import { MeasureKind } from "./enums";
export interface Measure {
    value: number;
    units?: string;
    error?: number;
    greaterOrLess?: MeasureKind;
}
export interface MeasureRange {
    min: Measure;
    max: Measure;
    includeMin?: boolean;
    includeMax?: boolean;
}
export interface INCHIProps {
    name: string;
    formula: string;
    CAS: string;
    molecularWeight: number;
    inchiString: string;
    inchiKey: string;
}
export interface TemperaturePressureCombo {
    temperature: Measure | MeasureRange;
    pressure: Measure | MeasureRange;
}
/**
 * Vapor pressure `Ps` is calculated by `Ps = exp(C1 + C2/T + C3 ln(T) + C4*T^C5)`, where `Ps` is in `Pa` and `T` is in `K`.
 */
export interface DIPPRVaporPressureProps {
    name: string;
    formula: string;
    CAS: string;
    C1: number;
    C2: number;
    C3: number;
    C4?: number;
    C5?: number;
    minimumTemperature: number;
    maximumTemperature: number;
    pressureAtMinimumTemperature: number;
    pressureAtMaximumTemperature: number;
}
/**
 * - Except for o-terphenyl and water, liquid density is calculated by `rho = C1/(C2^[1 + (1 – T/C3)^C4])` where `rho` is in `mol/dm3` and `T` is in `K`.
 * - The pressure is equal to the vapor pressure for pressures greater than 1 atm and equal to 1 atm when the vapor pressure is less than 1 atm.
 * - Equation used for the limited temperature ranges as noted for o-terphenyl and water, is `rho = C1 + C2*T + C3*T^2 + C4*T^3`.
 * - Equation used for water, is `rho = C1 + C2*(tau^1/3) + C3*(tau^2/3) + C4*(tau^5/3) + C5*(tau^16/3) + C6*(tau^43/3) + C7*(tau^110/3)` where `tau = 1 − T/TC`, and `TC = critical temperature (647.096 K)`.
 */
export interface DIPPRDensityProps {
    name: string;
    formula: string;
    CAS: string;
    molecularWeight: number;
    C1: number;
    C2: number;
    C3: number;
    C4: number;
    C5?: number;
    C6?: number;
    C7?: number;
    minimumTemperature: number;
    maximumTemperature: number;
    densityAtMinimumTemperature: number;
    densityAtMaximumTemperature: number;
}
/**
 * The liquid thermal conductivity is calculated by `k = C1 + C2*T + C3*T^2 + C4*T^3 + C5*T^4`
 * where `k` is the thermal conductivity in `W/(m∙K)` and `T` is the temperature in `K`.
 * Thermal conductivities are at either `1 atm` or the vapor pressure, whichever is higher.
 */
export interface DIPPRThermalConductivityProps {
    name: string;
    formula: string;
    CAS: string;
    molecularWeight: number;
    C1?: number;
    C2?: number;
    C3?: number;
    C4?: number;
    C5?: number;
    minimumTemperature?: number;
    maximumTemperature?: number;
    thermalConductivityAtMinimumTemperature?: number;
    thermalConductivityAtMaximumTemperature?: number;
}
export interface DIPPRCriticalConstantAndAcentricFactorProps {
    name: string;
    formula: string;
    CAS: string;
    molecularWeight: number;
    criticalTemperature: number;
    criticalPressure: number;
    criticalVolume: number;
    criticalCompressibilityFactor: number;
    acentricFactor: number;
}
export interface DIPPRVaporThermalConductivityProps {
    name: string;
    formula: string;
    CAS: string;
    molecularWeight: number;
    C1: number;
    C2: number;
    C3?: number;
    C4?: number;
    minimumTemperature: number;
    maximumTemperature: number;
    thermalConductivityAtMinimumTemperature: number;
    thermalConductivityAtMaximumTemperature: number;
}