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Final Processing Conditions

All polyurethanes need the complete cure as specified to develop the properties fully. If the product is allowed to stand for a week at ambient temperature, the full properties will be developed. [Pg.117]

A further heat treatment (sometimes referred to as annealing) or a longer, slightly hotter cure (18 hours at 130°C) will also improve properties such as tensile, tear, and overall toughness. [Pg.117]

Very hard compounds (80 Shore D and above) need this extra heat treatment to fully develop the bonding network and to prevent cracking under load or impact. The products will form glasslike fragments unless the extra heat treatment is complete. [Pg.117]

There are a number of other physical properties that are very important to the optimum performance of polyurethane other than the normally quoted ones in trade literature. These include temperature, dynamic, and hysteresis properties. [Pg.117]

The effect of temperature on polyurethanes has a number of zones (Garret, 2003)  [Pg.117]


Our studies showed the optimal viscosity ratio (riLcp/ tipp) for formation of small LCP domains and their spontaneous fibrillation to range from about 0.5 to 1. At lower viscosity ratios, the fiber structure was coarser, while at viscosity ratios above unity the LCP domains tended to be spherical or cluster-like. As the temperature and shear rate dependencies of LCP and the matrix polymer may well be different, it is extremely important to know the viscosity ratio under the actual processing conditions. Its effect on spontaneous fibrillation of the LCP domains forms the basis for material selection, but the final processing conditions determine how well the LCP phases will be fibrillated and oriented in... [Pg.311]

Molecular weight and polydispersity often can be manipulated. The degree of control over these properties will depend on the polymerization mechanism, conditions during polymerization, and final processing conditions, Polymers with low polydispersity have higher and sharper melting points than those... [Pg.629]

Systems involving an interface are often metastable, that is, essentially in equilibrium in some aspects although in principle evolving slowly to a final state of global equilibrium. The solid-vapor interface is a good example of this. We can have adsorption equilibrium and calculate various thermodynamic quantities for the adsorption process yet the particles of a solid are unstable toward a drift to the final equilibrium condition of a single, perfect crystal. Much of Chapters IX and XVII are thus thermodynamic in content. [Pg.2]

Depending on the final polymerization conditions, an equilibrium concentration of monomers (ca 8%) and short-chain oligomers (ca 2%) remains (72). Prior to fiber spinning, most of the residual monomer is removed. In the conventional process, the molten polymer is extmded as a strand, solidified, cut into chip, washed to remove residual monomer, and dried. In some newer continuous processes, the excess monomer is removed from the molten polymer by vacuum stripping. [Pg.251]

The following sections also include brief presentations of manufacturing procedures because the final properties of the fibers depend on the processing conditions. For more about the stmcture or mechanical characteristics of the fibers, the reader is directed to more comprehensive discussions presented elsewhere in the Eniyclopedia or in the Hterature (8,24—30). [Pg.5]

An interlock is a protec tive response initiated on the detection of a process hazard. The interlock system consists of the measurement devices, logic solvers, and final control elements that recognize the hazard and initiate an appropriate response. Most interlocks consist of one or more logic conditions that detect out-of-hmit process conditions and respond by driving the final control elements to the safe states. For example, one must specify that a valve fails open or fails closed. [Pg.797]

These tests must encompass the complete interlock system, from the measurement devices through the final control elements. Merely simulating inputs and checking the outputs is not sufficient. The tests must duplicate the process conditions and operating environments as closely as possible. The measurement devices and final control elements are exposed to process and ambient conditions and thus are usually the most hkely to fail. Valves that remain in the same position for extended periods of time may stick in that position and not operate when needed. The easiest component to test is the logic however, this is the least hkely to fail. [Pg.798]

Final Control Element-A device that directly changes the value of the variable used to control a process condition. [Pg.8]

State line Center point to Process Final air conditions Equipment used... [Pg.719]

The purpose of our calculation was to quantitatively evaluate the deformational behavior of the TLCP droplets and their fibrillation under the processing conditions, and finally, to establish a relationship among the calculated Weber number, the viscosity ratio, and the measured aspect ratio of the fibers. Figure 13 illustrates this procedure. All calculated results were plotted as... [Pg.693]

The process of adiabatic saturation in Section 24.4 assumed that the spray water temperature had no effect on the final air condition. If, however, a large mass of water is used in comparison with the mass of air, the final condition will approach the water temperature. If this water is chilled below the dew point of the entering air, moisture will condense out of the air, and it will leave the washer with a lower moisture content (see Figure 24.7). [Pg.247]

Some relevant effects of the polymorphism on the properties of polymeric materials are shown in the final section. In particular, it is shown that, while the occurrence of transitions between polymorphic forms can be detrimental for some systems, a precise knowledge of the polymorphic behavior and of the physical properties of the single forms can be used advantageously to improve the in use properties as well as the processing conditions of some polymeric materials,... [Pg.185]

In current practice the fluorescence assay is often followed by the use of hybridization techniques when more selectivity is required. We have for instance used the fluorescence techniques to obtain data on the nucleic acid content of malaria vaccine proteins produced in Escherichia coli. The rapid turnaround time of the fluorescence assay is particularly useful during the early stages of purification to determine the optimal process conditions. After the final process has been arrived at and a variety of methods used to assess the nucleic acid content (including the hybridization techniques), the fluorescence method can be developed for routine quality-control purposes. In certain cases, particularly at high protein concentrations, the dye may bind to the protein with... [Pg.48]

Km and values) and stereochemical properties. Ideally, screening should he carried out under reaction conditions that mimic the final process as closely as possible. This step is often one of the most time-consuming phases of process development, and improvements here can have significant impacts. [Pg.297]

GL 19] ]R 9] [P 20] About 20% (44 of 214) experiments were rejected since their conversions were too low (< 3%) to provide any useful information [64], After other experiments had also been rejected, finally 66% of aU experiments could be used. In a classical mini-batch test, 71% of all tests were employed, using the same reaction and processing conditions. [Pg.635]

Hydrogenation of lactose to lactitol on sponge itickel and mtheitium catalysts was studied experimentally in a laboratory-scale slurry reactor to reveal the true reaction paths. Parameter estimation was carried out with rival and the final results suggest that sorbitol and galactitol are primarily formed from lactitol. The conversion of the reactant (lactose), as well as the yields of the main (lactitol) and by-products were described very well by the kinetic model developed. The model includes the effects of concentrations, hydrogen pressure and temperature on reaction rates and product distribution. The model can be used for optinuzation of the process conditions to obtain highest possible yields of lactitol and suppressing the amounts of by-products. [Pg.113]


See other pages where Final Processing Conditions is mentioned: [Pg.456]    [Pg.631]    [Pg.115]    [Pg.117]    [Pg.278]    [Pg.280]    [Pg.172]    [Pg.355]    [Pg.7506]    [Pg.1025]    [Pg.18]    [Pg.456]    [Pg.631]    [Pg.115]    [Pg.117]    [Pg.278]    [Pg.280]    [Pg.172]    [Pg.355]    [Pg.7506]    [Pg.1025]    [Pg.18]    [Pg.384]    [Pg.206]    [Pg.328]    [Pg.459]    [Pg.23]    [Pg.67]    [Pg.225]    [Pg.457]    [Pg.1722]    [Pg.2057]    [Pg.2071]    [Pg.71]    [Pg.737]    [Pg.125]    [Pg.71]    [Pg.144]    [Pg.135]    [Pg.289]    [Pg.272]    [Pg.564]    [Pg.294]    [Pg.75]   


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Processing conditions

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