首页> 外文会议>Sugar Industry Technologists, Inc. Annual Meeting; 20060514-17; La Baule(FR) >Technology and Energy Economics of Sugar Production: Possibilities of Process Development
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Technology and Energy Economics of Sugar Production: Possibilities of Process Development

机译:糖生产的技术和能源经济学:工艺开发的可能性

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The energy required to make food is made up of the parts for the production of the raw materials through agriculture, together with the technological processing of the raw materials and the further treatment of the product until it is consumed. The energetic input is equal to the main and by-product energetic values created. An analysis of food production according to the Input-Output balancing is thus possible.rnThe specific energy input in relation to product in white sugar manufacturing form beet (including pulp drying) ranges between 6 and 12,5 MJ/kg. The minimum achievable at present lies below 4 MJ/kg. An essential precondition to reach this value is the energy link between pulp drying and sugar processing. Moreover, new ways to be found in crystallization, with innovations in continuous evapo-crystallization playing a key role.rnThe evapo-crystallization tower (VKT) enables the optimum design and construction of calandrias and stirrers for all cells in the cascade. As the individual cells can be by-passed and cleaned separately, high availability of the proposed plant is always ensured. Given the continuous pans with mechanical circulation can be Operated with small temperature differentials; this can be utilized for double-effected evaporation within a crystallization stage. Depending on the crystallization system, heating steam requirements are reduced by 35-50%.rnThe further development of evaporator technology in the sugar industry based not only on the requirement for high k-values, but also requires besides this a compact cost effective design of the operation with a minimum temperature gradient between heating steam and vapour. Based only on evaporator design, achieving a high heat flux density (kW/m2) at low temperature gradient, e.g. 8 stage evaporator systems with an economically interesting heating surface utilization can be realised.
机译:制作食物所需的能量由通过农业生产原料的部分,原料的技术处理以及对产品的进一步处理直至消费而构成。能量输入等于创建的主要和副产品能量值。因此,可以根据投入产出平衡来分析食品生产。rn与白糖生产形式甜菜中的产品(包括纸浆干燥)相关的比能量输入范围为6至12.5 MJ / kg。目前可达到的最小值低于4 MJ / kg。达到该值的基本前提是纸浆干燥和制糖之间的能源联系。此外,在结晶中发现新方法的过程中,连续蒸发结晶的创新也起着关键作用。蒸发结晶塔(VKT)可以为级联中的所有单元优化设计和构造加热装置和搅拌器。由于可以单独旁路和清洗各个电池,因此始终可以确保所提议的设备的高可用性。由于具有机械循环的连续锅可以在很小的温差下操作;这可用于结晶阶段内的双重蒸发。根据结晶系统的不同,加热蒸汽的需求量可降低35-50%。rn糖业中蒸发器技术的进一步发展不仅基于对高k值的要求,而且还要求紧凑的,经济高效的设计。在蒸汽和蒸气之间的最小温度梯度下运行。仅基于蒸发器设计,可在低温梯度下实现高热通量密度(kW / m2),例如可以实现经济实用的8级蒸发器系统。

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