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Validation of heat transfer data for fibre suspensions in coaxial pipe heat exchangers

机译:验证同轴管式热交换器中纤维悬浮液的传热数据

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摘要

Heat transfer data obtained previously in a small coaxial pipe heat exchanger were validated using a new, larger annular-area test unit with longer calming section and axial entry flow. Water and two suspensions of long-fibre softwood Kraft pulps with fibres having different coarseness (mass/unit fibre length) values were used. Data in both systems were obtained over a range of flow rates with the fibre concentration at 0.4% and compared. Heat transfer coefficient h c was found to decrease with increasing annular gap size for both water and fibre suspension flow at equal velocities. Various fibre dimensions and fibre characteristics are also shown to vary systematically with h c at the same experimental conditions. The effect of hydrodynamic annular entry length on heat transfer and pressure loss using water and fibre suspensions (concentrations 0.2% and 0.4%) are also described. It was found that that extending the central calming extension rod made no significant difference to h c values at the low fibre concentration of 0.2%, and only small differences at the higher concentration of 0.4%. The successful validation of data from the smaller-annulus coaxial pipe heat exchanger show that the relationships among heat and momentum transfer and fibre characteristics and specific properties of paper are also valid for both heat exchangers.
机译:以前在小型同轴管式换热器中获得的传热数据已使用新的较大的环形区域测试单元进行了验证,该单元具有更长的平静段和轴向进入流。使用水和具有不同粗度(质量/单位纤维长度)值的纤维的长纤维软木牛皮纸浆的两种悬浮液。两种系统的数据都是在一定的流速范围内获得的,纤维浓度为0.4%并进行了比较。发现在相等速度下,水和纤维悬浮液流的传热系数h c随着环形间隙尺寸的增加而减小。在相同的实验条件下,各种纤维尺寸和纤维特性也会随h c的变化而系统地变化。还描述了使用水和纤维悬浮液(浓度为0.2%和0.4%)的流体动力环形入口长度对传热和压力损失的影响。已经发现,在低纤维浓度为0.2%时,延伸中央镇定伸长杆对h c值无显着差异,而在较高浓度为0.4%时,h c值差异很小。从较小的环形空间同轴管式换热器获得的数据的成功验证表明,热量和动量传递与纤维特性和纸张的特定特性之间的关系对于这两个换热器也是有效的。

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