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Optimization of α-Amylase Application in the Sugarcane Industry

机译:α-淀粉酶在甘蔗工业中的应用优化

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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 α- amylases used by the U.S. sugar industry to control starch have intermediate temperature stability (up to 85 ℃ with an optimum ~70 ℃), and are produced from Bacillus subtilis. There is neither a uniform/standard method to measure the α-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℃, where α-amylases are mostly applied. A wide 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/$. Α-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 α-amylase with low activity (59 KNU/ml) for an average starch hydrolysis of 6.6% as determined with 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 α-amylase (59 KNU/ml) at 10 ppm (undiluted) gave an average hydrolysis of 25.4% that only increased to 28.5% at 20 ppm. Application of a B. subtilis α-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 α-amylase and starch. Application of the α-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℃) α-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,一些美国炼油厂警告说,如果不改善淀粉控制,原糖中的高淀粉浓度可能会受到惩罚。美国制糖业用于控制淀粉的大多数商品化α-淀粉酶具有中等的温度稳定性(最高达85℃,最适宜的约70℃),并且是由枯草芽孢杆菌生产的。在制糖业中,既没有统一的/标准的方法来测量α-淀粉酶的活性,也没有监管机构发布或调节任何商业酶的标准活性的方法和单位。一种包含Phadebus的方法?修改了蓝色淀粉片以模拟典型的最后蒸发器(pH 6.4和65.5℃)中的条件,这些条件主要使用α-淀粉酶。 α-淀粉酶存在广泛的活性(59.0至545.3 KNU / ml),不能反映其相对单位成本,即每美元的活性仅从40.7至161.8 KNU / ml / $有4倍的差异。在整个路易斯安那州的2005年加工季节中,在三个工厂的最后一个蒸发器中进行了A-淀粉酶优化试验。工厂1通常使用3.6 ppm /甘蔗重量。用碘量法测定的(未稀释的)枯草芽孢杆菌α-淀粉酶的活性低(59 KNU / ml),平均淀粉水解率为6.6%,在7.2 ppm剂量下仅增加到11.4%。在工厂3发生了类似的令人失望的结果。在工厂2,相同的α-淀粉酶(59 KNU / ml)在10 ppm(未稀释)下的平均水解度为25.4%,在20 ppm时仅增加到28.5%。在2 ppm时使用活性较高的枯草芽孢杆菌α-淀粉酶(545.3 KNU / ml)产生的平均水解度为26.7%,但在5 ppm时仅增加至29.6%,这是因为α-淀粉酶与淀粉之间的接触少。在工厂中,将α-淀粉酶用作在水中稀释3倍的工作溶液,可将2 ppm和5 ppm的接触和淀粉水解率分别从31.9%和42.0%改善,并且比未稀释时添加更具成本效益。关注使用地衣芽孢杆菌和嗜热脂肪芽孢杆菌经过工程改造的高温稳定性(最高115℃)α-淀粉酶的开发,该市场比制糖业的市场更大,并且可能会残留到原糖和精制糖,糖蜜和食品中,进行了讨论。

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