Unzip the package, put the content into any directory you like and add it to the MATLAB path, e.g. with the following command (inside Matlab!)
addpath('my_favorite_directory')
The following table shows all user level routines of the WATER95 package. All parameters and results are in standard SI units.
| Name | Interface | Purpose |
|---|---|---|
| saturationPressure | [pS, rhop, rhopp] = saturationPressure(T) | returns saturation pressure and densities of the liquid and vapor phase as functions of T |
| pressure | [p, x] = pressure(rho, T) | returns pressure and dryness fraction as functions of rho and T |
| enthalpy | [h, x] = enthalpy(rho, T) | returns specific enthalpy and dryness fraction as functions of rho and T |
| entropy | [s, x] = entropy(rho, T) | returns specific entropy and dryness fraction as functions of rho and T |
| heatCapacityV | [cV, x] = heatCapacityV(rho, T) | returns specific isochoric heat capacity and dryness fraction as functions of rho and T |
| heatCapacityP | [cP, x] = heatCapacityP(rho, T) | returns specific isobaric heat capacity and dryness fraction as functions of rho and T |
| soundVelocity | [w, x] = soundVelocity(rho, T) | returns sound velocity and dryness fraction as functions of rho and T |
| saturationTemperature | T = saturationTemperature(p) | returns the saturation temperature as function of p |
| density | rho = density(p, T) | returns the density as function of p and T |
| temperature | [T, x] = temperature(p, rho) | returns temperature and dryness fraction as functions of p and rho |
| temperaturePS | [T, x] = temperaturePS(p, s) | returns temperature and dryness fraction as functions of p and s |
| temperatureRS | T = temperatureRS(rho, s) | returns the temperature as function of rho and s |
| densityTX | rho = densityTX(T, x) | returns the density of wet steam given by temperature and dryness fraction |
| drynessFractionTS | x = drynessFractionTS(T, s) | returns the dryness fraction as function of T and s |
| isentropic | [pi,vi,Ti,si,xi] = isentropic(p1, v1, v2, N, logFlag) | returns values of p, v, T, s, x along an isentropic going from (p1,v1) to v2 |
| isobaric | [pi,vi,Ti,si,xi] = isobaric(p1, v1, v2, N, logFlag) | returns values of p, v, T, s, x along an isobaric going from (p1,v1) to v2 |
| isochoric | [pi,vi,Ti,si,xi] = isochoric(p1, v1, p2, N) | returns values of p, v, T, s, x along an isochoric going from (p1,v1) to p2 |
| isothermal | [pi,vi,Ti,si,xi] = isothermal(p1, v1, v2, N, NP,logFlag) | returns values of p, v, T, s, x along an isothermal going from (p1,v1) to v2 |
| isentropicTPP | [pi,vi,Ti,si,xi] = isentropicTPP(T1, p1, p2, N, logFlag) | returns values of p, v, T, s, x along an isentropic going from (T1,p1) to p2 |
| isothermalTPP | [pi,vi,Ti,si,xi] = isothermalTPP(T1, p1, p2, N, NP, logFlag) | returns values of p, v, T, s, x along an isothermal going from (T1,p1) to p2 |
| clausiusRankineCornerPoints | [pi,vi,Ti,si,xi,hi] = clausiusRankineCornerPoints(T1, p1, p2) | returns corner points of a Clausius-Rankine cycle defined by p1, p2 and T1 |
| efficiencyCR | [eta rW] = efficiencyCR(T1, p1, p2) | returns the efficiency eta and the work efficiency rW for a Clausius-Rankine process |
| clausiusRankine | [pi,vi,Ti,si,xi, N] = clausiusRankine(T1, p1, p2, logFlag, N) | returns points along a Clausius-Rankine cycle defined by p1, p2 and T1 |
| plotPVandTS | plotPVandTS(pi,vi,Ti,si, N) | plots a p-v and a T-s diagram for the given data |
| plotIsothermes | plotIsothermes() | plots a semilog p-v-diagram with isothermes for several (fixed) Ts |
| plotSaturationValues | plotSaturationValues() | plots diagrams of pS(T), rho(T), h(T) and s(T) on the saturation curve |
| plotIsochore | plotIsochore(rho, Tmax, Tmin) | plots a p-T diagram of an isochore for given rho from Tmin to Tmax |
| plotIsochoreDisplay | plotIsochoreDisplay() | plots p-T diagrams of isochores for several (fixed) rhos |
| plotPhaseDiagram | plotPhaseDiagram() | plots the phase boundaries in a p-T diagram |
| getHotSteamTable | [p, T, v, h, s] = getHotSteamTable() | returns a hot steam table with a range of useful values |
| getWetSteamTable | [T, p, vp, vpp, hp, hpp, sp, spp] = getWetSteamTable() | returns a wet steam table with a range of useful values |
| getWaterTable | [p, T, v, h, s] = getWaterTable() | returns a water table with a range of useful values |
| publishSaturationTable | publishSaturationTable(T, p, vp, vpp, hp, hpp, sp, spp) | creates a HTML document displaying the given values in table form |
| publishWaterTable | publishWaterTable(p, T, v, h, s, outfile, title) | creates a HTML document displaying the given values in table form |
| getCriticalValues | [Tc rhoc] = getCriticalValues() | returns the critical values of T and rho |
| getTriplePointTemperature | Tt = getTriplePointTemperature() | returns the temperature at the triple point |
| celsiusToKelvin | T = celsiusToKelvin(t) | converts temperatures from Celsius to Kelvin |
| vectorize1d | Y = vectorize1d(func, A) | applies the scalar function func(a) to the array A |
| vectorize2d | Y = vectorize2d(func, A, B) | applies the scalar function func(a,b) to the arrays A, B |
| getSecondResult | y = getSecondResult(func, x1 [, x2]) | returns the second result of a function with one or two output values |
| getThirdResult | y = getThirdResult(func, x1 [, x2]) | returns the third result of a function with one or two output values |