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OPTIMIZATION OF SUGARCANE FACTORY APPLICATION OF COMMERCIAL DEXTRANASES IN THE U.S.

机译:优化美国商业葡聚糖酶的甘蔗厂应用

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The application of commercial dextranases to break down dextran in U.S. sugar manufacture is still not optimized, partly because of misinformation about where to add the enzyme and which enzyme to use. Furthermore, there is no uniform method to measure the activity of commercial dextranases by producers/vendors/distributors, which has meant that direct comparison of activities is not possible. In this study, a simple titration method to determine the relative activity of dextranases was identified and modified for easy factory use. All activities were confirmed with an accurate IC-IPAD method using a NaOH/NaO Ac gradient. Most commercial dextranase enzymes in the U. S. are from a fungal source: Chaetomium gracile or erraticum, and are available in "non-concentrated" or "concentrated" forms. An approximate 8-10 fold difference in activity exists between the two concentration forms, and activity variations exist within each form. In 2002/03 only "non-concentrated" dextranases were applied in Louisiana to either last evaporator bodies (usually < 10 ppm/syrup) or juice. "Non-concentrated" and "concentrated" dextranases studied at juice pH 5.4-5.8, showed similar maximum activity at 48.9°C or 120°F, as monitored by IC. Dextranase activities, in lastevaporator syrup temperature (~63°C or 145°F) and Brix (-65°) conditions, were dramatically reduced (activity began to decrease after 25-30°Brix). Overall, juice applications were more efficient and economical than adding them to evaporator syrups. Application of "non-concentrated" dextranase to evaporator syrup was uneconomical. However, "concentrated" dextranase can be applied to syrup at levels as low as 10 ppm/solids (equiv. to 45 ppm/juice) to remove up to -37% dextran which is useful to consider when severe dextran problems occur. Heating juice to 48.9°C in the presence of all dextranases, dramatically removed more dextran (3380 ppm/°Brix) from a juice than at the current ambient temperature of application (32.2°C or 90°F) and was much more economical. For a "non-concentrated" dextranase, after 10 min at 10 ppm/juice and 48.9°C, -46.3% dextran was removed compared to 13.6% at 32.2°C. For the "concentrated" dextranase, after only 10 min at only 4 ppm/juice, 66.6% dextran was removed at48.9°C and was considered an overdose, compared to 29.6% at 32.2°C. Dextranase was shown to work in the presence of dithiocarbamate biocide in juice, and factory studies are being undertaken to check that no adverse dextran formation is occurring at 48.9°C. Under factory storage conditions, over a grinding season (90 days), the activity of "concentrated" dextranase decreased only slightly (~9%), whereas "non-concentrated" dextranase activity had approximately halved (-46%), and even reduced in activity when stored under refrigeration.
机译:商业葡聚糖酶在美国糖制造中分解葡聚糖的应用仍未优化,部分是因为关于添加酶以及使用哪种酶使用的地方的错误信息。此外,没有统一的方法来通过生产者/供应商/分销商测量商业葡聚糖酶的活性,这意味着无法比较活动的比较。在该研究中,确定了一种简单的滴定方法,以确定葡聚糖酶的相对活性并改性,以便于工厂使用。使用NaOH / Nao AC梯度,用精确的IC-iPad方法确认所有活动。大多数商业葡聚糖酶在U. S.中来自真菌来源:Chaetomium Gracile或Erraticum,并以“非浓缩”或“浓缩”形式。在两个浓度形式之间存在近似的8-10倍差异,并且在每个形式内都存在活动变化。在2002/03年,仅将“非浓缩”葡聚糖酶应用于路易斯安那植物(通常是<10ppm / syrup)或果汁中。在果汁pH 5.4-5.8中研究“非浓缩”和“浓缩”葡聚糖酶,其在48.9°C或120°F下显示出相似的最大活性,如IC监测。葡聚糖酶的活动,在lastevaporator糖浆温度(〜63℃或145°F)和白利糖度(-65℃)条件下,被显着降低(活动开始25-30°白利糖度之后开始减少)。总体而言,果汁应用比将它们加入蒸发器糖浆更有效和经济。 “非浓缩”葡聚糖酶在蒸发器糖浆中的应用是不经济的。然而,“浓缩”葡聚糖酶可以在低至10ppm /固体(当上至45ppm /果汁中的水平上施加糖浆,以除去高达-37%的葡聚糖,可在发生严重的葡聚糖问题时考虑。在所有右旋酶的存在下加热汁至48.9℃,从果汁中显着地除去更多的葡聚糖(3380ppm /°Brix),而不是在施加的当前环境温度(32.2°C或90°F)并且更经济。对于“非浓缩的”葡聚糖,后为10ppm /果汁10分钟,48.9℃,-46.3进行比较13.6%32.2在℃下除去%葡聚糖。对于“浓缩”葡聚糖酶,仅在4ppm /果汁中仅10分钟后,除去66.6%的葡聚糖,在48.9℃下除去,被认为是过量的,相比32.2℃的29.6%。显示葡聚糖酶在果汁中存在二硫代氨基甲酸酯杀菌剂的存在,并且正在进行工厂研究以检查在48.9°C时不会产生不良葡聚糖。在工厂储存条件下,在磨削季节(90天),“浓缩”葡聚糖酶的活性仅略微降低(〜9%),而“非浓缩”葡聚糖酶活性大致减半(-46%),甚至降低在储存在制冷时的活动中。

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