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Container temperature

It follows that the position of thermodynamic equilibrium will change along the reactor for those reactions in which a change of tire number of gaseous molecules occurs, and therefore that the degree of completion and heat production or absorption of the reaction will also vaty. This is why the external control of the independent container temperature and the particle size of the catalyst are important factors in reactor design. [Pg.144]

Mass and energy additions to the containment associated with all the foregoing phenomena and their effect on containment temperature pressure, and steam condensation. [Pg.318]

Transition to detonation in charmels without obstacles was recently successfully simulated numerically [11,12]. In these simulations, it was shown that shock compression of the unreacted mixture forms the hot spots resulting from shock-shock, shock-wall, and shock-vortex interactions. The hot spots contain temperature gradients that produce spontaneous reaction waves and detonations. [Pg.200]

Table 14.4 contains temperature and pressure data obtained while using microwave heating with a single closed vessel for two different acids. For nitric acid, 200°C (80°C over the atmospheric boiling point) and 7kg cm-2 was achieved in 12min and for hydrochloric acid 153°C (43°C over the atmospheric boiling point) and 7kg cm-2 was obtained in 5min. [Pg.444]

Cooling zone. In the cooling zone, an additional HEPA-hltered laminar how unit cools down the sterilized containers. When leaving the tunnel, the container temperature is about 10 to 20°C above room temperature. The laminar how unit and exhaust fan of the cooling zone are adjusted so that the tunnel remains pressurized, thus preventing any unsterilized air from entering. All critical process parameters are fully controlled by a... [Pg.511]

Thus, this consideration shows that the thermoelasticity of the majority of the new models is considerably more complex than that of the phantom networks. However, the new models contain temperature-dependent parameters which are difficult to relate to molecular characteristics of a real rubber-elastic body. It is necessary to note that recent analysis by Gottlieb and Gaylord 63> has demonstrated that only the Gaylord tube model and the Flory constrained junction fluctuation model agree well with the experimental data on the uniaxial stress-strain response. On the other hand, their analysis has shown that all of the existing molecular theories cannot satisfactorily describe swelling behaviour with a physically reasonable set of parameters. The thermoelastic behaviour of the new models has not yet been analysed. [Pg.54]

Common steps in sample preservation are the use of proper containers, temperature control, addition of preservatives, and the observance of recommended sample holding time. The holding time depends on the analyte of interest and the sample matrix. For example, most dissolved metals are... [Pg.17]

The primary parameters affecting entrainment and evaporation are solar radiation, ambient temperature, storage or process temperature and pressure, liquid spill surface area, wind speed and the properties of the spilled material (such as vapor pressure, surface tension, and viscosity). Suppressing volatility by reducing containment temperature and constraining pool size or exposed surface area via a dike or berm are effective postmitigation approaches and are discussed in Chapters 3 and 5. [Pg.32]

Physical properties The dynamic viscosity p of the buffer solution the diffusi-vity D of the substances to be separated in the buffer solution pgP0, the specific heat pCp and the thermal conductivity k. (These three quantities are the only ones which contain temperature in their dimensions therefore we will formulate them as quotients to obtain k/pgP0 and the thermal diffusivity, a = k/pCp). The electrical properties are electrical conductivity, kei (current density/electrical field strength), and electrophoretic mobility, p. [Pg.172]

Heating of the circulating water and, therefore, of the load is very gradual but quite rapid. A temperature of 121 °C is typically reached in 25-30min inside 500ml containers the heating rate clearly depends on the characteristics of the solution and its containers. Temperature uniformity in time and space during the... [Pg.3536]

Caution. Do not distil to complete dryness and avoid bath temperatures above lOff The solid residue might contain temperature-unstable byproducts that can explode violently. [Pg.52]

Removal of heat from the containers is of prime concern in designing such a facility. Several options are being considered, including cooled water basin, natural convection in air, and forced convection in air. Particular attention will be given to designing a system that will continue to maintain container temperature at acceptable levels even in the event of postulated accidents or temporary abandonment of the facilities under emergency conditions. [Pg.28]

The non-linearity in terms of concentrations and exponential factor containing temperature, make the task of closing the reaction source term quite difficult. Even for an isothermal system, the time-averaged reaction source term will contain a new term, the time average of the product of fluctuating concentrations ( c ) of component 1 and component 2 ... [Pg.136]

CONTAINER TEMPERATURE QUANTITY DELIVERY INFORMATION SPECIMEN NOTES... [Pg.312]

The physical state of hazardous material in a storage or transport container is an important factor in considering the fate or transport into the environment during an accidental spill or discharge situation. Define the conditions of container temperature (Tc) and ambient temperature (TJ that will maintain the status of a chemical with the following physical characteristics. Note that MP and BP are the melting point and boiling point of the chemical, respectively. [Pg.458]

Exponential relationships described the relationship between the sugar concentration (°Brix) and apparent viscosity (T ioo). The slopes of such plots for COJ samples containing 50 to 65 °Brix ranged from 0.187 at 9.9 °C to 0.127 at 30 °C. Mathematical expressions containing temperature and concentration were also developed by Vital and Rao ( 0.). ... [Pg.162]

COPI vesicles were first discovered when isolated Golgi fractions were incubated in a solution containing ATP, cytosol, and a nonhydrolyzable analog of GTP (see Figure 17-10). Subsequent analysis of these vesicles showed that the coat is formed from large cytosolic complexes, called coatomers, composed of seven polypeptide subunits. Yeast cells containing temperature-sensitive mutations in COPI proteins accumulate proteins in the... [Pg.716]

Some of the techniques used in this study have been described previously (13). Solutions were saturated with Ar (99.99% pure, supplied by Linde), using a modification of the technique described by Swinnerton et al. (17). The normal dose rate of approximately 6 X 1016 e.v. gram-1 min. 1 was delivered by a Gammacell-220 (AECL) cobalt-60 irradiation unit. Lower dose rates by a factor of nine were achieved by enclosing the irradiation vessels inside a lead container. Temperatures of irradiated samples were controlled to 1°C. in experiments where the effects of temperature were studied but in other experiments were 24 2°C. Care was taken to minimize the effects of volume contraction and expansion at low temperatures in order to exclude air from Ar saturated solutions. [Pg.326]


See other pages where Container temperature is mentioned: [Pg.236]    [Pg.71]    [Pg.143]    [Pg.446]    [Pg.478]    [Pg.54]    [Pg.265]    [Pg.300]    [Pg.260]    [Pg.98]    [Pg.518]    [Pg.226]    [Pg.474]    [Pg.182]    [Pg.118]    [Pg.916]    [Pg.3437]    [Pg.1277]    [Pg.1807]    [Pg.1812]    [Pg.1813]    [Pg.1816]    [Pg.879]    [Pg.27]    [Pg.401]    [Pg.70]    [Pg.386]    [Pg.3436]    [Pg.294]    [Pg.984]    [Pg.405]    [Pg.202]   
See also in sourсe #XX -- [ Pg.13 , Pg.44 ]




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