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Mathematical Modelling of a Reduced Thermal Energy Consuming Spray Dryer for Evaporating Caustic Soda Solution

机译:用于蒸发苛性钠溶液的降低热能消耗的喷雾干燥器的数学模型

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Experimental demonstration, mathematical modelling and simulation of a technique for reducing thermal energy consumption in the diaphragm cell process using a techno-economically viable process to produce 73% wt. NaOH from electrolytic diaphragm cell catholytes of about 10% wt. NaOH was carried out in this work. The technique completely eradicated the use of thermal energy in concentrating catholyte effluents from about 10% wt. NaOH solution to 50% wt. NaOH solution. This resulted in a specific energy savings of about 2.68×10~6 J/kg NaOH. The use of a spray dryer for increasing the concentration of 50% wt. NaOH solution to 73% wt. NaOH solution further improved the energy savings compared to that of multiple effect evaporators by 1.41×10~6 J/kg of solution, which corresponds to about 61.05% specific energy savings. The deviation of all simulated results from experimental data was between -0.062 and +0.084, portraying a good predictive tool for probing into the spray dryer operations. This work is expected to reduce considerably the total energy consumption of the diaphragm cell process through process integration or new processing methodology, with improved equipment designs.
机译:实验证明,数学建模和模拟技术可降低隔膜电池工艺中的热能消耗,该工艺使用技术经济可行的工艺来生产73%wt。来自电解隔膜电池阴极电解液的NaOH约为10%wt。在这项工作中进行了NaOH。该技术完全消除了将热能用于浓缩约10%wt。%的阴极电解液流出物中。 NaOH溶液至50重量%。 NaOH溶液。这样可以节省约2.68×10〜6 J / kg NaOH的比能量。使用喷雾干燥器将浓度提高50%(重量)。 NaOH溶液至73重量%。与多效蒸发器相比,NaOH溶液进一步节省了1.41×10〜6 J / kg的溶液,相当于约61.05%的比能耗。所有模拟结果与实验数据的偏差都在-0.062至+0.084之间,这说明了探究喷雾干燥器运行的良好预测工具。通过改进工艺和设备设计,通过工艺集成或新的工艺方法,这项工作有望大大减少隔膜电池工艺的总能耗。

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