Clarification of a wheat straw‐derived medium with ion‐exchange resins for xylitol crystallization

BACKGROUND: Xylitol bioproduction from lignocellulosic residues comprises hydrolysis of the hemicellulose, detoxification of the hydrolysate, bioconversion of the xylose, and recovery of xylitol from the fermented hydrolysate. There are relatively few reports on xylitol recovery from fermented media. In the present study, ion‐exchange resins were used to clarify a fermented wheat straw hemicellulosic hydrolysate, which was then vacuum‐concentrated and submitted to cooling in the presence of ethanol for xylitol crystallization. RESULTS: Sequential adsorption into two anion‐exchange resins (A‐860S and A‐500PS) promoted considerable reductions in the content of soluble by‐products (up to 97.5%) and in medium coloration (99.5%). Vacuum concentration led to a dark‐colored viscous solution that inhibited xylitol crystallization. This inhibition could be overcome by mixing the concentrated medium with a commercial xylitol solution. Such a strategy led to xylitol crystals with up to 95.9% purity. The crystallization yield (43.5%) was close to that observed when using commercial xylitol solution (51.4%). CONCLUSION: The experimental data demonstrate the feasibility of using ion‐exchange resins followed by cooling in the presence of ethanol as a strategy to promote the fast recovery and purification of xylitol from hemicellulose‐derived fermentation media. Copyright © 2008 Society of Chemical Industry     

Casein Hydrolysate Fractions Act as Emulsifiers in Process Cheese

ABSTRACT: Degrees of hydrolysis and emulsifying activity of casein hydrolysates were the highest at 4 h hydrolysis. The oil-off values of the mixture of hydrolysate (H) or supernatant (S) and traditional emulsifier (T) were not significantly different from the control made with traditional emulsifier, except for S + T = 3:1. Two other samples made with hydrolysate or supernatant only (H or S) showed higher oil-off value than the others (p < 0.05). In flavor property, no difference was found between samples made with traditional emulsifier and those made with the mixture of hydrolysate or supernatant at the ratio of 3 to 1. Therefore, these results indicated that a mixture of the hydrolysate or supernatant and traditional emulsifier might replace a traditional emulsifier in process cheese manufacturing.     

酪素/蒙脱土插层复合物制备及其耐水性能研究

在十六烷基季胺盐存在下进行蒙脱土插层得到[H4N(CH2)15CH3]+-蒙脱土插层物,酪素加热溶解后与[H4N(CH2)15CH]+-蒙脱土插层物混合,保温复合,然后沉淀分离,得到干酪素/蒙脱土纳米复合物。用XRD,TEM和TGA表征酪素纳米复合物的结构与性能。结果表明,插层复合物中蒙脱土晶片间距扩大,插层复合物耐热性能明显提高,与纯酪素相比,复合物拥有极好的耐水性能,特别适用于制备高速高性能啤酒生产线用贴标胶。     

Fractionation of partially stereoregular poly(propylene oxide)

Partially stereoregular poly(propylene oxide) samples were synthesized via reactions catalysed by a preformed analytically defined trimethylaluminium hydrolysate. These samples were fractionated into two contrastingly different fractions.

1. (i) D-polymers: This fraction constituted the major part (up to 90%). It mainly contained cyclic low molecular weight oligomers (MW < 1000). The linear chains found in D-polymers had hydroxyl end groups. No double bonds could be detected spectroscopically.

2. (ii) K-polymers: This fraction was high molecular weight stereoregular polymer. Stepwise thermal precipitation from dilute isooctane solution of K-polymers yielded a succession of fractions which differed in melting point. It appears that the phase equilibria during the thermal precipitations were not controlled by the molecular weights of species.

萃取法制备干酪素

干酪素是一种用途极为广泛的精细化工产品，用萃取法生产工业干酪素，其产品质量优于机械分离法，对生产特级品工业干酪素有一定推动作用。     

玉米黄粉酶解液在黄原胶发酵生产应用的研究

以玉米黄粉酶解液为氮源应用于黄原胶发酵培养基，探讨了蛋白酶种类、玉米黄粉酶解液添加量和酶添加量等因素对其发酵黄原胶粘度和产胶率的影响，并优化了复配氮源的种类及其复配比例。结果表明，碱性蛋白酶水解液作为氮源发酵黄原胶的粘度和产胶率优于其它蛋白酶解液；当酶解液添加量为6%、碱性蛋白酶添加量为8kU时，发酵黄原胶的粘度和产胶率可以达到4235cp和24.4g/L。大豆蛋白与玉米黄粉酶解液复配效果优于与棉籽粉、豆粕粉、花生粉的复配；玉米黄粉酶解液与大豆蛋白复配比为3:7时，发酵黄原胶的粘度和产胶率可以达到5833cp和32.4g/L，与单独以大豆蛋白为氮源无明显差异。本研究为提高玉米黄粉资源利用率、降低黄原胶的发酵生产成本提供了新思路。     

A Possible Industrial Solution to Ferment Lignocellulosic Hydrolyzate to Ethanol: Continuous Cultivation with Flocculating Yeast

The cultivation of toxic lignocellulosic hydrolyzates has become a challenging research topic in recent decades. Although several cultivation methods have been proposed, numerous questions have arisen regarding their industrial applications. The current work deals with a solution to this problem which has a good potential application on an industrial scale. A toxic dilute-acid hydrolyzate was continuously cultivated using a high-cell-density flocculating yeast in a single and serial bioreactor which was equipped with a settler to recycle the cells back to the bioreactors. No prior detoxification was necessary to cultivate the hydrolyzates, as the flocks were able to detoxify it in situ. The experiments were successfully carried out at dilution rates up to 0.52 h⁻¹. The cell concentration inside the bioreactors was between 23 and 35 g-DW/L, while the concentration in the effluent of the settlers was 0.32 ± 0.05 g-DW/L. An ethanol yield of 0.42–0.46 g/g-consumed sugar was achieved, and the residual sugar concentration was less than 6% of the initial fermentable sugar (glucose, galactose and mannose) of 35.2 g/L.     

干酪素型啤酒标签胶的研究进展

从制备原理及分散体系、交联剂、改性助剂等方面综述了干酪素型啤酒标签胶的研究进展,并对该领域研究进行了展望。     

碱性蛋白酶对酪蛋白水解的最适宜条件

蛋白质酶解是改善蛋白质特性，便于人体吸收的有效途径。我们对富含于乳制品中的酪蛋白，采用碱性蛋白酶进行水解实验。通过对主要影响因素的分析及回归方法，确定碱性蛋白酶对酪蛋白水解的最佳工艺条件：温度55℃，酶—底物比为7％，底物质量分数为6％，pH值为8。     

固定化细胞在三相流化床中发酵生产木糖醇

为了建立一种成本低、产率高、能连续高效地生产木糖醇的新工艺,研究了固定化假丝酵母(Candida sp.)细胞在三相流化床内分批发酵玉米芯半纤维素水解液生产木糖醇这一工艺过程.适宜的工艺条件为:32℃,起始木糖质量浓度100g/L,固定化细胞与发酵培养基体积比1:3.8,分段通气:0～24 h,0.5 L/min;24～80 h,0.175 L/min.利用固定化细胞重复进行6批发酵,木糖醇得率平均为63.5%.玉米芯半纤维素水解液未经脱色以及离子交换等脱毒处理便可直接有效地转化成木糖醇;三相流化床生物反应器动力消耗少、流化状态稳定均匀.该方法大大降低了原料预处理的成本,发酵结果较好.