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Optimization of alpha-Amylase Application in the Sugarcane Industry

机译:甘蔗工业中α-淀粉酶应用的优化

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In recent years there have been warnings by some U.S. refineries that there may be a penalty for high starch concentrations in raw sugar if starch control is not improved. Most commercial ot-amylases used by the U.S. sugar industry to control starch have intermediate temperature stability (up to 85° C with an optimum -70° C), and are produced from Bacillus subtilis. There is neither a uniform/standard method to measure the a-amylase activity in the sugar industry nor a regulatory body to issue or regulate standard activity methods and units for any commercial enzyme. A method incorporating Phadebus blue starch tablets was modified to simulate conditions in typical last evaporators, i.e., pH 6.4 and 65.5° C, where a-amylases are mostly applied. Awide range of activity existed for a-amylases (59.0 to 545.3 KNU/ml) that did not reflect their comparative unit costs, i.e., activity per U.S. dollar only differed 4-fold from 40.7 to 161.8 KNU/ml/dollar. alpha-Amylase optimization trials in the last evaporator at three factories were conducted across the 2005 Louisiana processing season. Factory 1 typically applied 3.6 ppm/cane wt. of (undiluted) B. subtilis a-amylase with low activity (59 KNU/ml) for an average starch hydrolysis of 6.6% as determinedwith an iodometric method, that only increased to 11.4% at a 7.2 ppm dosage. Similar disappointing results occurred at Factory 3. At Factory 2, the same a-amylase (59 KNU/ml) at 10 ppm (undiluted) gave an average hydrolysis of 25.4% that only increasedto 28.5% at 20 ppm. Application of a B. subtilis a-amylase of higher activity (545.3 KNU/ml) at 2 ppm gave an average hydrolysis of 26.7%, but only increased to 29.6% at 5 ppm because of low contact between the a-amylase and starch. Application of the a-amylase as a working solution diluted 3-fold in water at the factory improved contact and starch hydrolysis from 31.9 to 42.0% at 2 and 5 ppm, respectively, and is more cost-effective than adding it undiluted. Concern about the use of engineered high temperature stability (up to 115° C) alpha-amylases from Bacillus licheniformis and stearothermophilus, developed for larger markets than the sugar industry, and possible carry-over activity into raw and refined sugars, molasses, and food products, are discussed.
机译:近年来,如果淀粉控制没有改善,有些美国的炼油厂可能会对生糖中的高淀粉浓度有罚款。美国糖工业用于控制淀粉的大多数商业OT-淀粉酶具有中间温度稳定性(最高85℃,最佳-70°C),并由枯草芽孢杆菌生产。既没有均匀/标准的方法都没有统一/标准方法测量糖工业中的A-淀粉酶活性,也没有调节身体,以发出或调节任何商业酶的标准活性方法和单位。修饰了包含斑bus蓝淀粉片剂的方法以模拟典型的最后蒸发器中的条件,即pH6.4和65.5℃,其中主要施用淀粉酶。醒来的A-淀粉酶(59.0至545.3kNU / mL)存在的活动范围,其未反映其比较单位成本,即每美元的活性,只有40.7至161.8 KNU / ml /美元的不同。在2005年的路易斯安那州加工季节进行了三家工厂上次蒸发器中的α-淀粉酶优化试验。工厂1通常施加3.6 ppm / cane wt。 (未稀释的)B.枯草芽孢杆菌A-淀粉酶,其具有低活性(59kNU / mL),其平均淀粉水解为6.6%,如碘法测定,其仅在7.2ppm剂量下增加到11.4%。出厂时发生了类似的令人失望的结果3.在出厂2,在10ppm(未稀释)的相同A-淀粉酶(59knu / ml),平均水解为25.4%,仅在20 ppm下仅增加28.5%。在2 ppm的亚枯草芽孢杆菌A-淀粉酶的施用在2ppm的平均水解中为26.7%,但由于A-淀粉酶和淀粉之间的低接触,仅在5ppm下仅增加至29.6%。 A-淀粉酶作为在水中3倍稀释3倍的工作溶液的施用,分别在2和5ppm的31.9至42.0%的31.9至42.0%中稀释3倍,比加入未稀释的更具成本效益。担心使用芽孢杆菌的工程化高温稳定性(高达115°C)α-淀粉酶的使用,从甲硝杆菌和硬脂菌,为较大的市场开发而不是糖工业,以及可能的携带活性成原料和精制糖,糖蜜和食物产品讨论。

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