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Improving the energy efficiency of traditional multi-stage steam-jet-ejector vacuum systems for deodorizing edible oils

机译:改善传统多级蒸汽喷射器真空系统的能效,用于除臭食用油

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The general objective of study was to develop and extend multi-stage steam-jet-ejector vacuum systems with competitive technical-economic characteristics for Bulgarian refineries of vegetable oils. The energy efficiency of these systems was improved by solving the following main tasks: (i) systems analysis of these multistage plants and (ii) a selection of eligible surface roughness of steam-jet-ejectors as a way for reducing their hydraulic losses and steam consumption. The systems analyse reveals that the consumption of motive steam and cooling water can be reduced when (i) the last stage of vacuum systems employs a water-ring vacuum pump instead of steam ejectors; (ii) four-stage vacuum systems are applied when cooling water with temperature above 30o is used; (iii) the first stage of vacuum system is without a condenser when the plant uses cooling water with temperature above 30 °C; (iv) the values of intermediate pressures in the end of the first and the second stages are optimized by means of a minimization of the total consumption of motive steam and cooling water in these stages. An engineering approach was developed for determining the eligible surface roughness of ejectors depending on Re number and the diameter of actual section. This approach assures to be obtained a minimal linear friction factor in each section. On this basis the eligible values of roughness average Ra for seven representative sections of ejectors were specified. Linear correlations between the roughness recommended and the section diameter were derived as well. The results show that the highest smoothness in the range of Ra= 0.06÷0.12 μm should be required for the narrowest critical section of the nozzle. A family of four-stage vacuum systems with suction flow from 10 to 75 kg/h vapour-air mixture at a suction pressure 300 Pa was developed and commercialized. Twelve vacuum systems have manufactured and introduced successfully for deodorizing vegetable oils in Bulgarian enterprises.
机译:研究的总体目标是开发和使用植物油的保加利亚炼油厂竞争力的技术经济特性扩展多级蒸汽射流喷射器的真空系统。 (ⅰ)这些多级的植物系统的分析和(ii)选择蒸汽喷射喷射器的合格的表面粗糙度的一种方式的用于减少他们的液压损失和蒸汽:这些系统的能量效率通过求解以下主要任务改善消耗。该系统分析表明,可以当(i)真空系统的最后一级采用水环真空泵代替蒸汽喷射器可以减少动力蒸汽和冷却水的消耗; (ii)与温度高于30°,使用的冷却水当四个级真空系统被应用; (ⅲ)真空系统的第一级是一个没有冷凝器当植物用途的冷却水温度高于30℃; (ⅳ)在所述第一和第二阶段的端部中间压力的值由动力蒸汽的总消耗量的最小化和冷却水在这些阶段中的装置进行了优化。工程方法被用于确定取决于雷诺数喷射器的合格表面粗糙度和实际截面的直径显影。在每个部分中能够获得这种方法确保了最小的线性摩擦系数。在此基础上进行了指定的平均粗糙度Ra为为喷射器的7层代表性的部分符合条件的值。粗糙度之间的线性关系推荐和截面直径推导为好。结果表明,在RA的范围内的最高平滑度= 0.06÷0.12微米应该被要求用于喷嘴的最窄临界区。四阶段的真空系统与从10至75千克/小时蒸汽 - 空气混合物在吸入压力为300Pa吸引流的家庭是开发和商业化。十二真空系统已成功制造并为保加利亚企业除臭植物油成功引进。

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