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Gases concentration units

Removing more heat from the pumparound returns, either by generating steam or adding coolers. This can decouple the fractionator from the reboilers in the gas concentration unit. [Pg.299]

Removing external streams. If gas comes from another unit or vents from a column in the gas concentration unit, consider routing it to the interstage rather than the suction. The refinery needs to evaluate if external streams are worth recovering or whether they can be routed elsewhere. [Pg.301]

The quantity consumed or produced is conveniently expressed in partial pressure units if the substance is a gas. Concentration units are convenient if the reactant or product is in solution. The time measurement is also expressed in whatever units fit the reaction microseconds for the explosion of household gas and oxygen, seconds or minutes for the burning of a candle, days for the rusting of iron, months for the rotting of wood. [Pg.125]

Atmospheric chemists love to use a gas concentration unit called number density, in which the concentrations are given in units of molecules per cubic centimeter. Please calculate the number densities of oxygen in the atmosphere at sea level (1 atm, 25°C) and at an altitude of 30 km (0.015 atm, —40°C). [Pg.16]

Gas concentration unit. Unstable gasoline and lighter products from the main fractionation overhead are separated into fuel gas, C1-C4 for alkylation, and debutanized gasoline. [Pg.2573]

Adsorption systems employing molecular sieves are available for feed gases having low acid gas concentrations. Another option is based on the use of polymeric, semipermeable membranes which rely on the higher solubiHties and diffusion rates of carbon dioxide and hydrogen sulfide in the polymeric material relative to methane for membrane selectivity and separation of the various constituents. Membrane units have been designed that are effective at small and medium flow rates for the bulk removal of carbon dioxide. [Pg.172]

The solubihty coefficient must have units that are consistent with equation 3. In the hterature S has units cc(STP)/(cm atm), where cc(STP) is a molar unit for absorbed permeant (nominally cubic centimeters of gas at standard temperature and pressure) and cm is a volume of polymer. When these units are multiphed by an equihbrium pressure of permeant, concentration units result. In preferred SI units, S has units of nmol /(m GPa). [Pg.487]

Investigators of tower packings normally report kcCi values measured at very low inlet-gas concentrations, so that yBM = 1, and at total pressures close to 100 kPa (1 atm). Thus, the correct rate coefficient For use in packed-tower designs involving the use of the driving force y — y /yBM is obtained by multiplying the reported k co values oy the value of pf employed in the actual test unit (e.g., 100 kPa) and not the total pressure of the system to be designed. [Pg.607]

Equations (12.40) to (12.45) describe the velocities u, v, w, the temperature distribution T, the concentration distribution c (mass of gas per unit ma.ss of mixture, particles per volume, droplet number density, etc.) and pressure distribution p. These variables can also be used for the calculation of air volume flow, convective air movement, and contaminant transport. [Pg.1178]

Solution The experimental conditions are consistent with Equation (11.26) so that kiAi was measured. The experimental result was reported as KgAi because the overall mass transfer coefficient was based on the equivalent gas-phase driving force expressed in partial pressure units rather than concentration units. Because a pure gas was sparged, kg oo and Kj = k . Equation (11.3) relates Kg and Ki through Henry s law constant. [Pg.399]

C16-0007. Write the equilibrium constant expression for HCl gas dissolving in water to produce hydronium ions, and indicate the appropriate concentration units for each ... [Pg.1147]

In the preceding solvent extraction models, it was assumed that the phase flow rates L and G remained constant, which is consistent with a low degree of solute transfer relative to the total phase flow rate. For the case of gas absorption, normally the liquid flow is fairly constant and Lq is approximately equal to Li but often the gas flow can change quite substantially, such that Gq no longer equals Gj. For highly concentrated gas phase systems, it is therefore often preferable to define flow rates, L and G, on a solute-free mass basis and to express concentrations X and Y as mass ratio concentrations. This system of concentration units is used in the simulation example AMMONAB. [Pg.199]

The gas is at high concentration and therefore the column component balance equations are based on mole ratio concentration units. The form of the balance equations follow those of Sec. 4.4.1. [Pg.567]

La Mede, France (Ref, 12) 6 (most in buildings) A liquefied petroleum gas (LPC) leak in the gas concentration section of a catalytic cracking unit resulted in an explosion that destroyed the unit and demolished the adjacent control room. [Pg.84]

Figure 11. Variation of unattached fraction of potential alpha-energy and equilibrium factor according to a model of room aerosol behaviour and the effect on bronchial dose rate per unit radon gas concentration. Figure 11. Variation of unattached fraction of potential alpha-energy and equilibrium factor according to a model of room aerosol behaviour and the effect on bronchial dose rate per unit radon gas concentration.
The H2 is separated from C02 and purified at the final stage of the process. Older variations of the SMR process (Figure 2.5a) used solvents to remove the acid gas (C02) from the gaseous stream after WGS reactors. Solvents commercially used for C02 removal in the gas separation unit include monoethanolamine (most preferred and widely used solvent), water, ammonia solutions, potassium carbonate solutions, and methanol. This operation allows the reduction of C02 concentration in the process gas to about 100 ppm. The remaining... [Pg.41]

Equation 3-7 is converted to the more convenient concentration units of ppm by direct application of the ideal gas law. Let m represent mass, p represent density, and the subscripts v and b denote the volatile and bulk gas species, respectively. Then ... [Pg.87]

Arrhenius Parameters and Choice of Concentration Units for Gas-Phase Reactions... [Pg.80]

The term XA refers to the mole fraction of gas A. The mole fraction of gas A is equal to the moles gas A/total moles of gas in the mixture. The mole fraction is a concentration unit that we will see again in Chapter 12. [Pg.80]

Hormones often engage with different types of Ga sub-unit in a concentration-dependent fashion. [Pg.107]


See other pages where Gases concentration units is mentioned: [Pg.99]    [Pg.1256]    [Pg.519]    [Pg.521]    [Pg.518]    [Pg.520]    [Pg.42]    [Pg.126]    [Pg.107]    [Pg.211]    [Pg.460]    [Pg.1398]    [Pg.233]    [Pg.340]    [Pg.127]    [Pg.428]    [Pg.1256]    [Pg.1327]    [Pg.354]    [Pg.399]    [Pg.578]    [Pg.587]    [Pg.152]    [Pg.66]    [Pg.67]    [Pg.652]    [Pg.112]   


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Concentration units

Gas concentration

Gas units

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