喷射式并流填料塔板的研究

Experimental study on hydrodynamics and mass transfer efficiency of jet coflow packing tray (JCPT) was conducted in a φ285 mm column and a φ200 mm column, respectively. Compared with new vertical sieve tray which has been applied in the petrochemical industry since 1968, the JCPT has lower pressure drop, higher capacity and higher mass transfer efficiency, and seems promising in commercial application.     

喷射式并流填料塔板流体力学和传质性能

提出一种新型高效塔板——喷射式并流填料塔板（ＪＣＰＴ）,介绍１２００ｍｍ冷模塔流体力学实验结果和２００ｍｍ热模塔传质效率,给出了适用于工业设计性能参数的计算关联式。通过与新垂直筛板（ＮＶＳＴ）的比较表明,ＪＣＰＴ具有雾沫夹带小、处理能力大、塔板效率高等特点,是一种具有广泛应用前景的新型高效塔板。     

气液并流旋喷塔板的流体力学性能

结合新垂直筛板塔(NVST)和旋流板的特点提出了一种新型塔板——气液并流旋喷塔板，以空气水体系测试其流体力学性能。实验表明这种塔板的压降比NVST塔板减小10％20％，雾沫夹带上限比NVST塔板低，这些特性将使其比NVST塔板有较大的处理能力；而大提升量则保证了其有较高的传质效率，是一种很有应用前景的塔板。     

立体并流板的流体力学和传质性能

新型立体连续传质液体并流塔板是将LLC-Tray与两种并流流型相结合开发而成的新型塔板。通过实验测定了新型塔板的干、湿板压降,雾沫夹带,漏液等流体力学性能和传质性能,并进行关联得到了相应公式。结果表明,新型塔板板压降较低,雾沫夹带较低,液体处理量相对LLCT提高30%。     

大型塔板液体停留时间分布与板效率研究

报导在直径 2m的筛板塔实验装置中 ,用电导率连续测量系统同时测定塔板上 12个点的停留时间分布曲线及给出典型数据 ,并提出由停留时间分布曲线换算成塔板上浓度分布曲线以及计算塔板效率的方法     

双效并流立体旋液式塔板压降的实验研究

采用全新工艺流程,设计了一种新型双效气液并流吸收塔,塔内安装有改进型立体旋液式塔板。分别以空气、空气-水作为研究体系进行实验,考察了不同操作参数与塔板结构参数下双效气液并流吸收塔的干塔压降、湿塔压降以及立体旋液式塔板的干板压降、湿板压降,明确了双效气液并流吸收塔的操作参数范围。实验结果表明:立体旋液式塔板单板干板压降及湿板压降分别控制在70 Pa,180 Pa以内。在一效、二效各逆向安装3块塔板,全塔共完全安装6块塔板时,全塔压降最大,但是干塔压降及湿塔压降可分别控制在2 400 Pa,2 800 Pa以内,双效气液并流吸收塔与立体旋液式式塔板的组合在能耗及操作弹性方面优势明显。     

立体旋液式并流塔板的海水脱硫特性

引言海水烟气脱硫技术是利用天然海水的弱碱性吸收烟气中的SO2,达到净化烟气的目的[1-4]。该技术在最近四十年内已在世界范围内众多大型电厂实现工业化应用[5-6],目前,多数海水烟气脱硫系统采用ABB(即ALSTOM)公司的Flakt-Hydro工艺[7-8],以脱硫塔作为主要的吸收设备,如:喷淋     

塔板上液体混合池数与Peclet数之间的关系

提出了一个从已知的Peclet数确定塔板上液体混合池数的关联式。经计算结果比较，表明该关系式具有较高的精确度，在相同条件下，由混合池模型和扩散模型所计算的塔板效率，平均偏差为0．024％，最大偏差不超过0．40％。应用Ashley等和Eduljee的Pe-n关系式，平均误差分别为0．44％和0．29％，最大误差分别为－4．64％和1．93％。     

DJ塔板液体流动特性研究

利用光纤技术测定ＤＪ塔板的液体停留时间分布，研究板上液体的流动特性，提出简便有效的板结构改进措施，为大型ＤＪ塔板的合理设计和进一步工业应用提供参考依据。     

NS复合并流塔板提供节能利器

<正>2013年9月底,中国石油大学(华东重质油国家重点实验室开发的大通量、低压降、高效率的新型塔内件NS复合并流塔板技术,已在75座塔器的扩能改造和新建装置中应用。结果表明,仅更换塔板就可提高处理能力2倍以上,同时提高效率30%以上,节能50%以上,节省投资80%以上,解决了现有装置处理量翻番的扩量节能改造难题。塔板和填料是应用最广的蒸馏分离元件,由于     

Efficiency of dualflow trays in distillation

The mass transfer efficiencies of dualflow trays with open hole areas of 20, 28 and 37% were experimentally investigated under total reflux conditions in a 300-mm diameter distillation column using methanol-water and methanol-isopropanol systems. The results indicate that the efficiency of a dualflow tray is a strong function of the open hole area, the vapor/liquid load, and liquid properties such as surface tension and density. A fundamental model was developed to predict tray efficiency. The prediction was found to agree with the measured data to within 15.3%.     

十字旋阀塔板漏液性能

在φ1000mm的圆塔内,以空气-水为介质,对十字旋阀塔板的泄漏率进行了测试,考察了液流强度、出口堰高等因素对泄漏性能的影响,并将其与交错十字旋阀塔板、组合导向浮阀塔板和F1型浮阀塔板的泄漏率进行了对比。结果表明:十字旋阀塔板在气速超过临界阀孔气速且液流强度较小时具有很好的漏液性能,经数据关联,获得了十字旋阀塔板漏液点孔速的关联式。     

Mixed convection mass transfer studies of opposing and aiding flow in a parallel plate electrochemical flow cell

Studies of combined natural and forced convection in a vertical parallel plate electrochemical cell in laminar conditions in cases of opposing and aiding flow are reported. In an ongoing project it was necessary to identify conditions in which natural convection had no significant influence on mass transfer rates at the cell walls so that data could be validly compared with purely laminar flow computational models. For the different electrode lengths investigated, natural convection dominated at low Reynolds number and there was no Reynolds number dependence. At high Reynolds number the data approached the laminar flow solution. At intermediate Reynolds number, however, there existed a distinct region where free and forced convection were significant. At high electrolyte concentrations data did not merge with laminar flow equations until Re=1000 and low electrolyte concentration data for the large plate could not be compared with numerical predictions below Re of 250. An attempt was made to compare the data with those of other workers on combined forced and natural convection heat and mass transfer.     

Tray-to-tray method for estimation of the number of trays in gas–liquid columns in case of intensive entrainment

The paper deals with the tray-to-tray method for determining the required number of trays in gas–liquid columns in case of intensive entrainment. The equations for estimation of the tray efficiency are derived for top, bottom and intermediate trays, and they incorporate the number of gas and liquid phases transfer units, stripping factor, Peclet number of mixing and fractional entrainment. These equations can be simplified to the well-known one-parametric diffusion model explained in Bubble Tray Design Manual (1958) [Bubble Tray Design Manual, 1958, AIChE, New York] for case of negligible entrainment. The algorithm of tray-to-tray method is based on tray efficiency calculated for each tray separately and it enables the calculation of the number of required trays, starting from the bottom tray. Given example shows how the excessive entrainment decreases of the driving force of the process.     

平行流热管管内两相流动可视化实验研究

平行流热管换热器综合热管轴向高效换热和平行流换热器管外高效换热的优点,是一种新型的热管换热器。为了研究平行流热管工作机理及管内流动过程,搭建了平行流热管可视化实验台并对不同结构参数、不同加热功率和不同充注工质下的启动特性和传热传质规律进行了实验研究。实验结果表明：平行流热管工作机理复杂,并联管路内气柱和液柱在重力和不平衡压力的共同作用下进行互激振荡流动,并且管内出现泡状流、弹状流、环状流等多种流型,同时较高的加热功率和较大的管径会加剧工质在并联各管路之间的往复振荡,增加工质在蒸发段和冷凝段的扰动,提高热管的换热性能。     

顺流型溶液与空气热质交换性能

在顺流型平板降膜热质交换测试装置上对氯化锂水溶液与湿空气除湿、再生性能进行了实验研究,结合NTU-Le模型,着眼于湿空气与溶液耦合热质交换特性,获取了顺流条件下不同空气流量、溶液流量、溶液温度工况的耦合传热传质系数随运行参数的变化情况。研究结果为相关过程模型验证提供可靠数据,同时也为相关设备性能分析与计算提供重要基础数据。     

Entrance effect on mass transfer in a parallel plate electrochemical reactor

The influence of different fluid inlet types, slits or tubes, on mass transfer in a rectangular reactor was studied. Measurements of mass transfer coefficients were made using the limiting diffusion current technique based on ferricyanide ion reduction at a large nickel electrode located downstream of abrupt expansions. The overall mass transfer coefficients obtained were 3 to 13 times greater than those obtained in fully developed flows. Overall mass transfer coefficients were correlated for Reynolds numbers ranging from 400 to 3500 by a unique equation by introducing a nondimensional expansion factor defined by the ratio of the fluid inlet cross-section to that of the reactor. The correlation equation obtained was compared with literature data.     

塔板技术应用研究进展

介绍了近几年国内外开发应用的新型塔板,按气液流向不同将塔板分为3类进行概括,并对其结构特点和性能做出了评述,预测了未来塔板技术革新的方向.     

Understanding maldistribution in 3-pass trays

Understanding 3 pass trays is the key to design of 6 pass trays, such as those in the large towers expected in carbon-capture services. This paper presents a hydraulic distribution model for 3 pass trays with no liquid or vapor equalization. The model is verified by comparison with FRI's test data and with one operating tower. Our paper predicts good distribution for the 3 pass trays tested at FRI, and shows that the poor efficiencies in some of the tests were due to losing the downcomer seals and not tray maldistribution. The model predicts good distribution at maximum rates in the operating tower, but finds that at lower rates, where valves open and close, there is an extreme sensitivity of vapor distribution to small pressure drop variations. This sensitivity precludes reliable modeling of distribution in this region and may define an unstable region in the operation of 3 pass trays.