for replacing existing synthetic oxygen-barrier coatings on LDPE and PP films. Recent demonstration in a related project that whey protein films can be extruded suggests that extrusion coating of whey protein onto LDPE and PP should be possible. A system was developed whereby pilot-scale batches of cream (10-20 gal) could be tempered under controlled experimental conditions to establish variable solid-to-liquid fat ratios in cream prior to churning. Experimental batches of cream were churned using the Simon Freres Contimab 2 Continuous Butter Churn or an Egli Continous Butter Churn. Baseline process conditions of cream volumetric flow rate of 3 GPM, 1,500 RPM beater speed and 40 RPM working section resulted in butter containing approximately 16.5 percent moisture. Procedures for quantification of the solid-to-liquid fat ratio in milkfat were developed using differential thermal analysis (DSC-2920,TA Instruments). The method involves heating the test sample to 550C and keeping it isothermal for 10 minutes, followed by cooling to 400C at a rate of 100C per minute and then generating a thermogram of the sample from 400C to 550C at the rate of 50C per minute. Confocal microscopy is being developed to examine the crystalline habit of the milkfat products. Aging times at 50C for 0, 3 or 6 hours, and heating rate from 5-100C in 10 or 100 minutes were studied. Faster heating rates and shorter aging time resulted in butters with higher fat loss to buttermilk. Butters made from milkfat with different chemical compositions had different thermal, textural and rheological properties. When cows were fed a diet supplemented with a fat source of canola oil, long-chain oleic acid content of milkfat increased significantly and a more spreadable butter resulted. Regardless of their milkfat compositions, the rheological properties of butters showed strong temperature and frequency dependence. Quick cooling caused the formation of a high quantity of small crystals, resulting in a harder butter. This temper treatment also resulted in the hardest butters, made significantly harder with the addition of the high melting triacylglycerol, tripalmitin. In extreme opposite, the T6,21,12/t2,2,15 tempering scheme, commonly known as ALNARP, was originally designed to produce a soft butter from winter seasonal cream. This is because the “cold-warm-cold” temperature pattern that promotes the slow growth of large fat crystals results in a softer butter. Addition of tripalmitin to the T6,21,12/t2,2,15 butter did not result in a significant increase in hardness. Differences in microstructure using confocal laser microscopy were seen for the different tempering conditions, but further quantification of the images is needed to clearly express this information. A process system and analytical methodology have been established, whereby controlled experiments can be conducted to characterize how key process factors can influence milkfat products. This will allow us to better understand the factors influencing butter quality. Based on these studies, we discovered that processing variables for both cream and butter processing can influence the rheological properties of butter and its ultimate hardness/spreadability. The project further demonstrated that confocal laser microscopy may be a useful tool in characterizing any structural changes due to processing conditions. MPC is a relatively new dairy ingredient produced by membrane filtration of skim milk. It is available in a liquid form or as dry powder. MPC contains high levels of protein and calcium, and low lactose content. The casein-to-whey-protein ratio of MPC used in this study was similar to the standard 80:20 ratio found in milk. Both dried and liquid MPC were used to standardize whole milk or cream, respectively, for the manufacture of reduced-fat Cheddar cheese. Cheese yields were more than 150 percent higher when whole milk was standardized with MPC for reduced-fat cheesemaking. The yield increase was due to higher levels of total solids in the milk containing MPC (17 percent vs. 10 percent) and higher recoveries of total solids. Also, by adjusting the casein-to-fat ratio with MPC, cheesemakers can avoid operating a separator to remove a portion of the milkfat as cream. MPC also has an advantage over skim milk powder because it contains less lactose (18 percent) compared to ~50 percent for SMP, thereby eliminating the chances of undesirable fermentations during cheese manufacture and ripening. Furthermore, increasing vat capacity by using high-solids milk has additional economic benefits to the manufacturer because of savings in labor costs as more cheese can be produced per-unit time. Ripening of cheese made from MPC-fortified milk, as measured by proteolysis, is generally slower than in cheese made from whole milk standardized with skim milk. The flavor attributes of cheese containing MPC were similar to those without MPC. Also, MPC cheeses had little or no bitter flavors, whereas bitter flavor notes were detected in the cheeses made without MPC. MPC is a high-protein, low-lactose and high-calcium dairy ingredient. The casein-to-whey-protein ratio in MPC of 80:20 is similar to that in milk. The study demonstrates the potential for using MPC to standardize cheese milk to give high yields and good quality. |
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© 2009 CDRF - Research photos courtesy of USDA Agriculture Research Service.