ruoyi-api/ruoyi-ngtools/src/main/java/com/ruoyi/ngCalTools/controller/GasController.java

package com.ruoyi.ngCalTools.controller;

// GasController.java

import com.ruoyi.ngCalTools.model.GasProps;
import com.ruoyi.ngCalTools.service.DetailService;
import com.ruoyi.ngCalTools.service.GBT11062Service;
import com.ruoyi.ngCalTools.service.ThermService;
import com.ruoyi.ngCalTools.utils.GasConstants;
import org.springframework.web.bind.annotation.*;

@RestController
@RequestMapping("/NGCalcTools")
public class GasController {


    public ThermService thermService;
    public DetailService detailService;
    public GBT11062Service gbt11062Service;


    @PostMapping  ("/calculate")
    public GasProps calculateProperties(@RequestBody GasProps tempPar) {
           Zcal(tempPar, 0);
return  tempPar;

    }
    public int NG_Cal_Init() {
        //create object for calculating density
        if (null == detailService) {
            return GasConstants.MEMORY_ALLOCATION_ERROR;
        }

        //create object for calculating thermodynamic properties
        if (null == thermService) {
            return GasConstants.MEMORY_ALLOCATION_ERROR;
        }

        return GasConstants.NG_Cal_INITIALIZED;

    }// NG_Cal_Init
    public int NG_Cal_UnInit() {
        // delete the objects (if they exist)
        detailService = null;
        thermService = null;
        return 0;

    }
    public double SOS(GasProps gasProps) {
        // check if library is ready; initialize if necessary 
        if (null == detailService || null == thermService) {
            NG_Cal_UnInit();
            NG_Cal_Init();
        }
        switch (gasProps.dCbtj) {
            case 2:
                gasProps.dPb = 101325;
                gasProps.dTb = 273.15;
                break;
            case 1:
                gasProps.dPb = 101325;
                gasProps.dTb = 288.15;
                break;
            case 0:
                gasProps.dPb = 101325;
                gasProps.dTb = 293.15;
                break;
        }
        detailService.run(gasProps);
        gasProps.dCstar = 0;
        return gasProps.dSOS;
    }

    public double Crit(GasProps gasProps, double dPlenumVelocity)
    {
        //variables local to function 
        double DH, DDH, S, H;
        double tolerance = 1.0;
        double R, P, T, Z;

        int i;

        //check objects for readiness; try to initialize if not 
        if (null == detailService || null == thermService)
        {
            NG_Cal_UnInit();

            if (GasConstants.NG_Cal_INITIALIZED != NG_Cal_Init())
            {

                gasProps.lStatus =GasConstants. MEMORY_ALLOCATION_ERROR; return 0.0;

            }
        }
        switch (gasProps.dCbtj)
        {
            case 2:
                gasProps.dPb = 101325;
                gasProps.dTb = 273.15;
                break;
            case 1:
                gasProps.dPb = 101325;
                gasProps.dTb = 288.15;
                break;
            case 0:
                gasProps.dPb = 101325;
                gasProps.dTb = 293.15;
                break;


        }
        //begin by calculating densities and thermodynamic properties 
        thermService.Run(gasProps, detailService);

        //DH is enthalpy change from plenum to throat; this is our initial guess

        DH = (gasProps.dSOS * gasProps.dSOS - dPlenumVelocity * dPlenumVelocity) / 2.0;

        //trap plenum conditions before we alter the data stucture's contents
        S = gasProps.dS;

        H = gasProps.dH;

        R = gasProps.dRhof;
        P = gasProps.dPf;
        Z = gasProps.dZf;
        T = gasProps.dTf;

        DDH = 10.0;

        for (i = 1; i < GasConstants.MAX_NUM_OF_ITERATIONS; i++)
        {
            thermService.HS_Mode( gasProps, detailService, H - DH, S, true);
            thermService.Run( gasProps, detailService);
            DDH = DH;
            DH = (gasProps.dSOS * gasProps.dSOS - dPlenumVelocity * dPlenumVelocity) / 2.0;
            if (Math.abs(DDH - DH) < tolerance) break;
        }
        gasProps.dCstar = (gasProps.dRhof * gasProps.dSOS) / Math.sqrt(R * P * Z);
        gasProps.dPf = P;
        gasProps.dTf = T;
        thermService.Run(gasProps, detailService);
        gbt11062Service.Run(gasProps );
        return gasProps.dCstar;

    }
    public double Zcal(GasProps gasProps, double dPlenumVelocity)
    {
        if (null == detailService || null == thermService)
        {
            NG_Cal_UnInit();
            if (GasConstants.NG_Cal_INITIALIZED != NG_Cal_Init())
            {
                gasProps.lStatus =GasConstants. MEMORY_ALLOCATION_ERROR; return 0.0;
            }
        }
        switch (gasProps.dCbtj)
        {
            case 2:
                gasProps.dPb = 101325;
                gasProps.dTb = 273.15;
                break;
            case 1:
                gasProps.dPb = 101325;
                gasProps.dTb = 288.15;
                break;
            case 0:
                gasProps.dPb = 101325;
                gasProps.dTb = 293.15;
                break;
        }
        thermService.Run(  gasProps,  detailService);
        gbt11062Service.Run( gasProps);
        return gasProps.dZf;

    }
    double Cperf(GasProps gasProps)
    {

        double k, root, exponent;

        k = gasProps.dKappa; root = 2.0 / (k + 1.0);
        exponent = (k + 1.0) / (k - 1.0);

        return (Math.sqrt(k * Math.pow(root, exponent)));

    }

    double CRi(GasProps gasProps)
    {
        return (Cperf(gasProps) / Math.sqrt(gasProps.dZf));
    }

}