优化生物燃料生产装置中菜籽油运输成本的方法

K. Durczak, T. Brylewski
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摘要

背景。菜籽油是波兰气候条件下生产生物燃料的主要来源。这种油在原始状态下具有很高的运动粘度,远高于由它衍生的酯类RME。菜籽油的这种特性在工业液压系统的运输过程中产生了额外的成本。研究的目标是开发一种技术,通过加热菜籽油,然后再在储罐之间泵送,从而降低菜籽油的粘度。材料和方法。本研究以生菜籽油为原料进行酯交换。实验室的模拟试验是在专门设计的试验台上进行的,用于测试容积为5升的油箱的粘性液体的特性。将油在5℃温度范围内加热20÷80℃,并确定其加热成本HC,泵送成本PC,弥补总运输成本TC。然后用解析法和图解法确定菜籽油在管道运输过程中的最佳温度。结果。将新鲜菜籽油温度从20°C加热到80°C,运动粘度从62 mm2·s-1显著降低到10 mm2·s-1。在这个温度范围内,油加热成本的增长速度超过了电机驱动泵的低负荷带来的好处。结论。在液体体积小的情况下,提出油菜籽油制备罐加热的方法,以降低其粘度而无任何可识别的经济效益。数学分析表明,在研究的较低温度范围内(这里To = 20°C),总成本最小。然而,对于大流量和低温的液压装置操作,例如在冬季,当油产生有意义的流动阻力时,该方法可以变得有利可图。这需要在工业规模上进行进一步的研究。
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A method of optimizing the rapeseed oil transportation costs in biofuel production installations
Background. Rapeseed oil is the main source of production biofuels in the Polish climatic conditions. This oil in the raw state has a high kinematic viscosity, much higher than the esters derived from it RME. Such a property rapeseed oil generates additional costs during its transport in industrial hydraulic systems. The goal of study was to develop a technology to reduce the viscosity of rapeseed oil by heating it before further pumping between the tanks. Material and methods. The research was raw rapeseed oil prior to transesterification. The simulation tests in the laboratory were performed on a specially designed test bench for testing the properties of a viscous liquid having a volume of 5 liter tank. The oil is heated heater at 5°C temperature range 20÷80°C and determined the cost of its heating HC, the costs of pumping PC, making up the total cost of transport TC. Then the analytical method and graphical establish optimum temperature rapeseed oil during transport in pipelines. Results. Heating the fresh rapeseed oil temperature from 20°C to 80°C causes a significant reduction in the kinematic viscosity from 62 to 10 mm2·s-1. In this temperature range, the cost of oil heating grow faster than the benefits of a lower load the electric motor driving the pump. Conclusions. In the case of small volumes of liquid heating method proposed rapeseed oil preparation tank in order to reduce its viscosity without any recognizable economic benefits. Mathematical analysis showed that the total costs were the smallest in the lower temperature range studied (here To = 20°C). Yet, the method can become profitable for large flows and low temperatures of hydraulic installations operation e.g. in the winter season when a oil puts up a meaningful resistance of flow. This requires further research conducted on an industrial scale.
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