Experimental study of calcium sulfate fouling in a heat exchanger during liquid-solid fluidized bed with cylindrical particles
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Experimental study of calcium sulfate fouling in a heat exchanger during liquid-solid fluidized bed with cylindrical particles

机译:圆柱形颗粒液固流化床中热交换器中硫酸钙污垢的实验研究

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AbstractCalcium sulfate fouling was determined experimentally in a heat exchanger during liquid-solid fluidized bed with cylindrical particles and forced convective (without particles) heat transfer. The effects of bed voidage, wall temperature and foulant concentration on fouling resistance were studied during fluidized bed heating and compared with corresponding cases in forced convective (without particles) heating. The results show that fouling resistance was considerably decreased during fluidized bed heat transfer compared with forced convective heat transfer (without particles). Maximum fouling removal as heat transfer occurred at bed voidages ranging from 0.6 to 0.8; under these conditions, fouling resistance was lowered to at least one-seventh that of similar cases in forced convective heat transfer.]]>
机译:<![CDATA [ 抽象 硫酸钙污垢在液体固体流化床中通过圆柱形颗粒和强制对流(没有粒子)传热。在流化床加热期间研究了床空隙,壁温和污垢浓度对污垢抗性的影响,与强制对流(无颗粒)加热的相应案例相比。结果表明,与强迫对流热传递(没有颗粒)相比,流化床传热期间污垢抗性显着降低。最大污垢移除作为热传递发生在床上的床上,范围为0.6至0.8;在这些条件下,污垢抗性降至至少第七,在强制对流热传递中的类似病例中的至少一秒钟。 ]]>

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