RESULTS OF EXPERIMENTAL STUDIES OF THE HEAT ENGINEERING CHARACTERISTICS OF INDUSTRIAL FURNACE WATER-HEATING HEAT RECOVERY UNITS

N. Fialko, V. Prokopov, R. Navrodska, S. Shevchuk, A. Stepanova
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Abstract

The results of a complex of experimental studies of thermal and aerodynamic indicators of water-heating heat-recovery exchangers of dusty exhaust gases from glass-making furnaces are presented. The studies were carried out on an experimental installation located behind a glass-melting furnace, and in the process of start-up operations during the introduction into operation of modular-type water-heating heat exchangers (HWM) developed by IET NAS of Ukraine at various glass-producing enterprises. The studies were carried out using modern measuring equipment according to certified methods of the services of metrological adjustment of glass-making enterprises, with the participation of which the experiments were carried out. In the process of research, the heating capacity, average values of the heat transfer coefficients and aerodynamic resistance of heat exchange surfaces, which are assembled from of panel packages formed by pipes with membranes, under conditions of heat-recovery of dusty furnace gases, were determined. The dynamics of the formation of a layer of deposits of technological dust on the surface of the panels on the gas side and the contamination coefficient of surface were also subject to research. According to the data on the heat-recovery exchanger heating capacity, the rational period of its operation between cleaning the working surfaces was determined. The experimental parameters obtained were also compared with their calculated values, as well as with the data of other researchers. According to the results of the studies, it is shown that TVM heat exchangers when used in conditions of dusty furnace gases are characterized by high thermal efficiency due to the layout of the heat exchange surface from the packets of panels formed by pipes with membranes, and the possibility of cleaning these surfaces from deposits of technological dust with practical restoration of the initial indicators. Based on the data obtained, the duration of the cycles for cleaning membrane heating surfaces from dust deposits was determined: for furnaces for the production of glass packaging, this period was 10-14 days, and for furnaces for melting medical glass - 5-7 days.
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工业炉膛水加热余热装置热工特性的实验研究结果
本文介绍了玻璃冶炼炉含尘废气水加热式热回收换热器的热学指标和空气动力学指标的综合实验研究结果。该研究是在位于玻璃熔化炉后面的实验装置上进行的,并且是在将乌克兰IET NAS开发的模块化水加热热交换器(HWM)在各玻璃生产企业投入运行期间的启动操作过程中进行的。研究采用现代测量设备,按照玻璃制造企业计量调整服务的认证方法进行,并参与了实验。在研究过程中,测定了含尘炉气热回收条件下,由带膜管道组成的面板包组成的换热面的热容量、换热系数平均值和气动阻力。研究了气侧板表面工艺粉尘沉积层的形成动力学及表面污染系数。根据热交换器的热容量数据,确定了热交换器在两次清洗工作表面之间的合理运行周期。并将得到的实验参数与其计算值以及其他研究者的数据进行了比较。研究结果表明,在含尘炉气条件下使用的TVM热交换器具有高热效率的特点,因为热交换表面的布局是由带膜的管道形成的板包组成的,并且可以通过实际恢复初始指标来清除这些表面的工艺粉尘沉积。根据获得的数据,确定了清除膜受热面积尘的周期:用于生产玻璃包装的炉,周期为10-14天,用于熔化医用玻璃的炉为5-7天。
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