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Temperature and Time Effects

The mechanical behavior of polymer composites is not only defined by short-term properties such as stiffness, strength, and toughness but also long-term properties such as creep, stress relaxation, and fatigue. All such properties, vhich are affected by temperature and type of environment, can be modified through the addition of fillers. [Pg.35]

In general, most fillers increase the heat distortion temperature (HDT) of plastics as a result of increasing modulus and reducing high-temperature creep. Thermoelastic properties such as coefficient of thermal expansion (CTE) are also affected by the presence of fillers and have been modeled through a variety of equations derived from the rule of mixtures [8]. For directional fillers, this property is strongly orientation-dependent, and because of the difference between the CTE of the filler and that of the matrix, internal stresses may lead to undesirable warpage. [Pg.35]


Temperature and Time Effect on TPPT Reactivity in Oil Solution... [Pg.391]

Higher Temperature and Time Effects on Secondary Reactions... [Pg.315]

YeUowing of wool can occur during dyeing, depending on pH, temperature and time, and chlorinated wools ate especially sensitive. Bleaching agents that can be added to the dyebath have been developed based on sodium bisulfite and hydroxylamine sulfate (108). Addition of hydrogen peroxide to the dyebath after exhaustion can also be effective. [Pg.349]

The temperature and time of curing, as indicated in Table A 13.4, are indicative and for general guidance only. They may vary with the type and quality of paint and effectiveness of the furnace. For exact details, consult the paint manufacturer. The operator may also vary the given parameters slightly, based on his own experience and the end results. [Pg.406]

A number of areas in which plastics are used in electrical and electronic design have been covered there are many more. Examples include fiber optics, computer hardware and software, radomes for radar transmitters, sound transmitters, and appliances. Reviewed were the basic use and behavior for plastics as an insulator or as a dielectric material and applying design parameters. The effect of field intensity, frequency, environmental effects, temperature, and time were reviewed as part of the design process. Several special applications for plastics based on intrinsic properties of plastics materials were also reviewed. [Pg.229]

In this paper we present a meaningful analysis of the operation of a batch polymerization reactor in its final stages (i.e. high conversion levels) where MWD broadening is relatively unimportant. The ultimate objective is to minimize the residual monomer concentration as fast as possible, using the time-optimal problem formulation. Isothermal as well as nonisothermal policies are derived based on a mathematical model that also takes depropagation into account. The effect of initiator concentration, initiator half-life and activation energy on optimum temperature and time is studied. [Pg.322]

These simulations clearly reveal the importance of considering M, in calculating the optimal temperature. is dependent on the heat of polymerization (-AH) as given by Eq. (13). Most monomers have heats of polymerization in the range of 50 to 80 KJ/mol. We thus decided to study the effect of (-AH) on optimal temperature and time for various half-life values of the initiator. The results are shown in Figme 5. [Pg.327]

Figure 3. Effect of Initiatior Activation Energy on Optimum Temperature and Time. Figure 3. Effect of Initiatior Activation Energy on Optimum Temperature and Time.
Figure 4. Effect of Half-life on Optimum Temperature and Time. Mg = 0.47 mol/L (5vol%) Mj = 0.047 mol/L (0.5vol%) ... Figure 4. Effect of Half-life on Optimum Temperature and Time. Mg = 0.47 mol/L (5vol%) Mj = 0.047 mol/L (0.5vol%) ...
Figure 5. Effect of Heat of Polymerization on Optimal Temperature and Time for Initiator with 10 hour half life at marked T. Figure 5. Effect of Heat of Polymerization on Optimal Temperature and Time for Initiator with 10 hour half life at marked T.
Again, bacterial spores are much more resistant than vegetative cells, and their recorded resistance varies markedly depending upon their degree of dryness. In many early studies on dry heat resistance of spores their water content was not adequately controlled, so conflicting data arose regarding the exposure conditions necessary to achieve effective sterilization. This was partly responsible for variatiorrs in recommended exposure temperatures and times in different pharmacopoeias. [Pg.397]

In reality, finding a suitable solvent is not as easy as simply matching the polymer s solubility parameter (8 value). It is also important to take into account the effects of polymer crystallinity (as in the case of aPP and iPP, LDPE and HDPE). Because of their various chemical structures, it may be necessary to experiment with solvent, temperature, and time conditions to optimise the extraction strategy. [Pg.148]

In static headspace sampling [301,302] the polymer is heated in a septum-capped vial for a time sufficient for the solid and vapour phases to reach equilibrium (typically 2 hours). The headspace is then sampled (either manually or automatically) for GC analysis, often followed by FID or NPD detection. Headspace sampling is a very effective method for maintaining a clean chromatographic system. Changing equilibrium temperature and time, and the volumes present in the headspace vial can influence the sensitivity of the static headspace system. SHS-GC-MS is capable of analysing volatile compounds in full scan with ppb level... [Pg.469]

Future work in this area will involve the extension of these techniques to other temperatures in an effort to better characterize the overall reaction kinetics of these two processes. In addition, degree of cure obtained through isothermal DSC measurements will be compared with the fraction of acetylene consumed as measured by isothermal FTIR experiments for the same temperature and time. Also, the effect of the incorporation of metal fillers on the isomerization and crosslinking reactions will be addressed. [Pg.469]

High porosity carbons ranging from typically microporous solids of narrow pore size distribution to materials with over 30% of mesopore contribution were produced by the treatment of various polymeric-type (coal) and carbonaceous (mesophase, semi-cokes, commercial active carbon) precursors with an excess of KOH. The effects related to parent material nature, KOH/precursor ratio and reaction temperature and time on the porosity characteristics and surface chemistry is described. The results are discussed in terms of suitability of produced carbons as an electrode material in electric double-layer capacitors. [Pg.86]

The most crucial point for a successful microwave-mediated synthesis is the optimized combination of temperature and time. According to the Arrhenius equation, k = A exp(- a/RT), a halving of the reaction time with every temperature increase of 10 degrees can be expected. With this rule of thumb, many conventional protocols can be converted into an effective microwave-mediated process. As a simple example, the time for a reaction in refluxing ethanol can be reduced from 8 h to only 2 min by increasing the temperature from 80 °C to 160 °C (Fig. 5.1 see also Table 2.4). [Pg.94]


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