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Pressure/heat transfer

Reductive alkylations and aminations requite pressure-rated reaction vessels and hiUy contained and blanketed support equipment. Nitrile hydrogenations are similar in thein requirements. Arylamine hydrogenations have historically required very high pressure vessel materials of constmction. A nominal breakpoint of 8 MPa (- 1200 psi) requites yet heavier wall constmction and correspondingly more expensive hydrogen pressurization. Heat transfer must be adequate, for the heat of reaction in arylamine ring reduction is - 50 kJ/mol (12 kcal/mol) (59). Solvents employed to maintain catalyst activity and improve heat-transfer efficiency reduce effective hydrogen partial pressures and requite fractionation from product and recycle to prove cost-effective. [Pg.211]

At constant pressure, heat transferred equals the change in enthalpy qP = AH... [Pg.59]

Figure 6 Calculation results of transient behaviour of primary coolant pressure, heat transfer tube temperature of PPWC and IHX, RPV temperature and fuel temperature... Figure 6 Calculation results of transient behaviour of primary coolant pressure, heat transfer tube temperature of PPWC and IHX, RPV temperature and fuel temperature...
Number of transfer units Pressure Vapor pressure Heat-transfer rate Condenser duty Reboiler duty External-reflux ratio... [Pg.3]

Condenser and reboiler - heat of condensation and vaporization, heat loads, thermal and physical properties, temperature, pressure, heat transfer coefficient, sU eam capacities... [Pg.952]

In the absence of vapor shear effects, the heat transfer coefficient around the lower tubes in a bundle should decrease. However, in general, it is difficult to predict the actual value in a tube bundle depending on the influence of vapor and condensate velocities, turbulence effects, vapor flow direction, tube bundle layout, pressure, heat transfer surface conditions, and so on. [Pg.1334]

Heat transfer in gas-fluidized bed can occur by conduction, convection, and radiation depending on the operating conditions. The contribution of the respective modes of heat transfer to the coefficient of heat transfer depends on particle classification, flow condition, fluidization regimes, type of distributor, operating temperature, and pressure. Heat transfer between a single particle and gas phase can be defined by the conventional equation of heat transfer ... [Pg.165]

Working pressure permitted— as per latest inspection Test pressure Heat transfer area Shell volume... [Pg.125]

As a thermal and fluidic system is miniaturized, certain physical phenomena become more or less predominant with scale, according to the Cube-Square law. Let us consider a machine with a characteristic dimension of length scale /, such as its length or diameter. Surface forces and fluxes, such as friction, pressure, heat transfer, and mass flow, will decrease proportionally to a characteristic area of the machine, hence as Volumetric effects, such as inertia, gravity, or mass, will decrease as /. With respect to each other, the volumetric effects will decrease more rapidly than surface phenomena as the machine is miniaturized ... [Pg.2232]

Physics—fluids, temperature, pressure, heat transfer, work, and energy Math and statistics Basic equipment and technology Computer literacy skills Communication skills On-the-job skills... [Pg.18]

Common chemistry and physics topics include pressure, heat transfer, viscosity, atoms and elements, compounds, hydrocarbons, temperature, heat and energy, specific gravity, bonding, solutions, distillation, fluid flow, density, reactions, molecules, compounds, mixtures, and matter. [Pg.67]

Borodulya VA, Ganzha VL, Podberezsky AI, Upadhyay SN, Saxena SE. High pressure heat transfer investigations for fluidized beds of large particles and immersed vertical tube bundles, Int J of Heat and Mass Transfer 26 1577-584, 1983. [Pg.160]

Considerations of steam cycle efficiency and cost of the pressure circuit influence selection of coolant pressure. Heat transfer performance has not been a contributory factor in determination of pressure as there is no significant change in performance over the range of Interest. Higher thermal efficiency leads to a requirement for higher coolant pressure which increases the pressure circuit cost, largely due to the influence of the zlrcaloy pressure tubes. In addition to capital cost, fuel cost is also affected because of neutron absorption by the thicker pressure tube. Circuit pressure is therefore selected to obtain the optimum balance between these factors. [Pg.71]

A4.1.2 Definitions of terms and expressions reiated to supercriticai pressure heat transfer... [Pg.796]

Technical Appendices, which provides readers with additional information and data on current nuclear power reactors and NPPs thermophysical properties of reactor coolants, thermophysical properties of fluids at suhcritical and critical/supercritical pressures, heat transfer and pressure drop in forced convection to fluids at supercritical pressures, world experience in nuclear steam reheat, etc. [Pg.924]


See other pages where Pressure/heat transfer is mentioned: [Pg.95]    [Pg.511]    [Pg.393]    [Pg.503]    [Pg.44]    [Pg.409]    [Pg.517]    [Pg.145]    [Pg.489]    [Pg.196]    [Pg.554]    [Pg.2115]    [Pg.24]    [Pg.681]    [Pg.144]    [Pg.180]    [Pg.74]    [Pg.31]   


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Heat transfer at constant pressure

Heat transfer pressure effect

Pressure Drop and Heat Transfer

Pressure Drop and Heat Transfer in a Single-Phase Flow

Pressure Drop. Mass and Heat Transfer

Pressure heat transfer coefficient, boiling

Pressure transfer

Pressure/heat transfer duties

Process-side heat transfer and pressure drop

Shell-side heat-transfer and pressure drop (single phase)

Supercritical pressure forced convection heat transfer

Supercritical pressure heat transfer

Tube banks pressure drop heat transfer

Tube-side heat-transfer coefficient and pressure drop (single phase)

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