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Partial volumes pressure vessel

The water-filled autoclave containing the closed inner nickel cell is always in pressure equilibrium with an outside, room temperature, high-pressure vessel partially filled with mercury. Variation of the volume of the bellows is recorded by a float on the mercury contained in the room temperature vessel. The position of the float is determined magnetically (inductively) from outside. [Pg.138]

This chapter contains handy formulas for pressure vessels. Some of the formulas are from ASME, Section VIII, Division I 11], and others are associated formulations to calculate weights and partial fluid volumes. [Pg.11]

There are also handy pressure vessel formulas—calculation of head formulas with partial loaded volumes and head weights— included, making this a handy field guide. [Pg.198]

Suppose that we were to increase the total pressure inside a reaction vessel by pumping in argon or some other inert gas at constant volume. The reacting gases continue to occupy the same volume, and so their individual molar concentrations and partial pressures remain unchanged despite the presence of an inert gas. In this case, therefore, provided that the gases can be regarded as ideal, the equilibrium composition is unaffected despite the fact that the total pressure has increased. [Pg.502]

Br(g) from the thermodynamic data provided in Appendix 2A. (b) What is the vapor pressure of liquid bromine (c) What is the partial pressure of Br(g) above the liquid in a bottle of bromine at 25°C (d) A student wishes to add 0.0100 mol Br2 to a reaction and will do so by filling an evacuated flask with Br2 vapor from a reservoir that contains only bromine liquid in equilibrium with its vapor. The flask will be sealed and then transferred to the reaction vessel. What volume container should the student use to deliver 0.010 mol Br2(g) at 25°C ... [Pg.513]

Before calculating the pressures, we must visualize the reaction vessel. The container s total volume is 5.00 L, but 0.150 L is occupied by the aqueous solution. This leaves 4.85 L for the gas mixture. The partial pressure of hydrogen is calculated using the ideal gas equation and assuming that no H2 remains in solution this is a good assumption because hydrogen gas is not very soluble in water ... [Pg.324]

For the semi-batch stirred tank reactor, the model was based on the following assumptions the reactor is well agitated, so no concentration differences appear in the bulk of the liquid gas-liquid and liquid-solid mass transfer resistances can prevail and finally, the liquid phase is in batch, while hydrogen is continuously fed into the reactor. The hydrogen pressure is maintained constant. The liquid and gas volumes inside the reactor vessel can be regarded as constant, since the changes of the fluid properties due to reaction are minor. The total pressure of the gas phase (P) as well as the reactor temperature were continuously monitored and stored on a PC. The partial pressure of hydrogen (pnz) was calculated from the vapour pressure of the solvent (pvp) obtained from Antoine s equation (pvpo) and Raoult s law ... [Pg.190]

While in homogeneous systems the reaction is occurring throughout the entire volume of the reaction vessel and the partial pressures (concentrations) of the species participating in the rate-controlling step are often directly observable, the same is not true for heterogeneous systems. Here, reaction is confined to a monomolecular layer at the surface, around 10 "6 of the total volume of the reaction system, and the concentrations of... [Pg.4]

A reaction for the combustion of SO2 was prepared by opening a stopcock connecting two separate chambers. One of the chambers has a volume of 2.125L and is filled at 0.750 atm with SO2. The second chamber has the volume of 1.500 L filled at 0.500 atm with O2. The temperature of both is 80°C. (a) What were the mole fraction of SO2 in the mixture, the total pressure, and the partial pressures (b) If the mixture were to be passed over a catalyst that promoted the formation of SO3 and then was returned to the original two connected vessels, what were the mole fractions in the final mixture, and what was the final total pressure Assume that the final temperature is 80°C and that the conversion of the SO2 is complete to the extent of the availability of O2. [Pg.87]

Most storage vessels for cryogens are designed for a 90% liquid volume and a 10% vapor or ullage volume. The latter permits reasonable vaporization of the liquid contents due to heat leak without incurring too rapid a buildup of pressure in the vessel. This, in turn, permits closure of the container for short periods either to avoid partial loss of the contents or to permit the safe transport of flammable or hazardous cryogens. [Pg.190]

A decrease in the number of moles partially offsets this rise in pressure. Decreasing pressure will cause the reaction to move in the direction that forms more moles of gas. These changes in pressure might result from altering the volume of the reaction vessel at constant temperature. [Pg.165]

We can calculate the volume of the vessel from the final given conditions plus the value of the partial pressure of the water vapor in the final state... [Pg.104]

The volume of the water vapor at its partial pressure is the same as the volume of the vessel. [Pg.104]

Cas-Liquid Mass Transfer Gas-liquid mass transfer normally is correlated by means of the mass-transfer coefficient K a versus power level at various superficial gas velocities. The superficial gas velocity is the volume of gas at the average temperature and pressure at the midpoint in the taiik divided by the area of the vessel. In order to obtain the partial-pressure driving force, an assumption must be made of the partial pressure in equihbrium with the concentration of gas in the liquid. Many times this must be assumed, but if Fig. 18-26 is obtained in the pilot plant and the same assumption principle is used in evaluating the mixer in the full-scale tank, the error from the assumption is limited. [Pg.1456]

Dalton s Law of Portial Pressures. This law may be stated In a mixture of gases, each gas exerts a partial pressure equal to the pressure it would exert if it alone were present in the volume occupied by the mixture. In other words, the total pressure of a mixture of gases is equal to the sum of the partial pressures of its components. For example, consider two vessels of equal voltuues containing methane and ethane respectively, each at a pressure of one atmosphere. If the etiiane were forced into the methane tank at constant temperature, the pressure of the combined gases would be two atmospheres. According to Dalton s Law the partial pressures of the methane and ethane in the mixture would each be one atmosphere. [Pg.21]

At 600°C, a gas mixture of CO and CI2 is prepared that has initial partial pressures (before reaction) of 0.60 atm for CO and 1.10 atm for CI2. After the reaction mixture has reached equilibrium, the partial pressure of COCblg) at this temperature is measured to be 0.10 atm. Calculate the equilibrium constant for this reaction. The reaction is carried out in a vessel of fixed volume. [Pg.591]

We place 0.980 g of solid NH4CI into a closed vessel with volume 1.000 L and heat to 275°C. (a) In what direction does the reaction proceed. (b) What is the partial pressure of each gas at equilibrium (c) What is the mass of solid NH4CI at equilibrium ... [Pg.598]


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Partial pressure

Pressure vessels

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