编辑代码

using System;

public class Program
{
    public static void Main(string[] args)
    {
        // 示例输入参数
        float[] parameters = new float[17];
        parameters[0] = 1000.0f;    // hf
        parameters[1] = 1500.0f;    // h_pipe
        parameters[2] = 2000.0f;    // p_case
        parameters[3] = 0.2f;       // fw
        parameters[4] = 0.15f;      // Rp
        parameters[5] = 200.0f;     // qpl
        parameters[6] = 0.1f;       // dco
        parameters[7] = 0.08f;      // dci
        parameters[8] = 0.15f;      // dto
        parameters[9] = 0.12f;      // dti
        parameters[10] = 25.0f;     // tr
        parameters[11] = 100;       // points
        parameters[12] = 0.02f;     // gg
        parameters[13] = 0.018f;    // gw
        parameters[14] = 0.015f;    // go1
        parameters[15] = 1800.0f;   // pb
        parameters[16] = 1500.0f;   // h_pump

        // 管道直径数据
        float[] outerDiameter = { 0.2f, 0.25f };   // do_tube
        float[] innerDiameter = { 0.15f, 0.2f };   // di_tube
        float[] tubeLength = { 2000.0f };          // l_tube

        // 井深度数据
        float[] wellDepths = { 0.0f, 500.0f, 1500.0f };  // hhh
        float[] angles = { 0.0f, 0.1f, 0.2f };           // angle1

        // 调用流体动力学计算
        float[] results = new float[1];
        CalculateHfPwf(parameters, wellDepths, angles, 1, outerDiameter, innerDiameter, tubeLength, results);

        // 输出计算结果
        float calculatedPwf = results[0];
        Console.WriteLine($"Calculated Pwf: {calculatedPwf} psi");
    }

    public static void CalculateHfPwf(float[] pq, float[] hhh, float[] angle1, int tubejs, float[] do_tube, float[] di_tube, float[] l_tube, float[] result)
    {
        float Pwf = 0.0f;
        int ii2, ii3, ii1;
        float ro, ro1, yalitidu;
        float prz, ttz, r5, z1;
        float pav_g, tcz, pcz;
        float h_vertical_r, drt_h, angle, tav_g, z;
        float[] h = new float[200];
        float[] h_vertical = new float[200];
        float[] p = new float[200];
        float[] T = new float[200];
        float[] ttt = new float[20];
        float hf, h_pipe, p_case;
        float fw, Rp, qpl;
        float dci, dco, dti, dto;
        float tr;
        int points;
        float gg, gw, go1;
        float pb, h_well;
        float drt_h1;
        int i, j;
        float h_pump, t_pumpintake;
        float do_rod, di_rod;

        hf = pq[0];
        h_pipe = pq[1];
        p_case = pq[2];
        fw = pq[3];
        Rp = pq[4];
        qpl = pq[5];
        dco = pq[6];
        dci = pq[7];
        dto = pq[8];
        dti = pq[9];
        tr = pq[10];
        points = (int)pq[11];
        gg = pq[12];
        gw = pq[13];
        go1 = pq[14];
        pb = pq[15];
        h_pump = pq[16];

        h_well = hhh[points];
        if (h_well < h_pipe)
            h_pipe = h_well;

        // 计算井底流动压力 Pwf
        hhh[0] = 0;
        h_vertical_r = 0;
        for (j = 1; j < points; j++)
        {
            h_vertical_r += (float)((hhh[j] - hhh[j - 1]) * Math.Sin((double)angle1[j]));
        }

        drt_h1 = 50;
        if (Math.Abs(hf / drt_h1 - Convert.ToInt32(hf / drt_h1)) > 0.01)
        {
            ii1 = Convert.ToInt32(hf / drt_h1) + 1;
            for (i = 0; i < ii1; i++)
            {
                h[i] = i * drt_h1;
            }
            h[ii1] = hf;
        }
        else
        {
            ii1 = Convert.ToInt32(hf / drt_h1 + 0.5);
            for (i = 0; i <= ii1; i++)
            {
                h[i] = drt_h1 * i;
            }
        }

        if (Math.Abs((h_pipe - hf) / drt_h1 - Convert.ToInt32((h_pipe - hf) / drt_h1)) > 0.01)
        {
            ii2 = Convert.ToInt32((h_pipe - hf) / drt_h1) + 1;
            for (i = 1; i < ii2; i++)
            {
                h[ii1 + i] = hf + i * drt_h1;
            }
            h[ii1 + ii2] = h_pipe;
        }
        else
        {
            ii2 = Convert.ToInt32((h_pipe - hf) / drt_h1 + 0.5);
            for (i = 1; i <= ii2; i++)
            {
                h[ii1 + i] = hf + drt_h1 * i;
            }
        }

        if (Math.Abs((h_well - h_pipe) / drt_h1 - Convert.ToInt32((h_well - h_pipe) / drt_h1)) > 0.01)
        {
            ii3 = Convert.ToInt32((h_well - h_pipe) / drt_h1) + 1;
            for (i = 1; i < ii3; i++)
            {
                h[ii1 + ii2 + i] = h_pipe + i * drt_h1;
            }
            h[ii1 + ii2 + ii3] = h_well;
        }
        else
        {
            ii3 = Convert.ToInt32((h_well - h_pipe) / drt_h1 + 0.5);
            for (i = 1; i <= ii3; i++)
            {
                h[ii1 + ii2 + i] = h_pipe + drt_h1 * i;
            }
        }

        h_vertical[0] = 0;
        for (i = 1; i <= ii1 + ii2 + ii3; i++)
        {
            drt_h = h[i] - h[i - 1];
            for (j = 1; j < points; j++)
            {
                if (h[i] >= hhh[j - 1] && h[i] <= hhh[j])
                {
                    angle = angle1[j - 1];
                }
            }
            h_vertical[i] = h_vertical[i - 1] + drt_h * (float)Math.Sin((double)angle);
        }

        if (tubejs == 1)
        {
            dto = do_tube[0];
            dti = di_tube[0];
        }
        else if (tubejs == 2)
        {
            dto = do_tube[1];
            dti = di_tube[1];
        }

        T[ii1 + ii2 + ii3] = Temperature(fw, Rp, qpl, dco, dci, dto, dti, tr, h_vertical[ii1 + ii2 + ii3], h_vertical_r);

        // 井底到尾管处
        for (i = ii1 + ii2 + ii3 - 1; i >= ii1 + ii2; i--)
        {
            T[i] = Temperature(fw, Rp, qpl, dco, dci, dto, dti, tr, h_vertical[i], h_vertical_r);
        }

        // 尾管到泵吸入口
        if (h_pump == h_pipe)
        {
            t_pumpintake = T[ii1 + ii2];
        }

        for (i = ii1 + ii2 - 1; i >= 0; i--)
        {
            T[i] = Temperature(fw, Rp, qpl, dco, dci, dto, dti, tr, h_vertical[i], h_vertical_r);
        }

        p[0] = p_case;

        for (i = 1; i <= ii1; i++)
        {
            if (h[i] <= l_tube[0])
            {
                dto = do_tube[0];
                dti = di_tube[0];
            }
            else
            {
                dto = do_tube[1];
                dti = di_tube[1];
            }

            drt_h = h[i] - h[i - 1];
            tav_g = (T[i - 1] + T[i]) / 2;
            for (j = 1; j < points; j++)
            {
                if (h[i] >= hhh[j - 1] && h[i] <= hhh[j])
                {
                    angle = angle1[j - 1];
                }
            }

            z = 1;
            do
            {
                p[i] = p[i - 1] * (float)Math.Exp(0.03416 * gg * drt_h * (float)Math.Sin((double)angle) / (tav_g + 273) / z);
                pav_g = (p[i - 1] + p[i]) / 2;

                ttt[0] = go1;
                ttt[1] = gg;
                ttt[2] = pav_g;
                ttt[3] = tav_g;
                ttt[4] = Rp;
                ttt[5] = fw;
                ttt[6] = gw;
                ttt[7] = qpl;
                Pvtpara(ttt); // 调用 Pvtpara 方法

                ro1 = ttt[2];
                if (Math.Abs((ro - ro1) / ro) < 0.005)
                {
                    break;
                }
                else
                {
                    ro = (ro + ro1) / 2;
                }
            } while (true);
        }

        for (i = ii1 + 1; i <= ii1 + ii2; i++)
        {
            if (h[i] <= l_tube[0])
            {
                dto = do_tube[0];
                dti = di_tube[0];
            }
            else
            {
                dto = do_tube[1];
                dti = di_tube[1];
            }

            drt_h = h[i] - h[i - 1];
            tav_g = (T[i - 1] + T[i]) / 2;
            for (j = 1; j < points; j++)
            {
                if (h[i] >= hhh[j - 1] && h[i] <= hhh[j])
                {
                    angle = angle1[j - 1];
                }
            }

            ro = 1000;
            do
            {
                p[i] = p[i - 1] + ro * 9.8f * drt_h * (float)Math.Sin((double)angle) / 100000;
                pav_g = (p[i - 1] + p[i]) / 2;

                ttt[0] = go1;
                ttt[1] = gg;
                ttt[2] = pav_g;
                ttt[3] = tav_g;
                ttt[4] = Rp;
                ttt[5] = fw;
                ttt[6] = gw;
                ttt[7] = qpl;
                Pvtpara(ttt); // 调用 Pvtpara 方法

                ro1 = ttt[2];
                if (Math.Abs((ro - ro1) / ro) < 0.005)
                {
                    break;
                }
                else
                {
                    ro = (ro + ro1) / 2;
                }
            } while (true);
        }

        Pwf = p[ii1 + ii2 + ii3];
        result[0] = Pwf;
    }

    // Pvtpara 方法的声明
    public static void Pvtpara(float[] ttt)
    {
        // 在这里添加 Pvtpara 方法的具体实现
        // 可以根据 ttt 中的参数计算油气物性参数
    }

    // Temperature 方法的声明
    public static float Temperature(float fw, float Rp, float qpl, float dco, float dci, float dto, float dti, float tr, float h_vertical, float h_vertical_r)
    {
        // 在这里添加 Temperature 方法的具体实现
        // 根据给定的参数计算温度
        return 0.0f; // 这里需要替换为实际的返回值
    }
}