The Antoine equation for methane looks like: log10(P) = 6.69561 - 405.420 / (T +267.777). P is in mm Hg, T is in degrees C within temperature ranges -181 < T < -152.
The Nation Institute of Standards and Technology web site has the figures Note there are three coefficients - the Antoine equation gives a reasonable fit to vapour pressure.
Because solutions of quadratic equation depend solely on these three constants.
The equation of a capacitor is ...dv/dt = i/c... meaning that the rate of change of voltage with respect to time is proportional to current and inversely proportional to capacitance.If you build a circuit with a resistor r in series with a capacitor c charging to an ultimate voltage V from an initial voltage v=0 at t=0, then you can solve the differential equation (solution steps not included) and produce a generalized equation ...vt = V (1 - e(-t/rc) )... In the case of two time constants, you reach a value of 86% of charge voltage.
there are three types of constants in COBOL 1. numeric literals 2. figurative constants 3. non-numeric literals
constants are values that does not chnage through out the program exceution..
Antoine equations can only be used with pure components, not with mixtures. Considering ideal behaviour, the vapor pressure of a mixture would be P = P1*x1 + P2*x2 (Raoult's law), where P1 and P2 are the vapor pressures of the two components and x1 and x2 their molar fractions
The Antoine coefficients for isobutane in the temperature range of -83°C to 7°C are A=13.8254, B=2181.79, C=248.870. These coefficients are valid for Antoine's equation in the form of ln(Psat [kPa]) = A - B/(T[°C] + C). (Source Introduction to Chemical Engineering Thermodynamics 7th ed by J.M. Smith, p.682)
Actual vapor pressure can be calculated using the Antoine equation, which is a function of temperature and constants specific to the substance of interest. The equation is: ln(P) = A - (B / (T + C)), where P is the actual vapor pressure, T is the temperature in Kelvin, and A, B, and C are substance-specific constants.
{| |- | log10 Pvap = A - [B / (T °C + C)] barSUSTANCIA FORMULA A BC1-Buteno C4H8 3.91780 908.800 238.540 cis-2-Buteno C4H8 4.00958 967.320 237.873 trans-2-Buteno C4H8 4.00827 967.500 240.840 |} {| |- | log10 Pvap = A - [B / (T °C + C)] barSUSTANCIA FORMULA A BC1-Buteno C4H8 3.91780 908.800 238.540 cis-2-Buteno C4H8 4.00958 967.320 237.873 trans-2-Buteno C4H8 4.00827 967.500 240.840 |}
The Antoine coefficient for mercury is a set of temperature-dependent constants used in the Antoine equation to describe the vapor pressure of mercury as a function of temperature. These coefficients are specific to mercury and are commonly used in chemical engineering and thermodynamics to model and predict the behavior of mercury in various processes.
Antoine Coefficients for Nitric acid are A=6.6368 B=1.406 C= -52.15 range 274/376 (K) reference :- Vapour Pressure and Antoine Constants for Nitrogen Containing compounds
An equation is linear when it contains only variables of degree 1 and constants. ALL linear equations will be of the form: a1x1+a2x2+a3x3+...+anxn=c where an and c are constants.
It is y = a*b^x where a and b are constants.
It is the solution of a differential equation without there being any restrictions on the variables (No boundary conditions are given). Presence of arbitrary constants indicates a general solution, the number of arbitrary constants depending on the order of the differential equation.
Methane + Oxygen > Carbon (soot) + Water
CH4
methane + oxygen -> carbon dioxide + water 2 Methane molecules plus 4 Oxygen molecules gives 2 molecules of Carbon dioxide plus 4 Water molecules.