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Temperature, gas

There are an infinite number of other integrating factors X with corresponding fiinctions ( ) the new quantities T and. S are chosen for convenience.. S is, of course, the entropy and T, a fiinction of 0 only, is the absolute temperature , which will turn out to be the ideal-gas temperature, 0jg. The constant C is just a scale factor detennining the size of the degree. [Pg.335]

So far, the themiodynamic temperature T has appeared only as an integrating denominator, a fiinction of the empirical temperature 0. One now can show that T is, except for an arbitrary proportionality factor, the same as the empirical ideal-gas temperature 0jg introduced earlier. Equation (A2.1.15) can be rewritten in the fomi... [Pg.336]

As in tire case of themial conductivity, we see that the viscosity is independent of the density at low densities, and grows witli the square root of the gas temperature. This latter prediction is modified by a more systematic calculation based upon the Boltzmaim equation, but the independence of viscosity on density remains valid in the Boltzmaim equation approach as well. [Pg.675]

A non-tliennal, non-equilibrium plasma is characterized by an electron temperature much larger tlian tire ion temperature and tire neutral gas temperature (T T. Typical non-tliennal, non-equilibrium plasmas... [Pg.2796]

Monomer emulsions ate prepared in separate stainless steel emulsification tanks that are usually equipped with a turbine agitator, manometer level gage, cooling cods, a sprayer inert gas, temperature recorder, mpture disk, flame arrester, and various nossles for charging the ingredients. Monomer emulsions are commonly fed continuously to the reactor throughout the polymerisation. [Pg.169]

Exhaust gas temperature sensor Catalytic substrate Heat insulator... [Pg.308]

The time constants characterizing heat transfer in convection or radiation dominated rotary kilns are readily developed using less general heat-transfer models than that presented herein. These time constants define simple scaling laws which can be used to estimate the effects of fill fraction, kiln diameter, moisture, and rotation rate on the temperatures of the soHds. Criteria can also be estabHshed for estimating the relative importance of radiation and convection. In the following analysis, the kiln wall temperature, and the kiln gas temperature, T, are considered constant. Separate analyses are conducted for dry and wet conditions. [Pg.49]

In this equation, is the gas thermal conductivity the Hquid density the Hquid heat capacity T, the gas temperature the initial droplet temperature and the droplet boiling point. [Pg.55]

Quench Converter. The quench converter (Fig. 7a) was the basis for the initial ICl low pressure methanol flow sheet. A portion of the mixed synthesis and recycle gas bypasses the loop interchanger, which provides the quench fractions for the iatermediate catalyst beds. The remaining feed gas is heated to the inlet temperature of the first bed. Because the beds are adiabatic, the feed gas temperature increases as the exothermic synthesis reactions proceed. The injection of quench gas between the beds serves to cool the reacting mixture and add more reactants prior to entering the next catalyst bed. Quench converters typically contain three to six catalyst beds with a gas distributor in between each bed for injecting the quench gas. A variety of gas mixing and distribution devices are employed which characterize the proprietary converter designs. [Pg.279]

Determination of the Gas-Phase Temperature. The development given above is in terms of interface conditions, bulk Hquid temperature, and bulk gas enthalpy. Often the temperature of the vapor phase is important to the designer, either as one of the variables specified or as an important indicator of fogging conditions in the column. Such a condition would occur if the gas temperature equaled the saturation temperature, that is, the interface temperature. When fogging does occur, the column can no longer be expected to operate according to the relations presented herein but is basically out of control. [Pg.102]

SO2 gas is catalyticaHy oxidized to SO in a fixed bed reactor (converter) which operates adiabaticaHy in each catalyst pass. The heat of reaction raises the process gas temperature in the first pass to approximately 600°C (see Table 7). The temperature of hot gas exiting the first pass is then lowered to the desired second pass inlet temperature (430—450°C) by removing the heat of reaction in a steam superheater or second boiler. [Pg.185]

Gas leaving the converter is normally cooled to 180—250°C using boiler feedwater in an "economizer." This increases overall plant energy recovery and improves SO absorption by lowering the process gas temperature entering the absorption tower. The process gas is not cooled to a lower temperature to avoid the possibiUty of corrosion from condensing sulfuric acid originating from trace water in the gas stream. In some cases, a gas cooler is used instead of an economizer. [Pg.185]


See other pages where Temperature, gas is mentioned: [Pg.420]    [Pg.325]    [Pg.1106]    [Pg.3005]    [Pg.92]    [Pg.254]    [Pg.254]    [Pg.254]    [Pg.275]    [Pg.279]    [Pg.391]    [Pg.401]    [Pg.401]    [Pg.420]    [Pg.377]    [Pg.147]    [Pg.389]    [Pg.419]    [Pg.56]    [Pg.59]    [Pg.204]    [Pg.417]    [Pg.412]    [Pg.423]    [Pg.424]    [Pg.435]    [Pg.57]    [Pg.223]    [Pg.351]    [Pg.108]    [Pg.114]    [Pg.347]    [Pg.8]    [Pg.16]    [Pg.26]    [Pg.67]    [Pg.102]    [Pg.367]    [Pg.185]   
See also in sourсe #XX -- [ Pg.579 , Pg.580 , Pg.582 ]




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Accumulation of gas in a vessel at constant temperature

Acid temperature in input gas

Adiabatic stagnation temperature for an ideal gas

And the ideal gas temperature

Bath gas temperature

Catalyst Degradation, SO2 Strength, Feed Gas Temperature

Catalyst degradation, SO2 strength, and feed gas temperature

Compressed gas temperature

Compression of gases temperature rise

Control gas temperature controlled

Control of Gas Temperature by Bypassing

Control of product gas temperature method

Cooling of product gas melting temperature

Cooling of product gas temperature

Core gas temperature

Critical temperature of a gas

Critical temperatures of gases

Degradation feed gas temperature choice

Dilute gases temperature

Economizer bypass for gas temperature

Effect of Feed Gas Temperature on Intercept

Effect of Input Gas Temperature

Effects of Initial Temperature and Non-combustible Gases on Detonation Parameters

Efficiency) higher gas temperatures

Electrochemistry of Zirconia Gas Sensors temperature and

Equation of state for ideal gases at very low temperatures

Exhaust gas temperature

Exiting gases exit temperature

Factors Affecting Flue Gas Exit Temperature

Feed Gas Temperature Effect

Flue gas exit temperature

Flue gases, high-temperature

Flue-gas stack temperature

Flue-gas temperatures

Furnace gas exit temperature

Gas absolute temperature

Gas chromatography temperature

Gas chromatography temperature programming

Gas composition control target temperature

Gas input temperature

Gas pressure and temperature

Gas reaction temperature

Gas stoichiometry at standard temperature and pressure

Gas temperature, decrease

Gas-phase temperature

Gases autoignition temperature

Gases critical temperature

Gases ignition temperatures

Gases kelvin temperature

Gases maximum operating temperature

Gases standard temperature

Gases standard temperature and

Gases temperature and

Gases temperature effects

Gases volume-temperature relationships

Gases volume-temperature-pressure

Gases, temperature profiles

Global increase in atmospheric greenhouse gases and temperatures

HTGR (high-temperature, gas-cooled

Heatup paths affected by feed gas temperature

High and Low Temperature Water-Gas Shift Reactions

High temperature corrosion of structural materials under gas-cooled reactor helium

High temperature gas chromatography mass

High temperature gas chromatography mass spectrometry

High temperature gas cooled

High temperature gas cooled reactors

High temperature gas cooled reactors HTGRs)

High temperature water gas shift

High-Temperature Gas-Cooled Reactor Vessel (HTGCR)

High-Temperature SiC-FET Chemical Gas Sensors

High-temperature gas chromatography

High-temperature gas-cooled nuclear reactor

High-temperature gas-cooled reactor HTGR)

High-temperature gas-cooled reactors Plants

High-temperature gases

High-temperature gases environments

High-temperature gases kinetics

High-temperature gases mass change analysis

High-temperature gases oxidation

High-temperature gases oxidation rate laws

High-temperature gases reference materials

High-temperature gases structural changes

High-temperature gases sulfidation

High-temperature gases testing

High-temperature gases thermodynamics

Hot gas temperature

How does temperature affect the volume of a gas

Ideal gas temperature scale

Importance of Gas Temperature

Industrial data input gas temperatures

Influence of the Gas Inlet Temperature

Inlet gas temperature

Input Gas Temperature Effect

Intrapellet and Bulk Gas Temperature

Limiting Halite Deposition in a Wet High-Temperature Gas Well

Low temperature water gas shift

Major Effect - Catalyst Bed Input Gas Temperatures

Mass balances for affected by input gas temperature

Metal Oxides for Room-Temperature Gas Sensors

Natural gas hydrate temperature

Needs for More Binary or Multiple Gas Mixture Separation Data at High Temperatures

Noble gas recharge temperatures

Noble gases temperature effect

Of gases at various temperatures

Off-gas temperatures

Organometallic Complexes Observed at Low Temperature in Rare Gas or Other Media

Perfect gas temperature

Poc Gas Temperature History Through a Furnace

Pressure-Temperature Diagrams for Multicomponent Natural Gas Systems

Programmed temperature gas chromatography (ptgc)

Real gases critical temperature

SO2 oxidation efficiency gas temperature effect

SO3 concentrations in industrial gases temperature equation

Simultaneous retrieval of temperature and gas abundance

Solubility as a Function of Temperature and Henrys Constant at 25C for Gases in Water

Solubility of gases in water at various temperatures

Standard temperature and pressure for gases

Standard temperature for gases

Tail gas temperature

Temperature 6 Effect of Input Gas SO3 concentration on Output Acid

Temperature Ideal gas

Temperature and volume of gas

Temperature combined gas law

Temperature control, gas

Temperature control, gas bypass

Temperature control, gas calculations

Temperature control, gas devices

Temperature control, gas flowsheet

Temperature control, gas industrial

Temperature control, gas inefficiency explained

Temperature control, gas percent bypass

Temperature control, gas photograph

Temperature control, gas principle

Temperature control, gas theoretical

Temperature control, gas up and down

Temperature for gases

Temperature gas composition

Temperature gas kinetic

Temperature gas scale

Temperature gas solubility

Temperature gas yields

Temperature gas-liquid chromatography

Temperature gradient in the gas

Temperature gradient in the gas phase

Temperature ideal gas law

Temperature of gas product independent with oxygen

Temperature of gas product industrial data

Temperature of gases

Temperature sensitivity of the gas

Temperature sensitivity of the gas phase

Temperature, Heat and Quantitative Laws of Gases

Temperature-Programmed Evolution of Gases (TPE)

Temperature-programmed gas

Temperature-programmed gas chromatography

Temperatures, acid and gas control

Temperatures, acid and gas industrial

Temperatures, industrial catalyst bed input gas

Temperatures, industrial gas dehydration

Temperatures, industrial metallurgical gas

Temperatures, industrial spent acid decomposition gas

The Combined Gas Law Pressure, Volume, and Temperature

The High-Temperature Gas-Cooled Reactor

The Ideal Gas Law Pressure, Volume, Temperature, and Moles

The Ideal Gas Temperature Scale

Thermodynamic and Gas Scales of Temperature

Third catalyst bed input gas temperature

Very-high-temperature gas-cooled reactors

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