Beispiel #1
0
    private uint capacity()
    {
        uint ret = CoolPropPINVOKE.StringVector_capacity(swigCPtr);

        return(ret);
    }
Beispiel #2
0
 public string name()
 {
     string ret = CoolPropPINVOKE.AbstractState_name(swigCPtr);
     if (CoolPropPINVOKE.SWIGPendingException.Pending) throw CoolPropPINVOKE.SWIGPendingException.Retrieve();
     return ret;
 }
Beispiel #3
0
 public double p_triple()
 {
     double ret = CoolPropPINVOKE.AbstractState_p_triple(swigCPtr);
     if (CoolPropPINVOKE.SWIGPendingException.Pending) throw CoolPropPINVOKE.SWIGPendingException.Retrieve();
     return ret;
 }
Beispiel #4
0
 public double isothermal_compressibility()
 {
     double ret = CoolPropPINVOKE.AbstractState_isothermal_compressibility(swigCPtr);
     if (CoolPropPINVOKE.SWIGPendingException.Pending) throw CoolPropPINVOKE.SWIGPendingException.Retrieve();
     return ret;
 }
Beispiel #5
0
 public double melting_line(int param, int given, double value)
 {
     double ret = CoolPropPINVOKE.AbstractState_melting_line(swigCPtr, param, given, value);
     if (CoolPropPINVOKE.SWIGPendingException.Pending) throw CoolPropPINVOKE.SWIGPendingException.Retrieve();
     return ret;
 }
Beispiel #6
0
 public double acentric_factor()
 {
     double ret = CoolPropPINVOKE.AbstractState_acentric_factor(swigCPtr);
     if (CoolPropPINVOKE.SWIGPendingException.Pending) throw CoolPropPINVOKE.SWIGPendingException.Retrieve();
     return ret;
 }
Beispiel #7
0
 public void ideal_curve(string type, DoubleVector T, DoubleVector p)
 {
     CoolPropPINVOKE.AbstractState_ideal_curve(swigCPtr, type, DoubleVector.getCPtr(T), DoubleVector.getCPtr(p));
     if (CoolPropPINVOKE.SWIGPendingException.Pending) throw CoolPropPINVOKE.SWIGPendingException.Retrieve();
 }
Beispiel #8
0
 public double dalphar_dTau()
 {
     double ret = CoolPropPINVOKE.AbstractState_dalphar_dTau(swigCPtr);
     if (CoolPropPINVOKE.SWIGPendingException.Pending) throw CoolPropPINVOKE.SWIGPendingException.Retrieve();
     return ret;
 }
Beispiel #9
0
 public double first_partial_deriv(parameters Of, parameters Wrt, parameters Constant)
 {
     double ret = CoolPropPINVOKE.AbstractState_first_partial_deriv(swigCPtr, (int)Of, (int)Wrt, (int)Constant);
     if (CoolPropPINVOKE.SWIGPendingException.Pending) throw CoolPropPINVOKE.SWIGPendingException.Retrieve();
     return ret;
 }
Beispiel #10
0
 internal SsatSimpleState(global::System.IntPtr cPtr, bool cMemoryOwn) : base(CoolPropPINVOKE.SsatSimpleState_SWIGUpcast(cPtr), cMemoryOwn)
 {
     swigCPtr = new global::System.Runtime.InteropServices.HandleRef(this, cPtr);
 }
Beispiel #11
0
 public double conductivity()
 {
     double ret = CoolPropPINVOKE.AbstractState_conductivity(swigCPtr);
     if (CoolPropPINVOKE.SWIGPendingException.Pending) throw CoolPropPINVOKE.SWIGPendingException.Retrieve();
     return ret;
 }
Beispiel #12
0
 public void Reverse()
 {
     CoolPropPINVOKE.StringVector_Reverse__SWIG_0(swigCPtr);
 }
Beispiel #13
0
 public StringVector() : this(CoolPropPINVOKE.new_StringVector__SWIG_0(), true)
 {
 }
Beispiel #14
0
 private void reserve(uint n)
 {
     CoolPropPINVOKE.StringVector_reserve(swigCPtr, n);
 }
Beispiel #15
0
 public virtual SS get_reducing_state()
 {
     SS ret = new SS(CoolPropPINVOKE.AbstractState_get_reducing_state(swigCPtr), false);
     if (CoolPropPINVOKE.SWIGPendingException.Pending) throw CoolPropPINVOKE.SWIGPendingException.Retrieve();
     return ret;
 }
Beispiel #16
0
 public double first_saturation_deriv(parameters Of1, parameters Wrt1)
 {
     double ret = CoolPropPINVOKE.AbstractState_first_saturation_deriv(swigCPtr, (int)Of1, (int)Wrt1);
     if (CoolPropPINVOKE.SWIGPendingException.Pending) throw CoolPropPINVOKE.SWIGPendingException.Retrieve();
     return ret;
 }
Beispiel #17
0
 public SS get_state(string state)
 {
     SS ret = new SS(CoolPropPINVOKE.AbstractState_get_state(swigCPtr, state), false);
     if (CoolPropPINVOKE.SWIGPendingException.Pending) throw CoolPropPINVOKE.SWIGPendingException.Retrieve();
     return ret;
 }
Beispiel #18
0
 public double first_two_phase_deriv_splined(parameters Of, parameters Wrt, parameters Constant, double x_end)
 {
     double ret = CoolPropPINVOKE.AbstractState_first_two_phase_deriv_splined(swigCPtr, (int)Of, (int)Wrt, (int)Constant, x_end);
     if (CoolPropPINVOKE.SWIGPendingException.Pending) throw CoolPropPINVOKE.SWIGPendingException.Retrieve();
     return ret;
 }
Beispiel #19
0
 public virtual bool has_melting_line()
 {
     bool ret = CoolPropPINVOKE.AbstractState_has_melting_line(swigCPtr);
     if (CoolPropPINVOKE.SWIGPendingException.Pending) throw CoolPropPINVOKE.SWIGPendingException.Retrieve();
     return ret;
 }
Beispiel #20
0
 public SWIGTYPE_p_std__vectorT_std__string_t fluid_names()
 {
     SWIGTYPE_p_std__vectorT_std__string_t ret = new SWIGTYPE_p_std__vectorT_std__string_t(CoolPropPINVOKE.AbstractState_fluid_names(swigCPtr), true);
     if (CoolPropPINVOKE.SWIGPendingException.Pending) throw CoolPropPINVOKE.SWIGPendingException.Retrieve();
     return ret;
 }
Beispiel #21
0
 public double isobaric_expansion_coefficient()
 {
     double ret = CoolPropPINVOKE.AbstractState_isobaric_expansion_coefficient(swigCPtr);
     if (CoolPropPINVOKE.SWIGPendingException.Pending) throw CoolPropPINVOKE.SWIGPendingException.Retrieve();
     return ret;
 }
Beispiel #22
0
 public double fugacity_coefficient(uint i)
 {
     double ret = CoolPropPINVOKE.AbstractState_fugacity_coefficient(swigCPtr, i);
     if (CoolPropPINVOKE.SWIGPendingException.Pending) throw CoolPropPINVOKE.SWIGPendingException.Retrieve();
     return ret;
 }
Beispiel #23
0
 public double keyed_output(parameters key)
 {
     double ret = CoolPropPINVOKE.AbstractState_keyed_output(swigCPtr, (int)key);
     if (CoolPropPINVOKE.SWIGPendingException.Pending) throw CoolPropPINVOKE.SWIGPendingException.Retrieve();
     return ret;
 }
Beispiel #24
0
 public double gas_constant()
 {
     double ret = CoolPropPINVOKE.AbstractState_gas_constant(swigCPtr);
     if (CoolPropPINVOKE.SWIGPendingException.Pending) throw CoolPropPINVOKE.SWIGPendingException.Retrieve();
     return ret;
 }
Beispiel #25
0
 public SWIGTYPE_p_std__vectorT_CoolPropDbl_t mole_fractions_vapor()
 {
     SWIGTYPE_p_std__vectorT_CoolPropDbl_t ret = new SWIGTYPE_p_std__vectorT_CoolPropDbl_t(CoolPropPINVOKE.AbstractState_mole_fractions_vapor(swigCPtr), true);
     if (CoolPropPINVOKE.SWIGPendingException.Pending) throw CoolPropPINVOKE.SWIGPendingException.Retrieve();
     return ret;
 }
Beispiel #26
0
 public virtual SWIGTYPE_p_std__vectorT_CoolPropDbl_t get_mole_fractions()
 {
     SWIGTYPE_p_std__vectorT_CoolPropDbl_t ret = new SWIGTYPE_p_std__vectorT_CoolPropDbl_t(CoolPropPINVOKE.AbstractState_get_mole_fractions(swigCPtr), false);
     if (CoolPropPINVOKE.SWIGPendingException.Pending) throw CoolPropPINVOKE.SWIGPendingException.Retrieve();
     return ret;
 }
Beispiel #27
0
 public phases phase()
 {
     phases ret = (phases)CoolPropPINVOKE.AbstractState_phase(swigCPtr);
     if (CoolPropPINVOKE.SWIGPendingException.Pending) throw CoolPropPINVOKE.SWIGPendingException.Retrieve();
     return ret;
 }
Beispiel #28
0
 public PED get_phase_envelope_data()
 {
     PED ret = new PED(CoolPropPINVOKE.AbstractState_get_phase_envelope_data(swigCPtr), false);
     if (CoolPropPINVOKE.SWIGPendingException.Pending) throw CoolPropPINVOKE.SWIGPendingException.Retrieve();
     return ret;
 }
Beispiel #29
0
 public double rhomass_reducing()
 {
     double ret = CoolPropPINVOKE.AbstractState_rhomass_reducing(swigCPtr);
     if (CoolPropPINVOKE.SWIGPendingException.Pending) throw CoolPropPINVOKE.SWIGPendingException.Retrieve();
     return ret;
 }
Beispiel #30
0
    private uint size()
    {
        uint ret = CoolPropPINVOKE.StringVector_size(swigCPtr);

        return(ret);
    }