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啤酒酵母絮凝建模。

Modeling brewers' yeast flocculation.

作者信息

Caulet PJ, Luyben KC

机构信息

NIZO, Department of Process Engineering, P.O. Box 20, 6710 BA Ede, The Netherlands.

出版信息

Biotechnol Bioeng. 1998 Feb 5;57(3):330-41. doi: 10.1002/(sici)1097-0290(19980205)57:3<330::aid-bit10>3.0.co;2-k.

Abstract

Flocculation of yeast cells occurs during the fermentation of beer. Partway through the fermentation the cells become flocculent and start to form flocs. If the environmental conditions, such as medium composition and fluid velocities in the tank, are optimal, the flocs will grow in size large enough to settle. After settling of the main part of the yeast the green beer is left, containing only a small amount of yeast necessary for rest conversions during the next process step, the lagering. The physical process of flocculation is a dynamic equilibrium of floc formation and floc breakup resulting in a bimodal size distribution containing single cells and flocs. The floc size distribution and the single cell amount were measured under the different conditions that occur during full scale fermentation. Influences on flocculation such as floc strength, specific power input, and total number of yeast cells in suspension were studied. A flocculation model was developed, and the measured data used for validation. Yeast floc formation can be described with the collision theory assuming a constant collision efficiency. The breakup of flocs appears to occur mainly via two mechanisms, the splitting of flocs and the erosion of yeast cells from the floc surface. The splitting rate determines the average floc size and the erosion rate determines the number of single cells. Regarding the size of the flocs with respect to the scale of turbulence, only the viscous subrange needs to be considered. With the model, the floc size distribution and the number of single cells can be predicted at a certain point during the fermentation. For this, the bond strength between the cells, the fractal dimension of the yeast, the specific power input in the tank and the number of yeast cells that are in suspension in the tank have to be known. Copyright 1998 John Wiley & Sons, Inc.

摘要

酵母细胞的絮凝发生在啤酒发酵过程中。在发酵进行到一半时,细胞变得絮凝并开始形成絮状物。如果环境条件,如培养基成分和罐内流体速度是最佳的,絮状物会生长到足够大的尺寸以沉降。酵母的主要部分沉降后,剩下的是嫩啤酒,其中只含有少量酵母,这些酵母是下一工艺步骤(陈酿)中剩余转化所必需的。絮凝的物理过程是絮凝形成和絮凝破碎的动态平衡,导致包含单细胞和絮状物的双峰尺寸分布。在全规模发酵过程中出现的不同条件下测量了絮状物尺寸分布和单细胞数量。研究了诸如絮凝强度、比功率输入和悬浮酵母细胞总数等对絮凝的影响。开发了一个絮凝模型,并使用测量数据进行验证。酵母絮凝形成可以用碰撞理论来描述,假设碰撞效率恒定。絮状物的破碎似乎主要通过两种机制发生,即絮状物的分裂和酵母细胞从絮状物表面的侵蚀。分裂速率决定了平均絮状物尺寸,侵蚀速率决定了单细胞数量。关于絮状物尺寸相对于湍流尺度的情况,只需要考虑粘性子层。利用该模型,可以预测发酵过程中某一时刻的絮状物尺寸分布和单细胞数量。为此,必须知道细胞之间的键强度、酵母的分形维数、罐内的比功率输入以及罐内悬浮的酵母细胞数量。版权所有1998约翰威立父子公司。

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