离心式挤出机结构创新与固体输送及增压机理的研究
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摘要
离心式挤出机是一种新型聚合物加工机械,其主要创新点为将离心力场应用于固体输送及增压。本文以离心式挤出机的工作机理为主线,对离心式挤出机结构设计、工艺参数、固体输送增压机理、固体输送压力分布状态的数值模拟、固体输送增压机理的实验验证等多个方面进行探索和研究。
     本文全面地剖析了离心式挤出机的输送增压、圆盘熔融、计量挤出工作机理,提出了离心式挤出机的总体设计。并详细讨论了离心式挤出机的主要结构,其中包括主机、传动系统、控制测量系统、加热冷却系统、以及密封结构。同时,本文也阐述了离心式挤出机主要工艺参数以及结构参数的设计,其中包括离心力场、工作转速、剪切速率、传热能力、密封能力以及圆盘熔融段法向应力等。另外,由于离心式挤出机属于高速旋转机械,本文对其临界转速也进行了有限元数值分析。
     除上述离心式挤出机设计问题外,本文着重研究了离心式挤出机聚合物输送增压机理,建立了在离心力场的作用下聚合物输送压力分布的数值模型,得到转鼓中聚合物输送压力分布方程;同时,利用固体输送压力分布方程,分析了转鼓结构几何参数、聚合物物料属性、转鼓材料以及操作工艺条件对转鼓中聚合物输送压力分布的影响。
     数值分析研究表明,选取适当的转鼓锥角α、半径R_n以及转鼓材料,同时针对不同聚合物,选择不同的转速n可以得到预期的固体输送压力;提高转鼓内壁的表面光洁度、对转鼓内壁进行表面涂层处理,可大大减少摩擦,可将原本浪费的摩擦上的能量用以提高聚合物固送压力。
     根据离心式挤出机的聚合物输送机理,设计出聚合物输送增压实验装置,用以对离心式挤出机输送压力数值分析结果进行实验验证。实验测试结果表明,实验数据与数值分析数值吻合较好,证明了离心式挤出机固体输送压力分布数学模型具有合理性以及预测性。
     离心式挤出机将离心力场引入到聚合物加工领域,本研究取得的阶段性成果不仪可为该机的开发和应用提供理论依据,而且会对其它相关领域的聚合物加工技术与理论的研究产生辐射作用。
Centrifugal extruder is a new type of polymer processing machine, used centrifugal force field in polymer processing. In this paper, four aspects of the equipment--- the innovation technology of centrifugal extruder, solid conveying mechanism, mathematical simulate of the distribution of solid conveying pressure and experiments are studied for the development of centrifugal extruder.
     It is introduced comprehensively that solid conveying, melting, mix and metering of centrifugal extruder. The innovation technology of centrifugal extruder is introduced, including main machinery, drive system, control and measuring system, heating-cooling system and seal system. And the paper lists the parameters of main operation and machinery on centrifugal extruder. There are centrifugal field, rotate speed, power, shear rate, normal stress difference in disk stage seal capability and heating transfer. Because the centrifugal extruder is a kind of the rotation equipment with high speed, the analysis of vibration is made by ANSYS software.
     Polymer solid conveying processing of centrifugal extruder is studied. Built mathematical simulation modal of the conveying pressure distribution, the equation expressed the conveying pressure distribution can be obtained. Otherwise, the effects of pressure distribution, including rotor drum, polymer physical properties and operational conditions on the conveying pressure distribution have been analyzed.
     By studied, the conclusions are gotten that by reasonable rotor drum and rotation speed, the centrifugal extruder can established the necessary solid conveying pressure; the main geometrical parameters of the rotor drum influencing on the solid conveying pressure are the diameter and slope angle of rotor drum; the friction factors between the polymer and the wall of the rotor drum or dish can influence on the solid conveying pressure distribution; the physical properties of polymer influencing on the solid conveying pressure distribution are the density and friction factor of the polymer.
     The equipment is designed for validating the mathematical model for calculation of the solid conveying pressure. The results of the experiments show a good coincidence with the theoretical predicts.
     All the preliminary investigations can provide theoretical basis for application and development of this type of polymer processing machine.
引文
[1]胡世华,刘士国.当前我国塑料机械的现状与市场发展对策分析[J].商场现代化,2006,457:287
    [2]朱复华.挤出理论及应用[M].北京:中国轻工业出版社,2001.69-171
    [3]江波.我国塑料挤出成型机及辅机的发展现状与技术水平分析(上)[J].橡塑技术与装备,2002,28(10):1-5
    [4]罗世华.最近的挤出成型动向[J].塑料,1990,19(2):46-4
    [5]黄汉雄.两种取代螺杆的挤出新方法[J].塑料科技,1988,63(3):30-33
    [6]张沛,李勇.无螺杆挤出机[J].塑料加工,1992,1:32-34
    [7]吴宏武,周南桥,何和智,瞿金平.电磁动态塑化挤出机性能的研究[J].中国塑料,1996.10(1):53-58
    [8]D.C.Jones,H.F.Stripling.Extrusion without screws:the rotary alterative[J].Plastics Engineering,1987,43(6):49-52
    [9]R.F.Westorer.A Hydrodynamics Srewless Extruder[J].Secience Plastics Engineering,1962,18:1473-1480
    [10]彭响方,瞿金平.聚合物动态成型技术的研究及进展[J].高分子材料科学与工程,1999,15(5):8—12
    [11]吴大鸣,刘颖,李晓林.精密挤出成型原理及技术[M].北京:化学工业出版社,2004.5-8
    [12]王兴天.挤出机的现状与发展[J].塑料科技,1994,99(1):41-51
    [13]董俊华.卧式螺旋离心机的转鼓与螺旋输送器的有限元分析,[D].北京:北京化工大学,2004
    [14]肖云峰.卧螺沉降式离心机振动分析与物料输送功率计算的研究[D].北京:北京化工大学,2002
    [15]董俊华,刘忠明,范德顺.卧螺离心机双锥角转鼓结构的有限元分析[J].北京化工大学校报,2004,31(4):99—102
    [16]Edward Dintwa,Paul Van Liedekerke,Robert Olieslagers,Engelbert Tijskens,Herman Ramon.Model for Simulation of Particle Flow on a Centrifugal Fertiliser Spreader[J].Biosystems Engineering,2004,87(4):407-415
    [17]Xuesong Wang,Nick J.Miles,Sam Kingman.Numerical study of centrifugal fluidized bed separation[J].Minerals Engineering,2006,19:1109-1114
    [18]Douglas s.Chisholm.Processing of plastic[P].USP:3,358,323,1967-12-19
    [19]Douglas s.Chisholm.Centrifugal extrusion employing eddy currents[P].USP:3,483,281,1969-12-9
    [20]Douglas s.Chisholm.Centrifugal extrusion employing eddy currents[P].USP:3,912,799,1975-10-14
    [21]Douglas s.Chisholm.Method of devolatilization of synthetic resinous thermoplastic materials[P].USP:3,409,712.1968-12-5
    [22]Masao Konishi.Method and device for producing short fibers[P].USP:6,783,708 B2.2004-08-31
    [23]Erich Lenk.Spinning centrifuge[P].USP:5,075,063.1991-12-24
    [24]Kari Kirjavainen,Jvri Jarvenkyla.METHOD FOR MAKING A PRODUCT TO BE EXTRUDED,AND AN EXTRUDER[P].USP:6,187,237 B1.2001-2-13
    [25]Kari Kirjavainen,Jvri Jarvenkyla.EXTRUSION METHOD,EXTRUDER AND TXTRUDED PRODUCT[P].USP:6,203,740 B1.2001-5-20
    [26]Kari Kirjavainen,Jvri Jarvenkyla.EXTRUDER WITH SUPPLY CONDUIT FOR SUPPLYING EVEN FLOW OF MATERIAL[P].USP:6,086239.2000-7-11
    [27]Esko Hippelainen,Kari Kirjavainen,Jvri Jarvenkyla.METHOD FOR PRODUCING HOMOGENEOUS MATERIAL WITH AN EXTRUDER,AN EXTRUDER,AND A MULTILAYER PLASTIC PIPE[P].USP:6,073,657.2000-1-13
    [28]#12
    [29]#12
    [30]#12
    [31]#12
    [32]北京化工大学,华南理工大学.塑料机械设计(第二版)[M].北京:中国轻工业出版社,1995.29-30
    [33]Zehev Tadmor,Costas G.Gogos.Principles of Polymer Processing(Second Edition)[M].USA:A John Wiley & Sons,Inc.,2006.272-284
    [34]P.A.Moysey,M.R.Thompson.Modelling the solids inflow and solids conveying of single-screw extruders using the discrete element method[J].Powder Technology,2005,153:95-107
    [35]L.Prat,S.N'Diaye,L.Rigal,C.Gourdon.Solid-liquid transport in a modified co-rotating twin-screw extruder—dynamic simulator and experimental validations[J].Chemical Engineering and Processing,2004,43:881-886
    [36]李晓林.单螺杆精密挤出机理的研究[D].北京:北京化工大学,2003
    [37]彭响方,瞿金平.塑料电磁动态塑化挤出机的节能分析[J].中国塑料,1998,12(2):98—102
    [38]宫成仁,王岳涛,毕丽萍.提高挤压机固体输送能力的措施[J].山东纺织科技,2000,6:13—14
    [39]M.D.Lechner,W.Borchard.The infuence of strong centrifugal force fields on solutions:I.Improved Hermans-Ende equation[J].European Polymer Journal,1999,35:371-376
    [40]J.Broszeit.Finite-element simulation of circulating the memory-integral type:flow in a steady flow for fluids of single-screw extruder[J].Non-Newtonian Fluid Mech,1997,70:35-58
    [41]Quanping Yu,Guo-Hua Hu.Development of a helical coordinate system and its application to analysis of polymer flow in screw extruders Part I.The balance equations in a helical coordinate system[J].Non-Newtonian Fluid Mech,1997,69:155-167
    [42]Seppo Syrjala.A NEW APPROACH FOR THE SIMULATION OF MELTING IN EXTRUDERS[J].Heat Mass Transfer,2000,27(5):623-634
    [43]Serafim Bakalis,Mukund V.Karwe.Velocity distributions and volume flow rates in the nip and transitional regions of a co-rotating,self-wiping,twin-screw extruder[J].Joumal of Food Engineering,2002,51:273-282
    [44]J.M.Buick,J.A.Cosgrove.Numerical simulation of the flow field in the mixing section of a screw extruder by the lattice Boltzmann model[J].Chemical Engineering Science,2006,61:3323 -3326
    [45]M.H.R.Ghoreishy,M.Razavi-Nouri,G.Naderi.Finite element analysis of a thermoplastic elastomer melt flow in the metering region of a single screw extruder[J].Computational Materials Science,2005,34:389 - 396
    [46]Ahmad Khalifeh,Jean-Robert Clermont.Numerical simulations of non-isothermal three-dimensional flows in an extruder by a finite-volume method[J].Non-Newtonian Fluid Mech,2005,126:7-22
    [47]张敏,孙胜,贾玉玺,宫晓峰.聚合物挤出过程中的数值模拟技术[J].高分子通报,2003.3:52-57
    [48]贺鹏,许澍华,江波.基于阿基米德螺线的磨盘挤出机数学模拟[J].塑料,2003,32(2):60-64
    [49]C.Rawendaal.Mixing in Polymer Processing[M].New York:Marcel Dekker,1991.405-462
    [50]Y.B'ereaux,M.Moguedet,X.Raoul,J.Y.Charmeau,J.Balcaen,D.Graebling.Series solutions for viscous and viscoelastic fluids flow in the helical rectangular channel of an extruder screw[J].Non-Newtonian Fluid Mech,2004,123:237-257
    [51]黄丽主编.高分子材料[M].北京:化学工业出版社,2005.14-20
    [52]金日光,华幼卿.高分子物理(第二版)[M].北京:化学工业出版社,2000.217-220
    [53]吴其晔,巫静安.高分子材料流变学[M].北京:高等教育出版社,2002.7-8
    [54]刘忠明.卧式螺旋离心机理论计算和分析[D].北京:北京化工大学,2001
    [55]栗玉民.螺旋卸料离心机差速器的设计计算[J].流体机械,1994,22(8):38-40
    [56]朱伟,唐跃.聚合物挤出加工中有关温度分布计算、测量、控制方法概述[J],橡塑技术与装备,2006,32:25-29
    [57]蔡仁良.过程装备密封技术(第二版)[M].北京:化学工业出版社,2006.46-174
    [58]孙启才,金鼎五.离心机原理结构与设计计算[M].北京:机械工业出版社,1978.12-254
    [59]P.Lin,Y.Jaluria.Conjugate thermal transport in the channel of an extruder for non-Newtonian fluids[J].International Journal of Heat and Mass Transfer,1998,41:3239-3253
    [60]王银霞,任冬云,陈卫红,王根永.新型高速挤出机计量段冷却方法研究[J].塑料,2005,34(3):81-83
    [61]李庆领.聚合物在挤出加工过程中的传热及流动特性研究[D].武汉:华中科技大学,2004
    [62]A.J查普曼著,何用梅译.传热学[M].北京:冶金工业出版社,1984.25-167
    [63]沈成俊,张伟民,顾剑锋,陈乃录.电流法测量空气换热系数[J].热加工工艺,2006,35(6):41-43
    [64]王瑁成,邵敏.有限单元法基本原理和数值方法(第二版)[M].北京:清华大学出版社,1997.24-257
    [65]濮伟.离心机转鼓壁厚的影响因素及参数关系图[J].过滤与分离,2002,12(1):18—20
    [66]刘聪聪.离心式挤出机固体输送及增压机理的研究[D].北京:北京化工大学,2007
    [67]刘聪聪,吴大鸣,Kuzyayev I.M,赵晶.离心式挤出机固体输送段的压力分布模型[J].塑料,2007,36(6):97-101
    [68]赵晶,吴大鸣,刘聪聪.离心式挤出机在聚合物加工中应用和发展[J].塑料,2007,36(5):59-61
    [69]赵晶,吴大鸣,陈卫红,许红.离心式挤出机固体输送机理实验研究[J].塑料,2008,37(3):待刊出
    [70]赵晶,吴大鸣,Kuzyayev I.M.离心式挤出机工作原理以及其固体输送压力影响因素的研究[J].塑料,2008,37(4):待刊出
    [71]周剑平编著.精通Origin 7.0[M].北京:北京航空航天大学出版社,2004.11-51
    [72]成大先主编.机械设计手册第2卷(第二版)[M].北京:化学工业出版社,1994.12-346
    [73]成大先主编.机械设计手册第3卷(第二版)[M].北京:化学工业出版社,1994.34-210
    [74]成大先主编.机械设计手册第4卷(第三版)[M].北京:化学工业出版社,1994.31-350
    [75]导向科技编著.MATLAB 6.0程序设计与实例应用[M].北京:中国铁道出版社,2001.
    [76]成大先主编.机械设计手册第1卷(第二版)[M].北京:化学工业出版社,1994.1-141

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