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     Under the conditions of total concentration of monomer being 25-45%, initiator concentration being 0.06-0.1%, emulsifier concentration being 5-9% and polymerization temperature being 303K, the kinetic equation of copolymerization can be expressed: Rp=k[M]0.68[I]1.31[E]0.73.In this paper, above results are explained.
     在单体浓度为25─45%,引发剂浓度0.06—0.1%,乳化剂浓度为5—9%,聚合温度303K条件下,得到了共聚反应动力学方程:Rp=k[M]0.68[I]1.31[E]0.73,文中对上述结果做了解释.
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     The copolymer structure was characterized by IR and X-ray diffrac-tion, Maximum G%and E%were obtained at[APS]=[TU]=(6-8)10 ̄(-3)mol/L,[M]=0. 6mol/L,SA=2.0g/100ml,60℃ for 4h.
     当[APS]=[TU]=(6-8)×10 ̄(-3)mol/L、[M]=0.6mol/L、SA=2.0g/100mol、60℃、反应4h时,所得接枝共聚物的接枝率(G)及接枝效率(E)值最佳。
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     The total reaction rate of butadiene with α-MNLi initiate system was measured by the equation:-d[M]/dt=0.28[α-MNLi] ̄0.5[M],when the temperature was 40℃.
     40℃时,生成1,4-PB的反应动力学方程式为-d[M]/dt=0.28[C] ̄0.5[M]; DPE用量增大,表观增长反应过度常数K_p ̄η减小;
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     The polymerization process was characterized by a steady-state reaction within the experimental range, and polymerization rate is first order in both the concentration of neodymium compound and monomer,that is,Rp =-d[M]/dt=Kp[Nd][M].
     聚合速度对单体浓度和催化剂浓度均为一级关系,即聚合速度方程为Rp=Kp[Nd][M]
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     This article tries to demonstrate the phonetic system of Gao-chun Dialect, especially to describe three group of nasal consonant homonyms [m] [n] [η] which can act as syllables independently in Gao-chun Dialect, and also to analyze something related.
     本文介绍了高淳方言的语音系 统,特别是对高淳方言中鼻辅音[m][n][η]自成音节的三组同音字进行了描述,并就相关 问题作了一些分析。
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     The kinetics of butadiene polymerization with tow catalyst systems consisted of Nd(naph)3 and Al (i-Bu)3 or Al(i-Bu)2H was studied and a polymerization rate equation was obtained.
     研究了Nd(naph)_3-Al(i-Bu)_2Cl催化体系引发丁二烯聚合动力学,得到了聚合速度方程式-d[M]/dt=k_pα[c]0[M]
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     The experimental results indicated that the velocity of initial polymerization was in direct proportion to 1/2 power of the catalyst concentration and to 3/2 power of the monomer concentration. The apparent activation energy of polymerization was 49.91 kJ/mol from calculation.
     结果表明,初始聚合反应速度与两种引发剂各自浓度的1/2次方成正比,与单体浓度[M]的3/2次方成正比,并求得聚合反应表观活化能为49.91kJ/mol。
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     The equation of polymerization rate was obtained, Rp=7.5×1041.80. The overall activation energy was 27.7 kJ/mol, which was lower than that of ordinary system.
     在低转化率条件下,体系呈现稳态聚合特征,测得聚合反应速率方程为Rp = Kp[Nd]1 .8[ M]0 ,表观活化能为27.7 kJ/mol。
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     The probability density functions of the co-polarized and cross-polarized phase differences are analyzed by Muller matrix and the numerical results are also given.
     由米勒矩阵[M]分析了相差的密度函数,并得出各自相应的数值结果。
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     Kinetic charactristics of polyphenol oxidase(PPO)in burdock were studied. The result shows that the optimum pH and temperature are 7.2 and 50℃ respectively,and the maximum velocity is 105.4,the Michaelis constant was 0.16.The effect of inhibitors on the activity of PPO was studied in this paper as well.
     本文研究了牛蒡多酚氧化酶的动力学特性,结果表明其最适温度为50℃,最适pH值为7.2,最大反应速度Vmax=105.4[u],米氏常数Km=0.16[M]。 本文同时讨论了抑制剂对牛蒡多酚氧化酶活性的影响。
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  m
In all these cases we actually show that Γ=π1(M) has a finite index subgroup which is mapped onto a nonabelian free group.
      
As an example of how this can be used, we show that the ring of invariants (under the adjoint action of SL (3)) ofg copies ofM3 is C-M.
      
As a corollary we obtain that the moduli space of rank 3 and degree 0 bundles on a smooth projective curve of genusg is C-M.
      
[M]) for the symplectic case and Berndt and Vanhecke [BV1] for the rank-one case.
      
LetMm be a closed smooth manifold with an involution having fixed set of the form (point)?Fn, 0>amp;lt;n>amp;lt;m.
      
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