共查询到20条相似文献,搜索用时 15 毫秒
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从生产实际角度,探讨了PET产品主要品质指标的影响因素,如色值、端羧基值、二甘醇值及特性黏度等受温度、压力、原料配比、添加剂品质等的影响情况。 相似文献
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Wenhao Pu Changsui Zhao Yuanquan Xiong Cai Liang Xiaoping Chen Peng Lu Chunlei Fan 《Chemical engineering science》2010,65(8):2500-2512
A kinetic–frictional model, which treats the kinetic and frictional stresses in an additive manner, was incorporated into the two fluid model based on the kinetic theory of granular flow to simulate three dimensional flow behaviors of dense phase pneumatic conveying of pulverized coal in horizontal pipe. The kinetic stress was modeled by the kinetic theory of granular flow, while the friction stress is from the combination of the normal frictional stress model proposed by Johnson and Jackson [1987. Frictional–collisional constitutive relations for granular materials, with application to plane shearing. Journal of Fluid Mechanics 176, 67–93] and the modeled frictional shear viscosity model proposed by Syamlal et al. [1993. MFIX documentation and theory guide, DOE/METC94/1004, NTIS/DE94000087. Electronically available from http://www.mfix.org], which was modified to fit experimental data. For the solid concentration and gas phase Reynolds number was high, the gas phase and particle phase were all treated as turbulent flow. The experiment was carried out to validate the prediction results by three kinds of measurement methods. The predicted pressure gradients were in good agreement with experimental data. The predicted solid concentration distribution at cross section agreed well with electrical capacitance tomography (ECT) image, and the effects of superficial velocity on solid concentration distribution were discussed. The formation and motion process of slug flow was demonstrated, which is similar to the visualization photographs by high speed video camera. 相似文献
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Visual analysis of particle bouncing and its effect on pressure drop in dilute phase pneumatic conveying 总被引:1,自引:0,他引:1
During the pneumatic conveying of plastic pellets, it has been observed that materials with similar physical characteristics may develop substantial difference in pressure drop, whose cause is not fully understood. This experimental study focused on the dynamic behavior of the particles during conveying and its influence on pressure drop.The bouncing of the particles during pneumatic conveying in dilute phase was visually analyzed by means of a high speed video camera. The experiments included two different plastic pellets of similar size and density but different modulus of elasticity. The conveying trials were carried out in a 0.052 m I.D. aluminum pipe conveying system approximately 35 m long. The loading was controlled by an airflow control valve and a variable speed drive rotary valve. For each material, a series of tests were performed creating a matrix of six solids rates for five different air velocities. During the conveying trials a high speed video camera was used to record the actual particle motion in a horizontal section with fully accelerated flow. The videos showed significant difference in bouncing between the soft and the hard pellets. The soft pellets showed very random and intense bouncing with strong rotation, which affected the rebound considerably. In fact, some particles bounced even backwards. On the other side, the hard pellets showed significantly less bouncing and rotation.In addition to the high speed videos, in each test the pressure drop was measured in the horizontal and vertical directions. As expected, a significant difference in pressure drop was recorded for the same conveying settings when using the different materials. The pressure drop showed a close relation to the bouncing of the particles, being much higher for the soft pellets.It can be concluded that the increased pressure drop, developed by the soft polyethylene pellets, is in part due to the multiple times the particles must be reaccelerated during their transit through the conveying system. Additionally, the reduction in the average particle velocity increases the drag force. All of this resulted in up to 3-fold increase in pressure drop across the conveying line compared to the hard polyethylene pellets that showed significantly less bouncing. 相似文献
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针对单搭接接头,根据胶粘剂固化过程中的传热情况,将其温度场简化为无内热源的热传导问题,将平均换热系数看作固化温度的函数,采用集总参数法,得到胶粘剂固化过程中温度的预测公式,并用实验对公式计算结果进行了验证。运用该公式,分别讨论了固化温度、固化时间、被粘物材料属性、被粘物厚度、搭接长度、被粘物长度、胶粘剂初始温度、搭接宽度对胶粘剂固化过程中的温度影响规律。结果表明,前面5个因素对胶粘剂固化过程中的温度影响较大,后面两个因素基本无影响,当搭接长度相同,且与被粘物长度比值小于0.3时,被粘物长度也基本无影响。 相似文献
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《化学工业与工程技术》2016,(6):39-45
介绍了10万t/a低压焦炉煤气制甲醇装置的工艺流程,采用C307铜基甲醇合成催化剂。结合实际生产数据,分析了影响甲醇产率的主要因素,包括原料气(焦炉气)气量、压力、温度、空速、氢碳比、催化剂的毒物以及设备性能。生产操作和经验表明,提高甲醇产率需要多因素综合考虑,在气量一定的条件下,温度与压力波动越小,甲醇产量越高;根据动力消耗和催化剂生产强度,空速一般控制在4 000~20 000 h-1;在入塔气中φ(CO2)一般控制在2%~5%,对甲醇合成有利;硫化物、氯化物以及羰基铁等金属毒物必须有效脱除,以提高甲醇合成产率,并延长催化剂使用寿命;通过提高设备性能,可以保持生产的稳定性,提高甲醇产量。 相似文献
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以聚氨酯丙烯酸酯(PUA)为基体、甲基丙烯酸-β-羟乙酯(HEMA)为活性稀释剂、异丙苯过氧化氢(CHP)为引发剂、N,N′-二甲基苯胺为促进剂、糖精为助促进剂、二苯甲酮(BP)/叔胺为光引发剂和对苯二酚为稳定剂,采用双引发体系和双固化[UV(紫外光)、厌氧固化]体系制备PUA基UV厌氧胶。通过单因素试验法优选出制备UV厌氧胶的最佳工艺条件。结果表明:当w(HEMA)=20%、w(CHP)=2%、w(光引发剂)=3.0%、w(N,N′-二甲基苯胺)=w(糖精)=0.8%和w(对苯二酚)=0.06%时,UV厌氧胶的综合性能良好,其光固化定位时间为8 s、剪切强度超过5 MPa。 相似文献
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The transportation of particles along pipes or ducts using an imposed gas flow is known as pneumatic conveying. The type of granular flow in such systems is strongly dependent on the imposed gas flow rate, and can be categorised by a distinct set of modes. These modes range from dilute flow, where the grains are entirely suspended in the gas, to moving dunes and slug flow, in which the bore of the pipe is blocked by a slow moving plug of material. Understanding the transitions between these modes is critical to the design and application of pneumatic conveying systems. Particle shape is a crucial factor in systems with gas–grain interactions but has so far been overlooked in models of pneumatic conveying. We carry out a series of simulations using the discrete element method coupled to gas flow and show that particle shape is critical to the transition between different flow modes. Particles which are spherical, or nearly spherical, transition to slug flow at high gas flow rates, whereas non-spherical particles transition instead to dilute flow. We show the lower voidage fraction in beds of non-spherical particles is crucial to explaining this behaviour. 相似文献
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龙滩坝矿段采场结构参数及地压控制数值模拟研究 总被引:2,自引:0,他引:2
龙滩坝矿段矿体的直接顶底板大多为铝土页岩和黏土岩,顶板稳固性较差,有必要对开采过程中的采场稳定性进行模拟分析。采用3D-σ数值模拟软件建立三维模型,设计了直接顶板下不同采场跨度、切顶后不同采场跨度、留点柱等采场结构形式,对各种采场结构下矿岩的应力、位移、塑性区和安全率的分布进行了分析,结果表明:因矿体直接顶板稳定性较差,采场跨度对顶板稳定性的影响较大,应将采场跨度控制在6 m左右,才能保证开采过程中的顶板稳定;通过对切顶方案的模拟分析,认为将稳定性较差的直接顶板切除后,在间接顶板下采场跨度能达到15 m左右;根据模拟结果并结合现场实际情况,采场应预留3 m×3 m的点柱,点柱间矿块的跨度宜控制在6 m,以保证采场直接顶板的稳定。 相似文献
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In many industries particulate materials are conveyed pneumatically, and it is both important and challenging to measure the mass flow rate of solids in a gas-solid mixture online.In this article we present some results from experiments carried out on a semi-industrial pneumatic conveying system located at the Department of Powder Science and Technology, Tel-Tek in Porsgrunn, Norway. We have successfully calibrated a regression model which relates the pressure distributions along the pipeline to the mass flow rate of powder. The method for mass flow rate estimation presented in this paper is based on multivariate calibration (chemometrics).Twenty-one pressure transmitters are distributed along the entire length of a pneumatic conveying system. The pressure samples from all transmitters constitute axial pressure distribution signatures, which in this study are used to calibrate a Partial Least Squares Regression model. When the Partial Least Squares Regression model is properly calibrated and validated, the model can be used to predict powder mass flow rate directly from new pressure signatures in the pneumatic conveying system used, under the same conditions of pressure and air flow.The results show that it is not necessary to use all the pressure transmitters available to predict mass flow rate. This paper presents promising results using only 5 pressure transmitters. Pressure transmitters are inexpensive, reliable and easy to use, and are widely used in the industry. This method has been tested with different values of pressure and air flow rates, with equally promising results. All prediction results are validated with independent data. 相似文献
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Duan Feng Bao-Sheng Jin Ya-Ji Huang Bin Li Yu Sun Yiming Wu Ming-Yao Zhang 《Korean Journal of Chemical Engineering》2010,27(6):1707-1714
High temperature preheated air and steam as gasifying agent and coal gasification was performed in a pressurized turbulent
circulating fluidized bed (CFB) gasification pilot plant to investigate the pressurized gasification process and estimate
its potential. Within the scope of this paper this test facility as well as its operation behavior was described. Furthermore,
the parameter pressure has been investigated regarding its influence on the syngas composition and was presented and discussed
in the following. The results show that the gasification quality is improved at higher pressure because of the better fluidization
in the reactor. Coal gasification at a higher pressure shows advantages in lower heat value and carbon conversion. With the
gasifier pressure increased from 0.1MPa to 0.3MPa, the gas heating value is increased by 15%. Increasing the gasifier pressure
would increase the carbon conversion from 57.52% to 76.76%. Also, the dry gas yield and efficiency of cold gas increase little
with the increase of the gasifier pressure. The operating parameter of pressure exists at optimum operating range for this
specific CFB coal gasification process. 相似文献