METHOD OF REDUCING WATER HARDNESS SALTS AND HEAT AND MASS EXCHANGE EQUIPMENT FOR ITS IMPLEMENTATION

докт. техн. наук, Целень Б.Я канд. техн. наук, канд. техн. наук Резакова Т.А, канд. техн. наук
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Abstract

Thousands of steam and water boilers of medium and low parameters operate in the country's industry, municipal energy, and agriculture. Their reliable work is largely determined by maintaining a rational water-chemical regime. Dissolved impurities that affect the operation of boiler equipment primarily include hardness salts. When using hard water, scale is formed on the surfaces, heat transfer deteriorates, and pipes are overheated from the heating side, which can lead to their destruction. The purpose of the work is to improve the quality of softened water, reduce the consumption of reagents, and accelerate the softening process due to the use of heat and mass exchange equipment. In the work, water desalination was carried out by the method of discrete-pulse energy input in a rotor-pulsation apparatus. Ammonia was used as a reagent for removing hardness salts. The water-ammonia mixture is processed in the rotor-pulsation apparatus at a flow pulsation frequency of 3-5 kHz and a pressure drop amplitude of 360-400 kPa until the temperature rises to 40ºС. The increase in temperature occurs due to the transition of mechanical energy into thermal energy. It was determined that the degree of softening of water is 99% at a mass concentration of ammonia of 0.022%, and the amplitude of the pressure drop is 400 kPa. As the amplitude of the pressure drop decreases to 380 and 360 kPa, the degree of water softening decreases to 90 and 95%, respectively. It is also determined that water desalination using the rotor-pulsation apparatus should be carried out in the mode of recirculation of ammonia solution with a concentration of 0.022%, with a flow pulsation frequency of 4 kHz and a pressure drop amplitude of 400 kPa. As a result of the work, the optimal technological parameters of water treatment were determined and the efficiency of its purification using the proposed equipment was proved in comparison with the conventional one.
降低水硬度盐的方法及其实施的热质交换设备
全国工业、市政能源、农业中、低参数蒸汽、水锅炉数千台。它们可靠的工作在很大程度上取决于保持合理的水化学机制。影响锅炉设备运行的溶解杂质主要包括硬度盐。当使用硬水时,表面形成水垢,传热恶化,管道从加热侧过热,这可能导致其破坏。该工作的目的是提高软化水的质量,减少试剂的消耗,并因使用热交换设备而加速软化过程。在转子脉动装置中,采用离散脉冲能量输入的方法进行海水淡化。用氨作为脱除硬度盐的试剂。水-氨混合物在转子脉动装置中以3-5 kHz的流量脉动频率和360-400 kPa的压降幅值处理,直至温度升至40ºС。温度的升高是由于机械能向热能的转变而发生的。测定了氨质量浓度为0.022%时,水的软化度为99%,压降幅值为400 kPa。当压降幅值减小到380 kPa和360 kPa时,水软化程度分别减小到90%和95%。还确定了转子脉动装置的海水淡化应以浓度为0.022%的氨溶液再循环模式进行,流量脉动频率为4 kHz,压降幅值为400 kPa。通过试验,确定了水处理的最佳工艺参数,并与常规设备进行了对比,验证了该设备对水的净化效果。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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