首页> 外文会议>International Society of Sugar Cane Technologists Congress vol.1; 20050130-0204; Guatemala City(GT) >MODELLING A CONTINUOUS PAN INSTALLATION USING SUGARS™ FOR WINDOWSreg;
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MODELLING A CONTINUOUS PAN INSTALLATION USING SUGARS™ FOR WINDOWSreg;

机译:使用SUGARS™forWINDOWS®对连续的Pan安装进行建模

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The installation of a continuous pan for the Sugar Cane Growers Cooperative of Florida factory was modelled using the Sugars™ computer program to evaluate changes in the process and potential changes in revenues. A model was constructed of the existing factory, and factory data were used to define the performance of equipment in the model and to estimate the solubility characteristics of the syrup by determining the coefficients for the Vavrinecz solubility function. Balance calculations from the model were then compared to the actual operation to verify the model. Next, the model was modified to use a continuous pan for 50% of the ''B'' boiling and reduced sucrose supersaturation for the ''A'' and ''C boilings to compensate for the reduced loadings in these boilings from the installation of the continuous pan. The reduced loading in the ''A'' boiling would occur because an existing ''B'' batch pan would be moved to the ''A'' boiling when it is replaced by the new continuous pan, and the ''C boiling would be reduced because of a load reduction. Results from the simulation showed that the factory could expect an increase in process revenues with decreases in the final molasses purity and the bagasse consumed by the boilers. ''B'' centrifugal performance was then increased to see if the effect of more consistent crystal size variation in the ''B'' massecuite from the continuous pan would improve factory performance. It was found that improvements in ''B'' centrifugal performance were not as significant as the performance improvements from the lower supersaturation values used in the ''A'' and ''C boilings.
机译:使用Sugars™计算机程序模拟了佛罗里达州甘蔗种植者合作社的连续锅的安装,以评估过程中的变化以及潜在的收入变化。在现有工厂的基础上建立模型,并使用工厂数据定义模型中设备的性能,并通过确定Vavrinecz溶解度函数的系数来估计糖浆的溶解度特性。然后将来自模型的余额计算与实际操作进行比较,以验证模型。接下来,对模型进行修改,以使用连续锅进行“ B”沸腾的50%,并降低“ A”和“ C”沸腾的蔗糖过饱和度,以补偿安装中这些沸腾的负载减少连续锅。降低“ A”沸腾的负荷是因为将现有的“ B”分批锅替换为新的连续锅,然后将其移至“ A”沸腾,而将“ C”沸腾由于负载减少而减少。模拟的结果表明,随着最终糖蜜的纯度和锅炉所消耗的蔗渣的减少,工厂可以预期过程收益的增加。然后提高“ B”离心性能,以观察连续锅中“ B”质量的更稳定晶体尺寸变化的效果是否会改善工厂性能。发现“ B”离心性能的改善不如“ A”和“ C”沸腾中使用的较低过饱和度值带来的性能改善显着。

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