共查询到19条相似文献,搜索用时 93 毫秒
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本文以电厂循环冷却塔塔底黏泥中分离纯化出的致垢微生物铁细菌为实验介质,利用污垢热阻动态模拟实验台,在恒定工况下(水温30℃,流速0.4 m·s-1),动态模拟了光管、缩放管、横纹管三种不锈钢典型换热器微生物污垢形成过程。在分析比较三种典型换热器传热性能的基础上,实验测试了三种换热器的污垢热阻,并对垢样成分进行了分析。结果表明:强化管(缩放管和横纹管)传热性能和抑垢能力优于光管,光管、缩放管和横纹管的污垢诱导期分别为;25 h、40 h和45 h,污垢热阻值为:6×10~(-4)m~2·K·W~(-1)、2×10~(-4)m~2·K·W~(-1)和3×10~(-4)m~2·K·W~(-1),由此表明三种换热管的传热和抑垢能力:缩放管横纹管光管。在铁细菌形成的污垢垢样成分分析中Fe元素含量最多,其次是C,表明循环冷却水中铁含量的多少是污垢形成的重要因素之一。 相似文献
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多孔介质高强度传热传质的理论研究 总被引:3,自引:0,他引:3
提出了高强加热下含湿多孔介质传热传质新模型,模型包括的水分种类齐全、水分迁移机制全面,假设条件相对较少,考虑了非Fourier传热效应和非Fick传质效应,模型通过具体的含湿量分区分析得到简化。 相似文献
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降膜结晶过程传热传质简化积分模型模拟计算 总被引:6,自引:0,他引:6
本文在对降膜结晶分离过程进行传热传质分析的基础上,建立了简化数学模型。文中按时间先后次序分成若干时间流股,并对每一流股按随体坐标自上而下对传热和传质方程进方积分,其中利用稳态充分发展的传热传质公式计算局部、即时的结晶量,进一步将不同时间流股所得结晶量叠加即得到结晶在空间和时间上的分布。文中将计算结果与所作的实验结果进行了比较,二者吻合较好。最后利用本文的计算模型进一步对广泛的影响因素进行了研究,获得一系列有益的结果。 相似文献
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中空纤维膜换热器可同时实现传质传热, 该换热器可应用于吸收式制冷系统以改善制冷性能. 为探究该膜换热器在溴化锂吸收式制冷系统的运行工况下的传热传质特性, 搭建中空纤维膜换热器性能测试实验台, 采用控制变量法探究在热侧不同入口溶液流速、温度下该换热器的传热量及膜通量变化规律特性. 结果表明: 在热流体其它参数保持不变的情况下, 中空纤维膜换热器热侧溶液的入口流速由3.05 m/s 增至3.30 m/s 时, 换热器总传热量与膜通量均随之加大, 增幅分别为16.0%和2.2%; 该膜换热器的总传热量在冷侧溶液与热侧溶液入口温差10°C 至15°C 内, 增幅达到18.9%, 而膜通量受膜两侧溶液的入口温差变化影响较小, 增幅仅3.1%. 研究表示: 温度的变化对中空纤维膜换热器的传热传质性能影响更为显著, 而流速的变化对水分子的运动影响较小. 相似文献
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Mixed Convection Heat and Mass Transfer in a Micropolar Fluid with Soret and Dufour Effects 下载免费PDF全文
A mathematical model for the steady, mixed convection heat and mass
transfer along a semi-infinite vertical plate embedded in a micropolar
fluid in the presence of Soret and Dufour effects is presented. The
non-linear governing equations and their associated boundary conditions
are initially cast into dimensionless forms using local similarity
transformations. The resulting system of equations is then solved
numerically using the Keller-box method. The numerical results are
compared and found to be in good agreement with previously published
results as special cases of the present investigation. The non-dimensional
velocity, microrotation, temperature and concentration profiles are
displayed graphically for different values of coupling number, Soret
and Dufour numbers. In addition, the skin-friction coefficient, the
Nusselt number and Sherwood number are shown in a tabular form. 相似文献
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The heat and mass transfer from a grooved tube is investigated experimentally for a falling-film flow. The experiments are conducted on a helical trapezoidal grooved tube at three temperatures of the feeding water: 30°C, 35°C, and 40°C. The Reynolds number (Re) of the air ranges between 1,500 and 3,500. Nusselt number (Nu) is expressed as a function of the Prandtl number (Pr), Re for air (Rea), Re for water (Rew); Sherwood number (Sh) is expressed as a function of the Schmidt number (Sc), Rea, and Rew, and the correlation coefficients are determined. 相似文献
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In this work, the heat transfer characteristics of supercritical pressure CO2 in vertical heating tube with 10 mm inner diameter under high mass flux were investigated by using an SST k-ω turbulent model. The influences of inlet temperature, heat flux, mass flux, buoyancy and flow acceleration on the heat transfer of supercritical pressure CO2 were discussed. Our results show that the buoyancy and flow acceleration effect based on single phase fluid assumption fail to explain the current simulation results. Here, supercritical pseudo-boiling theory is introduced to deal with heat transfer of scCO2. scCO2 is treated to have a heterogeneous structure consisting of vapor-like fluid and liquid-like fluid. A physical model of scCO2 heat transfer in vertical heating tube was established containing a gas-like layer near the wall and a liquid-like fluid layer. Detailed distribution of thermophysical properties and turbulence in radial direction show that scCO2 heat transfer is greatly affected by the thickness of gas-like film, thermal properties of gas-like film and turbulent kinetic energy in the near-wall region. Buoyancy parameters Bu < 10−5, Bu* < 5.6 × 10−7 and flow acceleration parameter Kv < 3 × 10−6 in this paper, which indicate that buoyancy effect and flow acceleration effect has no influence on heat transfer of scCO2 under high mass fluxes. This work successfully explains the heat transfer mechanism of supercritical fluid under high mass flux. 相似文献
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为定量研究多组分系统在多孔介质内传质过程中组分之间的交互作用现象,本文基于Maxwell-Stefan模型对CH4/Ar/H2混合气体在单个直孔道内的纯扩散过程和C2H6/C3H8/N2混合气体在活性炭上的吸附扩散过程进行了模拟,定量地描述和分析了多组分系统中组分之间在传质过程中的交互作用。研究表明:对于扩散过程,组分之间的交互作用表现为大分子对小分子的拖带;对于吸附过程,这种作用表现为强吸附质能够替代已被吸附在吸附剂表面的弱吸附质;主体扩散为主要的传质形式。 相似文献
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撞击流中颗粒碰撞传热理论模型研究 总被引:1,自引:0,他引:1
建立了考虑颗粒接触面导热的颗粒碰撞传热模型,相应完善了气固两相撞击流理论模型,并对不同条件的撞击流干燥过程进行了模拟。计算结果与实验结果非常吻合,从而验证了所建模型的正确性。本文还分析了颗粒碰撞传热、加料方式以及喷嘴间距对撞击流干燥性能的影响规律。结果表明:在本文所涉及的撞击流干燥过程中,颗粒碰撞传热对干燥性能的影响并不明显;单边加料时颗粒物料的降水幅度及撞击流装置的干燥强度都明显大于双边加料的工况;喷嘴间距较大时,物料的降水幅度及装置的干燥强度均较大。 相似文献
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采用格子Boltzmann方法,基于孔隙尺度,对填有均匀介质的复合方腔顶盖驱动双扩散混合对流及流固共轭传热、吸附进行数值模拟.在孔隙率ε=0.79,普朗特数Pr=0.7,格拉晓夫数Gr=104和路易斯数Le=1.0时,就不同浮升力比(-100≤Br≤100)和吸附率常数(0.001≤k1≤0.005)对方腔内部热质传输的影响进行比较.给出流线、等温线、等浓度线、平均努赛尔数Nuav、舍伍德数Shav和吸附量等.结果表明Br通过改变介质所处流场的浓度分布影响吸附,而k1的增加显著地提高吸附效率和吸附能力. 相似文献