{"title":"开发将甘薯淀粉转化为葡萄糖浆的试验系统。","authors":"Valerian C K Silayo, John Y Lu, Heshmat A Aglan","doi":"10.3727/1542966034605306","DOIUrl":null,"url":null,"abstract":"<p><p>Sweet potato has been chosen as one of NASA's crops to support human beings in future space missions. One of the possible uses is to make syrup that can be used as a general sweetener. In this work a simple engineering system for converting sweet potato starch into glucose syrup was studied on a laboratory scale. The system comprises the following main units: a blender, continuous stirred tank reactor (CSTR), centrifugal and vacuum filters, deionization column and vacuum evaporator. The system was tested by carrying out conversion processes from fresh sweet potato roots. The roots were pealed, sliced, homogenized, heated and hydrolyzed by diastase of malt and Dextrozyme C (Novo Nordisk BioChem, North America, Inc.) enzymes in the CSTR. After hydrolysis the slurry was filtered, de-ionized and concentrated to get glucose syrup. The performance of the system was evaluated based on the quality of the conversion. The main factor was the level of reducing sugars except for the deionization where ash content and color were the main factors. Through careful control of the system units, good heating performance in the CSTR was obtained and the hydrolysis process attained sufficient conversion. The filtration process that incorporated the centrifuge was faster than when it was by-passed to the vacuum filter but losses in sugars were higher. Deionization removed more than 90% of the ash and reduced pigmentation, with probable insignificant losses in sugars during the deionization process. Recovery levels when the centrifuge was used and when it was by-passed could reach about 65% and 78%, respectively. These correspond to reducing sugar concentration of 259 and 310 mg/ml in 150-ml syrups from 300 g of sweet potatoes in each process. However, from concentration trials, syrups with volumes of 100 and 70 ml with the respective dextrose equivalence of 281 and 213 mg/ml were obtained. The syrups obtained were brownish in color and the process that employed centrifugal filtration gave a product with color that resembled the original color of the sweet potatoes. Further work is required to improve the overall system performance.</p>","PeriodicalId":86963,"journal":{"name":"Habitation (Elmsford, N.Y.)","volume":"9 1-2","pages":"9-15"},"PeriodicalIF":0.0000,"publicationDate":"2003-01-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://sci-hub-pdf.com/10.3727/1542966034605306","citationCount":"8","resultStr":"{\"title\":\"Development of a pilot system for converting sweet potato starch into glucose syrup.\",\"authors\":\"Valerian C K Silayo, John Y Lu, Heshmat A Aglan\",\"doi\":\"10.3727/1542966034605306\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<p><p>Sweet potato has been chosen as one of NASA's crops to support human beings in future space missions. One of the possible uses is to make syrup that can be used as a general sweetener. In this work a simple engineering system for converting sweet potato starch into glucose syrup was studied on a laboratory scale. The system comprises the following main units: a blender, continuous stirred tank reactor (CSTR), centrifugal and vacuum filters, deionization column and vacuum evaporator. The system was tested by carrying out conversion processes from fresh sweet potato roots. The roots were pealed, sliced, homogenized, heated and hydrolyzed by diastase of malt and Dextrozyme C (Novo Nordisk BioChem, North America, Inc.) enzymes in the CSTR. After hydrolysis the slurry was filtered, de-ionized and concentrated to get glucose syrup. The performance of the system was evaluated based on the quality of the conversion. The main factor was the level of reducing sugars except for the deionization where ash content and color were the main factors. Through careful control of the system units, good heating performance in the CSTR was obtained and the hydrolysis process attained sufficient conversion. The filtration process that incorporated the centrifuge was faster than when it was by-passed to the vacuum filter but losses in sugars were higher. Deionization removed more than 90% of the ash and reduced pigmentation, with probable insignificant losses in sugars during the deionization process. Recovery levels when the centrifuge was used and when it was by-passed could reach about 65% and 78%, respectively. These correspond to reducing sugar concentration of 259 and 310 mg/ml in 150-ml syrups from 300 g of sweet potatoes in each process. However, from concentration trials, syrups with volumes of 100 and 70 ml with the respective dextrose equivalence of 281 and 213 mg/ml were obtained. The syrups obtained were brownish in color and the process that employed centrifugal filtration gave a product with color that resembled the original color of the sweet potatoes. 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引用次数: 8
摘要
甘薯已被美国宇航局选为支持人类未来太空任务的作物之一。其中一种可能的用途是制作糖浆,可以用作一般的甜味剂。在实验室规模上研究了一种简单的将甘薯淀粉转化为葡萄糖浆的工程系统。该系统包括以下主要装置:搅拌器、连续搅拌罐式反应器(CSTR)、离心和真空过滤器、去离子塔和真空蒸发器。该系统通过对新鲜甘薯根进行转化过程进行了测试。根被剥皮、切片、均质、加热并在CSTR中用麦芽淀粉酶和Dextrozyme C (Novo Nordisk BioChem, North America, Inc.)酶水解。水解后的浆液经过滤、去离子、浓缩得到葡萄糖浆。根据转换质量对系统的性能进行了评价。除去离子作用外,还原糖水平是主要影响因素,灰分含量和颜色是主要影响因素。通过对系统单元的精心控制,在CSTR中获得了良好的加热性能,并且水解过程得到了充分的转化。结合离心机的过滤过程比旁路到真空过滤器的过滤过程要快,但糖的损失更高。去离子去除了90%以上的灰分,减少了色素沉着,在去离子过程中糖的损失可能微不足道。使用离心机和旁路时的回收率分别可达65%和78%左右。这相当于在每道工序中从300克红薯中提取的150毫升糖浆中的还原糖浓度分别为259毫克和310毫克/毫升。然而,从浓度试验中,获得了体积为100和70 ml的糖浆,葡萄糖当量分别为281和213 mg/ml。得到的糖浆呈褐色,采用离心过滤的过程使产品的颜色与红薯的原始颜色相似。需要进一步的工作来提高整个系统的性能。
Development of a pilot system for converting sweet potato starch into glucose syrup.
Sweet potato has been chosen as one of NASA's crops to support human beings in future space missions. One of the possible uses is to make syrup that can be used as a general sweetener. In this work a simple engineering system for converting sweet potato starch into glucose syrup was studied on a laboratory scale. The system comprises the following main units: a blender, continuous stirred tank reactor (CSTR), centrifugal and vacuum filters, deionization column and vacuum evaporator. The system was tested by carrying out conversion processes from fresh sweet potato roots. The roots were pealed, sliced, homogenized, heated and hydrolyzed by diastase of malt and Dextrozyme C (Novo Nordisk BioChem, North America, Inc.) enzymes in the CSTR. After hydrolysis the slurry was filtered, de-ionized and concentrated to get glucose syrup. The performance of the system was evaluated based on the quality of the conversion. The main factor was the level of reducing sugars except for the deionization where ash content and color were the main factors. Through careful control of the system units, good heating performance in the CSTR was obtained and the hydrolysis process attained sufficient conversion. The filtration process that incorporated the centrifuge was faster than when it was by-passed to the vacuum filter but losses in sugars were higher. Deionization removed more than 90% of the ash and reduced pigmentation, with probable insignificant losses in sugars during the deionization process. Recovery levels when the centrifuge was used and when it was by-passed could reach about 65% and 78%, respectively. These correspond to reducing sugar concentration of 259 and 310 mg/ml in 150-ml syrups from 300 g of sweet potatoes in each process. However, from concentration trials, syrups with volumes of 100 and 70 ml with the respective dextrose equivalence of 281 and 213 mg/ml were obtained. The syrups obtained were brownish in color and the process that employed centrifugal filtration gave a product with color that resembled the original color of the sweet potatoes. Further work is required to improve the overall system performance.