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基于实际工程应用,采用CFD软件,建立了内管为螺纹管的新型螺旋套管式换热器的三维实体模型,并使用管程流体与壳程流体耦合计算的方法进行模拟计算,重点分析了螺纹槽高和槽距等结构参数对管程流体流动与传热特性的影响。结果表明:螺纹的扰流和导流作用,改变了管程螺旋通道横截面上的二次流结构,除在横截面外侧区域形成一个不规则主涡外,还在截面内侧区域的近螺纹处产生了大小不一的附加涡旋。主涡和附加涡共同作用加剧了壁面和中心区流体的热质交换,强化了换热效果。在研究范围内(Re=8 000~40 000),螺旋套管式换热器内管采用螺纹管与内管采用光管相比换热效果提高了约36%~143%。螺纹槽高及槽距对管程流体传热影响较大,Nu和f随槽高的增加而增加,随槽距的增大而减小。 相似文献
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利用计算流体力学软件对内管为螺纹管的螺旋套管换热器壳程流体的湍流流动和换热性能进行了数值模拟。通过与内管为光管的研究结果对比,揭示了内管为螺纹管时壳程流体的速度场和温度场分布,研究了雷诺数、槽高对壳程流体湍流流动及换热性能的影响,并利用场协同原理初步揭示了螺纹复合螺旋流动强化流体换热的机理。结果表明,螺纹内管的螺纹凸起对螺旋套管换热器壳程流体的扰流和导流作用明显,在研究范围内(Re=10000~24000),内管为螺纹管的螺旋套管换热器壳程流体的传热效率较内管为光管的模型最大提高了22.1%;结构参数相同时,随着Re增大,螺旋套管换热器壳程流体的Nu逐渐增大,阻力系数f逐渐减小,综合评价因子Ψ逐渐减小,在研究范围内,Nu最大增加了85.6,f最大减少了0.008,Ψ从1.35减小至1.18。当Re一定时,当量高度h’增大,f逐渐增大,Nu先增大后减小。由场协同原理分析得出,h’=0.220时,在螺纹凸起扰流和导流的作用下壳程流体的温度场与速度场协同性能较好,综合评价因子Ψ最大,螺纹的优化当量高度h’宜取约0.220。 相似文献
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螺旋槽管与折流栅组合的高效水冷器的传热和阻力特性与其管、壳程的结构因素密切相关,本文就螺旋槽管槽深对水冷器管、壳程传热与阻力特性的影响进行了实验研究.结果表明:壳程流速变化对水冷器传热系数的影响更加明显,即壳侧热阻相对较大,强化传热应以强化壳侧换热为主要目标;螺旋槽管槽深对水冷器传热系数的影响很大,应在实际工程设计中确保实际槽深符合设计要求;槽深越深,管壳程阻力也相应增加,即传热的强化是以阻力增加为代价.根据实验结果还得到了不同结构水冷器的管、壳程换热与阻力计算关联式. 相似文献
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流体在螺旋隔板换热器的壳程类似于塞状流流动,几乎没有返混和流动死区.在相同压降下,其传热系数比普通的弓形隔板换热器高得多.以润滑油作为实验介质,研究了润滑油在螺旋隔板单管换热器的壳程传热和压降性能,并与光滑管进行了性能对比.采用Wilson图解法分别分离出了螺旋隔板花瓣管和光滑管单管换热器的管程传热系数,并计算出各自的壳程传热系数,壳程传热系数相对误差为±3%.实验结果表明,在相同Reynolds数下,螺旋隔板花瓣管单管换热器的Nusselt数和压降Δp分别是螺旋隔板光滑管单管换热器的2~2.7倍和1.3~1.4倍.与螺旋隔板光滑管单管换热器相比,螺旋隔板花瓣管单管换热器的传热性能的提高远高于压降的提高,证明在螺旋流条件下,花瓣管具有很好的传热强化性能. 相似文献
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考虑壳程流体和管程流体的耦合传热,对套管式换热器管程流体的流动特性和换热特性进行数值分析。对比不同模型的管程流体的Nu和f,发现了螺纹管传热的优越性,结合管程流体速度场、温度场的细观信息,揭示了管程流体的换热性能和流动特性,并分析了不同流体介质对其管程换热效果的影响。结果表明:内管采用螺纹管时,螺旋套管式换热器管程流体的换热性能明显优于光滑内管,在研究范围内,内管采用螺纹管的Nu是采用光管的1.76~1.9倍,流体受离心力、螺纹扰流和螺旋槽导流的复合作用,强化了管程流体的传热。在同一雷诺数下,30号透平油的Nu最大,约为空气的3.8~5.01倍,然后依次是水、水蒸气、空气。 相似文献
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Solid solutions of diphosphates of zinc and copper and of zinc and cobalt were synthesized from mixtures of pure diphosphates at temperatures up to 1000°C. Their X-ray diffractometry patterns varied continuously from one end member to the other. Solid solutions of orthophosphates of composition Zn3−x Cox(PO4 )2, with x = 0.4–1.6, were formed at temperatures up to 950°C; all exhibited the structure of γ-Zn3 (PO4 )2. Solid solutions of orthophosphates of composition Zn3−x Cux (PO4 )2 exhibited more-complex behavior. At 1000°C and copper contents of 20–80 mol%, a phase that is related to Cu3 (PO4 )2, termed here the "ε-phase," predominated. At 850°–950°C and in the region from 20 mol% to ∼33 mol% of copper, the solid solutions (the "η-phase") adopted the structure of graftonite. At 800°–900°C and 10–15 mol% of copper, the solid solutions exhibited a new structure (the "δ-phase"), which we found to be related to the mineral sarcopside. At temperatures 950°C, the solutions that contained 5–15 mol% of copper (the "β-phase") had the structure of β-Zn3 (PO4 )2, whereas at 800°–850°C, solutions with 5 mol% of copper (the "-phase") exhibited the structure of γ-Zn3 (PO4 )2. Attempts to synthesize Cu+ ZnPO4 and Cu+ Cu2+ Zn3 (PO4 )3 were unsuccessful. 相似文献
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为了提高油田的生产效率,设计最佳的油气集输处理的工艺流程,更好地完成油气水分离处理的任务。对油气集输工艺技术进行优化,发挥高效油气水分离处理设备的优势,提高油气水处理的质量,保证油气集输工艺顺利实施,获得最佳的油田产量外输。 相似文献
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建设创新型国家是我们中华民族的历史责任。“自主创新、重点突破、支撑发展、引领未来”的16字方针应当成为我们未来创新活动的指南。建设创新型国家把自主创新放在首位,并提出了引领未来的高标准要求。钢铁科技创新必须突出重点,抓住创新成果产业化这个关键,支撑起行业和国民经济的发展。 相似文献
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相比已经完善丰富的开采和勘探技术,油气的运输以及储存却仍然存在不足之处。我国对能源安全提出更加严格要求的同时,对区域经济的发展规划也有足够重视。因此,保障油气管道的安全则成为了我国能源安全战略的重中之重。在阐释油气管道现阶段在储运安全保障技术发展状况的基础上,分析了现存的问题及解决问题的手段,并指出未来可能使用的目标策略,为今后研究者提供一定程度上的借鉴经验。 相似文献
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膜的污染和劣化及其防治对策 总被引:25,自引:0,他引:25
较为系统地介绍了膜污染和劣化的定义和特点,因膜污染和劣化而造成的膜性能变化,以及如何预防、减少或清除膜污染和劣化的一些通用方法。 相似文献
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James L. White David G. Salladay David O. Quisenberry Donald L. MacLean 《应用聚合物科学杂志》1972,16(11):2811-2827
Gel permeation chromatographic (GPC) and thin-layer chromatographic (TLC) studies of polystyrene, polybutadienes (BR), and their copolymers (SBR) have been carried out. GPC primarily separates them on the basis of molecular size, and TLC, on the basis of composition. Methods of obtaining absolute molecular weight distributions for BR and SBR based upon variations of the Strasbourg Universal Calibration procedure are described. In particular, [η]–M relationships in both the GPC solvent (THF) and in a second solvent (toluene) were used; in addition, results of statistical mechanical calculations for \documentclass{article}\pagestyle{empty}\begin{document}$\overline {s^2 }$\end{document} (based on the assumption of negligible steric hindrance and freely rotating bonds) were applied. An experimental comparison of these methods was carried out, and use of the [η]–M relationships for both solvents was found to give satisfactory results. The predictions of the statistical theory were too low. A detailed study of polymer–solvent–gel interaction in the GPC unit was made through investigation of ternary phase equilibrium in the (polystyrene)–THF–(polymer) system. The polymers studied included BR and SBR with varying styrene contents. Experimental techniques for TLC separations of BR, SBR, and polystyrene according to the composition are described. 相似文献