会议论文ei检索查询(共7篇)
会议论文ei检索查询(共7篇)厕所里跳高
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篇一：什么样的会议论文能够被SCI或者EI检索什么样的会议论文能够被SCI或者EI检索！（转载）管理提醒: 本帖被 kidy008 从新人展示移动到本区现在检索很多，包括SCI，SCIE，EI，ISTP，ACM。关于哪些会被检索，很多人关注，写个短文供大家参考，当然不保证绝对正确，基本都差不多。 1.SCI检索 SCI检索包括SCI的3500多个期刊，大部分都是很著名的刊物，国内的e文刊物只有科学通报，中国科学，《计算机科学技术学报》（英文）等寥寥几种被SCI检索。一些非常著名的会议可能会被SCI检索，但事先一般都会被某个刊物出版（一般为springer的）然后再被检索。查询自己论文是否被SCI检索可以到在图书馆主页里面的：Web of Science Proceedingsfull fill the esntial function, stress the shape beauty, and saving ater. The quality of the sanitary implement has been requested to include exact size tolerance, fine external appearance, physics function, flushing function etc. Flushing function is the ability that the bedpan ejects filth, ashes it clearly hile controlling the amount of ater. Without question, flush function is one of the uppermost functions. According to the flushing ay, bedpan can be divided into ash-don type, siphonic type and ejecting siphonic type. Wash-don bedpan rush out filth by the impact of the ater, the poer is decided by potential energy of the ater in tank subtracts losing energy. Siphonic bedpan?s flush poer primarily relies on siphonic poer. III. THE STRUCTURE DESIGN OF SIP
HONIC BEDPAN?S FLOW CHANNEL As mentioned above, under the condition of piping ater-filled, hatever means e adopt, it ill not produce the siphonic phenomenon if air is interfud. So e should make sure that the piping ction dimension is appropriate, as figure 1 shos, the diameter of D-E gment is degressive. According to the statics and hydromechanics theories, hile the fluid in piping flos
stably, the physical volume flux is constant at any ction of the pipe. So the smaller of the pipe ction, the higher of the current velocity of the fluid. So the diameter change could result in the ater velocity change in the D-E gment. Figure 1. The structure design of siphonic bedpan?s flo channel Thus at the beginning of the siphonic bedpan?s flo channel, the flushing velocity of the ater being higher and higher, form the E-F gment in advance, expedite siphonic process, reduce the amount of ater, attained the purpo of saving ater. The D-E gment is rising, and its ction diameter is generally among 55-65 mm. The ability of rushing out filth ill be eakend ith larger diameter, the result may increa ater amount. While the drainage amount in forepart ill be influenced ith smaller diameter, it ill cau the ater surface rising, and result in siphonic phenomenon later. The E-F gment is a hump gment, its perfect ction diameter generally among 45-55 mm. The F-G gment is a increasing gment, the diameter is being bigger from small, and the ction is being la信息管理与信息系统考研方向
毛豆肉丝风湿症状rge, it ill loer gment?s the current length increa, velocity of in the addition fluid, make make siphonic siphonic phenomenon keep more time, And its ction diameter is generally among 55-60 mm.IV. THREE-DIMENSIONAL STEADY NUMERIC SIMULATION FOR FLOWING IN BEDPAN Bedpan?s geometrical modeling is the most plicated in sanitary implements, its CAD model include plicated surface and characteristics, the may result in many difficulties during the numeric simulation and influence the result. Considering the siphonic bedpan?s hole flo channel as puting area, and the difficulty to t up the CAD model in ADINA, so this paper make u of Pro/E to conduct the parameterization model of the siphonic bedpan. The ater arp is 200 mm high, and the pipe diameter in the largest ction is 80 mm. Then the model
is imported into ADINA8.3 through IGES data format. In ADINA, e still need to predigest the physics model before adding load and boundary conditions. Detailed information is as follos: Load: velocity method is defined such a volume fraction F, defining the value of the point having fluid as 1, the value of the point having no fluid as 0. Thus, in a mesh unit, the F average value reprents the a that fluid contained the unit. If the average value is 1, the mesh is filled ith the fluid, if the average value is 0, then for empty mesh. If the value is beteen 0 and 1, the mesh is free surface mesh. So it has advantages of easy realization, small calculation quantity, high-precision etc, and can handle ple
x nonlinear problem such as free surface folding, free surface filling ater etc. When the model involves flo theories of the to phas or multi-pha, it introduces the single fluid model to solve problem. Namely, in the ater-air to pha flo field, ater and air obey the same team momentum equation. In the puting area, each controlling volume is filling ith ater and air, and their volume fraction?s addition should be 1, namely, a?aa?1 Among above, ?a? denotes the volume fraction, subscript and ?a? denote ater and air respectively. Once the ater and air?s volume fractions are knon, all their unknon quantity and characteristic parameter can be denoted by average volume fraction. Tracking the ater-air interface can be solved by nether concutive
equation. ?a?t ?Va?0 Thereinto, ?V? denotes velocity vector.
shortlistB. Boundary conditions The material property and the boundary conditions are as follos: Gas pha is air, and its density is 1.293 kg/m3, viscosity is 1.7894×10-5 kg/Flushing proces The figure 4 shos floing field distributions at different moment. Figure 4. Distributing of flo at different moment by simulation for the variational ction bedpan In the figures
above, areas in red colour reprent ater, areas in navy blue reprent air, other colours reprent the mixture of ater and air. Contrasting the flo field distribution of the constant ction bedpan to the
食字成语variational ction bedpan, e ill found, to the constant ction bedpan, pipe?s tiptopduring hile 0-5s, to ater the variational caput hasn?t ction gotten bedpan, across ater the caput has already gotten across during 0-1s and in 5.6 s, ater becau in hen the arp the ater has floed caput out got pletely. across the pipe?s This mainly tiptop, the siphonic phenomenon happens. Water arp?s outflo increas largely. This makes ater level drop rapidly and reach loest level in arp, and then the siphonic phenomenon stops, ater velocity bees loer, ater that has not gotten across the pipe?s tiptop start to turn back, and finally bee level off. 2) Pressure distribution The figure 5 shos pressure distribution at different moment for the variational ction bedpan. In the folloing figures, to the constant ction bedpan, the minus pressure is -695.4 Pa, hile to the variational ction bedpan, the minus pressure is -1733 Pa, this difference shos the strong function of siphon. Figure 5. Pressure distributing at different moment for the variational ction bedpan 3) Velocity distribution As the figure 6 shos, velocity for the variational ction bedpan is averagely larger than the velocity for the constant ction bedpan, conquently, it provide effective gist for variational ction bedpan, it can easily achieve effectively flushing aim pared to the constant ction bedpan. Besides, it indirectly indicates that the variational ction bedpan can easily achieve the function of saving ater. Figure 6. The velocity distribution of the to kind ctions bedpan pipe VI. CONCLUSIONS This paper studied on the structure optimization of the siphonic bedpan?s flo channel, recurring
to finite element softare ADINA, three-dimensional steady flo numeric simulation of ater floing in bedpan is carried out, the VOF analysis on siphonic bedpan?s flushing process has also been carried out. The results can help technics designers find out the disfigurement esntially, enhance the precision in the porcelain sanitation field. Further more, it ill shorten the exploiting time and expen of the ne product consumedly, bring remarkable economic benefit to producing enterpri. ACKNOWLEDGMENT America The preferred spelling is ithout an “e” of the ord “acknoledgment” in after the “g”. Avoid the stilted expression, “One of us thanks . . .” Instead, try “R.B.G. thanks”. Put applicable sponsor acknoledgme nts here; DO NOT place them on the first page of your paper or as a footnote. REFERENCES Yue bangguo, “Talking about bedpan?s flushing filth function and saving ater,” Chinaare, 2001 Wu ziniu, The basic elements of puting hydromechanics. Beijing: the Science Press. 2001. 1-8. Hong fangen, “Kinetic object round free surface floing field value simulation and experimentation rearch,” Doctor Degree thesis. Wuxi, Jiangsu, China: Chine atercraft science rearch center. 2001.4. C.W. Hirt, B.D. Nichols. Volume of fluid method for the dynamics of free boundaries. Journal of Computational Physics, 1981, 39:201-225. Lin huzong, Phantasmagoric floing science-multipha hydromechanics. Beijing: the book concern of Qinghua University, Guangzhou: the book concern of Jinan University. Wang youcheng, Shao min, The theory and numeric method on finite element analysis. Beijing: the book concern of Qinghua University, 1997. 篇四：论文怎样写才能被EI检索论文怎样写才怎么开电脑
能被EI收录 2016年06月12日星期五上午 10:15 从2002年起《吉林大学学报0253-4827 Applied Mathematics and Mechanics 0890-5487 China Ocean Engineering 1004-5341 China Welding
