| Real[4] | par_c_1 | (1/0.1e5)*{-1, 0, 0, 1} | control gains, {u, p_1, p_2, p_3} |
| Real | par_c_2 | 0 | control signal for par_c_1*{u, p_1, p_2, p_3} = 0 |
| Real | par_dyn_1 | 1e6 | control signal gain |
| Real | par_dyn_2 | -1e6 | state gain |
| Real | par_dyn_3 | 0 | initial state |
| Real | par_dyn_4 | -1/10e-3 | minimal der(state) value |
| Real | par_dyn_5 | 1/10e-3 | maximal der(state) value |
| Real[2] | par_stat_1 | {0, 1} | positions assignment |
| Real[2] | par_stat_2 | {0.5, 0.5} | coverage parameter for state < p_x[i] |
| Real[2] | par_stat_3 | {0.5, 0.5} | coverage parameter for state > p_x[i] |
| Real[2] | par_res_1 | 313.15*{1, 1} | temperature |
| Real[2] | par_res_2 | 1.393e-6*{1, 1} | mass proportion of undissolved air to total mass of mixture |
| Real[2] | par_res_3 | 1e6*{1, 1} | nominal effort |
| Real[2] | par_res_4 | 1e-3*{1, 1} | nominal flow |
| Real[2] | par_res_5 | 0.5e5*{1, 1} | reference pressure difference |
| Real[2] | par_res_6 | 0.5e-3*{1, 1} | reference volume flow |
| Real[2] | par_res_7 | 854.307*{1, 1} | reference density |
| Real[2] | par_res_8 | 2*{1, 1} | volume flow exponent for resistance calculation |
| Real[2] | par_res_9 | 1e-2*par_res_3./par_res_4 | minimal resistance |
| Real[2] | par_res_10 | 1e6*par_res_3./par_res_4 | maximal resistance |
| Integer[2] | par_res_11 | 2*{1, 1} | constitutive equation causality, par_res_5=1(effort out), par_res_5=2(flow out) |