References

ORC{T<:Real} <: ThermoCycleProblem

Defines an Organic Rankine Cycle (ORC) problem with thermodynamic and design parameters specified in Kelvin and dimensionless efficiencies.

Fields

• fluid::EoSModel: Equation of State (EoS) model representing the working fluid.
• z::AbstractVector{T}: Mole fraction composition vector of the working fluid.
• T_evap_in::T: Inlet temperature of the evaporator [K].
• T_evap_out::T: Outlet temperature of the evaporator [K].
• ΔT_sh::T: Degree of superheating at the expander inlet [K].
• T_cond_in::T: Inlet temperature of the condenser [K].
• T_cond_out::T: Outlet temperature of the condenser [K].
• ΔT_sc::T: Degree of subcooling at the pump inlet [K].
• η_pump::T: Isentropic efficiency of the pump [-].
• η_expander::T: Isentropic efficiency of the expander [-].
• pp_evap::T: Minimum temperature difference (pinch point) at the evaporator [K].
• pp_cond::T: Minimum temperature difference (pinch point) at the condenser [K].

    ORCEconomizer{T<:Real} <: ThermoCycleProblem

Defines an Organic Rankine Cycle (ORC) configuration with an economiser (regenerative heat exchanger), extending the base ORC problem with a specified effectiveness.

Fields

• orc::ORC{T}: Base ORC system definition containing the thermodynamic parameters.
• ϵ::T: Effectiveness of the economiser (regenerator) [-].

SolutionState - A struct to hold the solution state of the nonlinear solver.

• x::Vector{T}: The solution vector.
• f_calls::I: The number of function calls made during the solving process.
• iterations::I: The number of iterations taken to converge.
• residuals::Vector{T}: The residuals at the solution.
• lb::Vector{T}: The lower bounds used in the solver.
• ub::Vector{T}: The upper bounds used in the solver.
• autodiff::Bool: A flag indicating whether automatic differentiation was used.
• fd_order::I: The order of finite difference used if autodiff is false.
• lenx::T: The final change in the solution vector.
• lenf::T: The final change in the residuals.
• soltype::Symbol: A symbol indicating the type of cycle (:unknown,:subcritical,:transcritical). This will be updated with the cycle type after solving.

Struct for solver and system paramters N - hex discrtization (incase of mixtures) internal_pinch - to check if pinch point was met in two-phase

COP(prob::ThermoCycleGlides.ThermoCycleProblem, sol::SolutionState) -> Float64

Computes the coefficient of performance (COP) of a thermodynamic cycle given the problem definition and its corresponding solution state.

Arguments

• prob::ThermoCycleGlides.ThermoCycleProblem: The thermodynamic cycle problem containing fluid models, boundary conditions, and component parameters.
• sol::SolutionState: The solution state object containing the converged state variables (x), residuals, and convergence information.

generate_box_solve_bounds(prob::HeatPump) -> lb, ub Generates lower and upper bounds for the heat pump problem based on its parameters.

optimize(prob::ThermoCycleProblem; kwargs...)

Its goal is to find the optimal subcooling and superheating values that maximize the cycle performance (COP or ORC -efficiency).

This should return the optimized cycle struct and the result from Metaheuristics

Plots TS diagram

Function that gives specific power ratings for HP by fixing outlet power of compressor to equal 1.

Function that gives specific power ratings for HP by fixing outlet power of compressor to equal 1.

Function that gives specific power ratings for ORC by fixing outlet power of expander to equal 1.

show_parameters(prob::ORC) prints parameters in REPL

Solves for pressure values in HP and ORC cycles for the given glide and problem parameters. 
Define those problems in the respective structs. 
For now the default box-nonlinear solver is newton-raphson, but this can be changed to other solvers in the future.

η(prob::ThermoCycleGlides.ThermoCycleProblem, sol::SolutionState) -> Float64

Computes the thermal efficiency of a thermodynamic cycle given a problem definition and its corresponding solution state.

Arguments

• prob::ThermoCycleGlides.ThermoCycleProblem: The thermodynamic cycle problem containing fluid properties, boundary conditions, and component parameters.
• sol::SolutionState: The solution state object containing the converged state variables (x), residuals, and convergence information.

Returns

• Float64: The computed cycle efficiency, defined as the ratio of net work output to heat input.

Notes

This method acts as a wrapper that extracts the solution vector x from sol and calls the lower-level η(prob, x) implementation.

p[1] -> condensor pressure p[2] -> evaporator pressure