The role of PB-1 on the long chain branching of PP by electron beam irradiation in solid state and melt viscoelastic behavior

2013 ◽  
Vol 87 ◽  
pp. 64-70 ◽  
Author(s):  
Farzaneh Ardakani ◽  
Yousef Jahani ◽  
Jalil Morshedian
2005 ◽  
Vol 99 (1) ◽  
pp. 260-265 ◽  
Author(s):  
B. Krause ◽  
M. Stephan ◽  
S. Volkland ◽  
D. Voigt ◽  
L. Häußler ◽  
...  

2018 ◽  
Vol 20 (11) ◽  
pp. 2596-2610 ◽  
Author(s):  
Minwoo Lee ◽  
Min Haeng Heo ◽  
Hyunho Lee ◽  
Hwi-Hui Lee ◽  
Haemin Jeong ◽  
...  

Cellulose nanocrystals were preparedviashort-time pretreatment by electron-beam irradiation in the solid state and disintegration using high pressure homogenization.


2015 ◽  
Vol 10 (3) ◽  
pp. 237-241
Author(s):  
Naoto Tomite ◽  
Yukitaka Arai ◽  
Yoshimichi Ohki ◽  
Toru Hinata ◽  
Masakazu Washio

AIP Advances ◽  
2016 ◽  
Vol 6 (9) ◽  
pp. 095304 ◽  
Author(s):  
P. V. Borisyuk ◽  
O. S. Vasilyev ◽  
Y. Y. Lebedinskii ◽  
A. V. Krasavin ◽  
E. V. Tkalya ◽  
...  

1977 ◽  
Vol 50 (1) ◽  
pp. 99-108 ◽  
Author(s):  
N. Nakajima ◽  
E. R. Harrell ◽  
E. A. Collins

Abstract A practical range of frequency with the Rheometric mechanical spectrometer for the determination of G′ and G″ was shown to be from 2.5×10−2 to 2.5×102s−1, but one decade lower frequency may be reached routinely. The values G′ and G″ may be calculated from the steady-state viscosity curve obtained with the variable-speed Mooney rheometer. However, with samples having long-chain branching, the calculated G′ and G″ are somewhat higher, the difference being close in magnitude to the error of the measurements. With the variable-speed Mooney rheometer, the highest available shear rate is 16 s−1, about one decade less than that with the Rheometrics instrument. With high-molecular-weight rubbers, the range is further reduced, because of “slipping” or “fracturing” of the polymer. On the other hand, the Mooney rheometer enables one to extend the low-frequency range to 2×10−3s−1 very conveniently. The degree of long-chain branching may be estimated from the viscoelastic behavior by comparing complex viscosity and steady-state viscosity at the same time scale, both measurements being made with a Mooney rheometer at a slow speed with a single charge of sample.


2008 ◽  
Vol 44 (1) ◽  
pp. 200-212 ◽  
Author(s):  
E. Borsig ◽  
M. van Duin ◽  
A.D. Gotsis ◽  
F. Picchioni

Author(s):  
Chang Dae Han

The fact that a polymer consists of a number of chains of different lengths, each in turn consisting of a series of monomer units, means that the motion of one part of the polymer chain will profoundly affect the motion of other parts. Hence, for a given polymer, a description of microscopic processes occurring under a given flow field depends on hypotheses regarding the molecular structure and mechanisms of flow in the polymer. Today, it is well-known, gained from practical experience, that the molecular weight, the molecular weight distribution, and the degree of long-chain branching influence the rheological properties of polymeric liquids. Therefore, a better understanding of the relationship between molecular parameters and rheological properties is very important from the standpoints of both polymer synthesis and polymer processing. However, the theoretical development of this aspect of the problem is far from complete, although some important progress has been made. In the preceding chapter, we discussed the viscoelastic behavior of polymeric liquids from the phenomenological point of view, without associating the significance of theoretical predictions to molecular origin(s). Specifically, we have seen that the rheological equations of state contain parameters that vary from polymer to polymer. Since it has amply been demonstrated by experiment that the extent of a particular viscoelastic behavior is greatly influenced by the molecular parameters, such as molecular weight, molecular weight distribution, and the degree of long-chain branching, predictions of any viscoelastic behavior of polymers on the basis of phenomenological theory is of very limited use to either control the quality of polymers produced or improve the performance of polymers, unless the parameters appearing in various continuum constitutive equations are related to molecular parameters.


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