乳品厂压缩制冷装置的热集成

S. Bykanov, Babak Tetiana Babak, Roman Stotskyi
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引用次数: 0

摘要

采用夹点分析方法,对不同奶牛场的氨压缩制冷装置进行了热集成。以该机组1000kw制冷量的原理图为依据。计算了给定制冷量下的主循环温度、制冷剂消耗量及其比热容。根据这些数据,形成了一个流表,其中包括制冷剂氨的热流和两种冷流:化学水处理用水和技术用水。氨热流分为氨蒸气冷却、冷凝和过冷三种流。测定了各流的热容、流量和热负荷(流焓变)。换热器的最小温差DTmin = 8°С是根据该工艺的技术经济计算确定的。绘制了最小温差的复合曲线。采用问题表算法确定了冷热流的夹点温度。确定了冷热负荷最小值(QHmin和QСmin)。确定热回收能力为701.8 kW。建立网格图,按照CP和N规则布置换热器。根据网格图提出了工艺流程的改造方案,包括安装3台换热器、1台冷却器和2台加热器,以达到目标温度和流量。建议采用阿法拉伐板式换热器作为换热设备。本设计投资回收期约为两年。
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THERMAL INTEGRATION OF COMPRESSION REFRIGERATION UNITS IN DAIRY FACILITIES
The heat integration of an ammonia compression refrigeration unit, that is used in different dairy facilities, was carried out by the pinch analysis methods. The schematic diagram of such unit with a cooling capacity of 1000 kW was taken as a basis. The main cycle temperatures, refrigerant consumption and its specific heat capacity were calculated for a given refrigerating capacity. Based on these data, a stream table was formed, that included a hot stream of a refrigerant – ammonia – and also two cold streams: water for chemical water treatment and water for technology. The hot stream of ammonia was divided into three streams: cooling of ammonia vapors, condensation and subcooling. Heat capacities flowrates and heat loads (stream enthalpy change) of the streams were determined. The minimum temperature difference in heat exchangers DTmin = 8°С was determined on the basis of technical and economic calculations for this process. The composite curves were plotted for the minimum temperature difference. The pinch temperatures were determined by the problem table algorithm for the hot and cold streams. The minimum values of hot and cold utilities load (QHmin and QСmin) were determined. The heat recovery capacity was determined, which was 701.8 kW. A grid diagram was built and heat exchangers are arranged in accordance with CP and N rules. The retrofit of process flowsheet is proposed on the basis of the grid diagram that includes the installation of three heat exchangers, one cooler and two heaters to achieve the target temperatures and flow rates. The use of Alfa Laval plate heat exchangers is proposed as heat exchange equipment. The payback period of the design is about two years.
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