Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

Molecular weight and distribution

The degree of polymerization will usually be determined by the concentration of X. Some X may be lost in side reactions during the formation of IX. In some [Pg.459]

Other variations and combinations of these processes are also possible and are described in the following sections. [Pg.460]


Fig. 7. Shear viscosity at 180°C of polypropylene of different molecular weight and distribution vs shear rate (30) see Table 4 for key. Pa-s = 0.1 P... Fig. 7. Shear viscosity at 180°C of polypropylene of different molecular weight and distribution vs shear rate (30) see Table 4 for key. Pa-s = 0.1 P...
The processes used commercially for the manufacture of film and sheeting materials are generaUy similar in basic concept, but variations in equipment or process conditions are used to optimize output for each type of film or sheeting material. The nature of the polymer to be used, its formulation with plasticizers (qv), fillers (qv), flow modifiers, stabilizers, and other modifiers, as weU as its molecular weight and distribution are aU critical to the... [Pg.378]

Radical polymerization is often the preferred mechanism for forming polymers and most commercial polymer materials involve radical chemistry at some stage of their production cycle. From both economic and practical viewpoints, the advantages of radical over other forms of polymerization arc many (Chapter 1). However, one of the often-cited "problems" with radical polymerization is a perceived lack of control over the process the inability to precisely control molecular weight and distribution, limited capacity to make complex architectures and the range of undefined defect structures and other forms of "structure irregularity" that may be present in polymers prepared by this mechanism. Much research has been directed at providing answers for problems of this nature. In this, and in the subsequent chapter, we detail the current status of the efforts to redress these issues. In this chapter, wc focus on how to achieve control by appropriate selection of the reaction conditions in conventional radical polymerization. [Pg.413]

And there are others. If you are using a walk-up system, there will probably be some general guidelines posted on it. Assume that these are useful and adhere to them as far as possible. They will be by their very nature, no more than a guide, as every sample is unique in terms of its molecular weight and distribution of signal intensity. Also, a walk-up system is likely to be limited in terms of how much time... [Pg.14]

The. aiftlicatiaiL at qtgssuis. has. a. djamaJk. dta. oa. tjjfi. mo aiusaL properties of polymeric materials. The precise nature of this effect varies with such factors as temperature, polymer, molecular weight and distribution, and magnitude of applied pressure. Each material must be evaluated separately under the specific conditions of use. [Pg.66]

We note from Table VIII a strong interest in halogenated resists, particularly those substituted with chlorine. The addition of chlorine to the aromatic structure of polystyrene has a marked effect on cross-linking efficiency. Monodisperse polystyrene, for example, has a sensitivity on the order of 50 p C/cm2, yet with as little as 20% chloromethyl groups substituted on the ring, the sensitivity is improved to 2 C/cm2 for comparable molecular weight and distribution. [Pg.77]

The main interest of this work, therefore, lay in the field of water-soluble polymers and their influence on drag reduction in turbulent pipe flow, as it is from this field that the major technological use is to be expected. The investigation of the influential parameters for this class of polymers, such as molecular weight and distribution thereof, thermodynamic quality of the solvent, to name but a few (see Sect. 6.3.3), must precede a clear-cut characterization (see Sect. 6.3.1) of the polymer used. [Pg.155]

Upon start-up, and between runs, the reactor was full of water. The initial run required operation for a time equivalent to 2. 1 residence times to displace the water, with 1.5 residence times between each run. The difference is because the preheater was not filled with water between runs. Samples were regularly and periodically collected after 1.5 or 2. 1 residence times for further characterization. Molecular weights and distributions were measured by GPC. [Pg.562]

In this variation of high performance liquid chromatography (HPLC), the columns are packed with material that will hold back molecules dependent on the molecular size. Using the correct solvent system and column types, the molecular weight and distribution of the polyols can be determined. Standard samples are needed to calibrate the system. The molecular weight distribution of prepolymers can also be determined. This will enable an estimation to be made of the number of soft segment chains there are. [Pg.193]

Liu J, Yang F, Xian M et al (2001) Molecular weight and distribution of the copolymer of lignin/phenol in the copolymerization catalyzed by peroxidase. Macromol Chem Phys 202 840-848... [Pg.173]

Epoxy networks may be expected to differ from typical elastomer networks as a consequence of their much higher crosslink density. However, the same microstructural features which influence the properties of elastomers also exist in epoxy networks. These include the number average molecular weight and distribution of network chains, the extent of chain branching, the concentration of trapped entanglements, and the soluble fraction (i.e., molecular species not attached to the network). These parameters are typically difficult to isolate and control in epoxy systems. Recently, however, the development of accurate network formation theories, and the use of unique systems, have resulted in the synthesis of epoxies with specifically controlled microstructures Structure-property studies on these materials are just starting to provide meaningful quantitative information, and some of these will be discussed in this chapter. [Pg.116]

In these equations, and are the initial molecular weights, 4>(s) and 4>(x) are the quantum yields for the scissioning and cross-linking reactions, respectively D is absorbed dose and is Avogadro s number. The slopes of the respective plots of I/M and I/M versus dose produce two simultaneous equations, the solution of which yields values for 4>(s) and 4>(x). We (60) have analyzed the data obtained for a number of polysilane derivatives by GPC (gel permeation chromatography) to evaluate the respective molecular weights and distributions (Table III). Polystyrene standards were used for molecular weight calibration. [Pg.438]

Figure 3. Use of aniline to control molecular weight and distribution. Figure 3. Use of aniline to control molecular weight and distribution.

See other pages where Molecular weight and distribution is mentioned: [Pg.204]    [Pg.316]    [Pg.100]    [Pg.617]    [Pg.458]    [Pg.490]    [Pg.499]    [Pg.605]    [Pg.630]    [Pg.335]    [Pg.6]    [Pg.162]    [Pg.67]    [Pg.466]    [Pg.100]    [Pg.237]    [Pg.133]    [Pg.1435]    [Pg.78]    [Pg.578]    [Pg.588]    [Pg.294]    [Pg.118]    [Pg.60]    [Pg.4]    [Pg.42]    [Pg.204]    [Pg.269]    [Pg.284]    [Pg.419]    [Pg.197]   
See also in sourсe #XX -- [ Pg.490 ]




SEARCH



Distribution weight

Molecular distribution

Molecular weight and

Molecular weight distribution

© 2024 chempedia.info