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Application of microfiltration in process cheese spread and whey protein concentrate manufacture.

机译:微滤在加工干酪酱和浓缩乳清蛋白中的应用。

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摘要

Application of microfiltered (MF) milk for Process cheese spread (PCS) and whey protein concentrate (WPC) manufacture was investigated. Microfiltered milk retentate was used for PCS manufacture and permeate was utilized for WPC manufacture. Microfiltration of raw skim milk (0.2% fat) resulted in two fractions casein was concentrated in microfiltered milk retentate (MFR), and microfiltered milk permeate (MWP) which included whey proteins, was practically casein-free. The MFR was ultrafiltered (UF) to approximately 1.3X and the resulting concentrate (MFC) was used for Process cheese manufacture. To develop cheese base with 'Swiss cheese like' flavor, MFC was fermented with thermophilic lactic acid bacteria (Lb. bulgaricus and St. thermophilus) along with propionic acid bacteria (P. shermanii). 'Swiss cheese like' flavor was perceptible in the fermentate after 5 days of incubation, but the flavor was very mild to be perceived in Process cheese. Process cheese spread were therefore formulated with flavor concentrates. Milk protein concentrate (MPC) 70, because of its higher protein and lower lactose, was used to fortify solids in PCS formulations with higher MFC. Three treatments and a control (C) were formulated such that the ratio of natural Swiss cheese:MFC was 2:3 (T1), 1:3 (T2), no natural cheese (T3), and C from only natural cheese (3 replicates). With an increase in the amount of MFC, mineral content increased while protein content and spreadability decreased. Spreadability of C and T1 was significantly higher than that of T2 and T3 after 2.5 and 5 min. There was a decrease in viscosity with an increase in the amount of MFC in the formulation possibly because of overcreaming in PCS with natural cheese. Viscosity of C, T1, T2, and T3 was 0.73, 0.68, 0.67, and 0.63 Pa s, respectively. Relatively lower dependence of viscoelastic moduli on frequency of T1 and T2 than that of C and T3 suggested a poor interaction between the protein from natural cheese and MFC. Partial replacement of natural Swiss cheese with MFC improved sensory properties of PCS. Overall flavor, body and texture, appearance, and acceptability scores of T1 (7.2, 7.4, 7.8, and 7.4, respectively) were higher than those of the control (6.2, 6.3, 7.5, and 6.2, respectively). Scores of control and T2 were not significantly different. All the scores of T3 were significantly lower than those of other treatments. In a separate study, MWP was UF and then spray dried to milk whey protein concentrate (MWPC). Clarified and pasteurized Cheddar cheese whey was either directly UF or first MF and then UF before spray drying to produce conventional whey protein concentrate (CWPC) or microfiltered conventional whey protein concentrate (DWPC), respectively. None of the streams for MWPC manufacture were ever pasteurized. The UF concentration factor was 10X for MWPC (4 replicates) and 8X for CWPC and DWPC (3 replicates). The MWPC products therefore had higher protein content (48.7%) than CWPC and DWPC (34.8 and 37.2%, respectively). All three products were compared for native protein and functional properties (gelation, emulsion stability, and foam overrun and foam stability). Native protein measured as protein precipitable at pH 4.6 was lower in MWPC (82.5%) than in CWPC (92.8%) and DWPC (95.6%). Gelation, measured as least concentration endpoint (LCE), was affected by the source of whey. Gel formation in CWPC and DWPC occurred at 6.3 and 6.2% protein, respectively, which was significantly lower than that of MPWC (7.1%). Emulsion stability (ES) of product produced with MF (MWPC and DWPC) was lower (1.6 and 1.3%, respectively) than that produced without MF (CWPC), 5.4%. Microfiltration of whey source resulted in 'turbidity-free' WPC solution. Foam overrun of DWPC was greater than that of MWPC (1059.7 and 952.7%, respectively) but the foam stability of MWPC was higher than that of DWPC. Thus, WPC resulting from MF of whey source exhibits functional properties that are very different from those produced by the conventional method. Microfiltration therefore can be successfully employed for developing new dairy ingredients and expanding their use in the food industry.
机译:研究了微滤(MF)牛奶在加工干酪酱(PCS)和浓缩乳清蛋白(WPC)生产中的应用。将微滤过的牛奶截留物用于PCS制造,将渗透物用于WPC制造。对脱脂奶(0.2%脂肪)进行微滤,将两部分酪蛋白浓缩在微滤过的牛奶截留物中(MFR),而包含乳清蛋白的微滤过的牛奶透过物(MWP)几乎不含酪蛋白。将MFR超滤(UF)至约1.3倍,所得浓缩物(MFC)用于加工干酪的生产。为了开发具有“瑞士奶酪样”风味的奶酪基料,将MFC与嗜热乳酸菌(保加利亚乳杆菌和嗜热链球菌)以及丙酸菌(谢尔曼氏疟原虫)一起发酵。孵育5天后,发酵物中可以感觉到“瑞士奶酪样”的味道,但是在加工奶酪中感觉到的味道非常温和。因此,加工干酪酱是用风味浓缩物配制的。牛奶蛋白浓缩物(MPC)70由于其较高的蛋白质和较低的乳糖,被用于强化具有较高MFC的PCS配方中的固体。配制了三种处理方法和一种对照(C),以使天然瑞士奶酪:MFC的比例为2:3(T1),1:3(T2),无天然奶酪(T3),而C仅由天然奶酪(3复制)。随着MFC含量的增加,矿物质含量增加,而蛋白质含量和铺展性降低。在2.5和5分钟后,C和T1的可扩展性显着高于T2和T3。随着配方中MFC含量的增加,粘度降低,这可能是由于PCS与天然干酪的过度奶油化所致。 C,T1,T2和T3的粘度分别为0.73、0.68、0.67和0.63 Pa s。相对于C和T3,粘弹性模量对T1和T2频率的依赖性较低,这表明天然奶酪和MFC之间的相互作用较差。用MFC部分替代天然瑞士奶酪可改善PCS的感官特性。 T1的总体风味,身体和质地,外观和可接受性得分(分别为7.2、7.4、7.8和7.4)均高于对照组(分别为6.2、6.3、7.5和6.2)。对照和T2得分无显着差异。 T3的所有分数均明显低于其他治疗。在另一项研究中,MWP为超滤,然后喷雾干燥为乳清蛋白浓缩物(MWPC)。澄清和巴氏杀菌的切达干酪乳清分别是直接超滤或先用MF,然后是超滤,然后进行喷雾干燥以分别生产常规乳清蛋白浓缩物(CWPC)或微滤常规乳清蛋白浓缩物(DWPC)。用于生产MWPC的物流均未经过巴氏消毒。 UFPC的UF浓度因子是MWPC的10倍(4个重复),而CWPC和DWPC的UF浓度因子是8倍(3个重复)。因此,MWPC产品比CWPC和DWPC(分别为34.8和37.2%)具有更高的蛋白质含量(48.7%)。比较所有三种产品的天然蛋白质和功能特性(凝胶化,乳液稳定性,泡沫膨胀度和泡沫稳定性)。 MWPC(82.5%)在pH 4.6下可沉淀的天然蛋白质含量低于CWPC(92.8%)和DWPC(95.6%)。乳胶(以最低浓度终点(LCE)衡量)受乳清来源的影响。 CWPC和DWPC中的凝胶形成分别发生在6.3和6.2%的蛋白质上,这明显低于MPWC(7.1%)。用MF生产的产品(MWPC和DWPC)的乳化稳定性(ES)分别比不使用MF生产的产品(CWPC)低5.4%和1.6%。乳清源的微滤产生了“无浊度”的WPC解决方案。 DWPC的泡沫膨胀率高于MWPC(分别为1059.7和952.7%),但MWPC的泡沫稳定性高于DWPC。因此,由乳清源的MF产生的WPC表现出与通过常规方法产生的那些功能特性非常不同的功能特性。因此,微滤可以成功地用于开发新的乳制品成分并扩大其在食品工业中的用途。

著录项

  • 作者

    Somni, Himanshu.;

  • 作者单位

    South Dakota State University.;

  • 授予单位 South Dakota State University.;
  • 学科 Agriculture Food Science and Technology.
  • 学位 Ph.D.
  • 年度 2009
  • 页码 124 p.
  • 总页数 124
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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