Table 1 Equations of the thermal fluid properties.
From: Multiobjective design optimization of parabolic trough collectors
Type | Fluid | Property equation | T (K) |
|---|---|---|---|
Liquidsa | Pressurized watera | \({c}_{p}=0.01755{ T}^{2}-11.15 T+5931\) (11) \(\kappa =-4.9\times {10}^{-6} {T}^{2}+0.00389 T-0.098\) (12) \(\rho =-0.00225 {T}^{2}+0.895 T+928\) (13) \(\mu =1.6\times {10}^{-8} {T}^{2}-1.52\times {10}^{-5} T+0.00371\) (14) | 300–550 |
Therminol VP-1a | \({c}_{p}=1.058\times {10}^{-3} {T}^{3}-0.01458 {T}^{2}+9.192 T-156\) (15) \(\kappa =-8.7\times {10}^{-24}{T}^{3}-1.786\times {10}^{-7} {T}^{2}+1.357\times {10}^{-5} T+0.147\) (16) \(\rho =-2.25\times {10}^{-6} {T}^{3}+0.002511 {T}^{2}-1.746 T+1405\) (17) \(\mu =7.542\times {10}^{-13} {T}^{4}-1.688\times {10}^{-9} {T}^{3}+1.403\times {10}^{-6} {T}^{2}-0.0005154 T+0.07097\) (18) | 300–580 | |
Molten solar salt33 | \({c}_{p}=1443+0.172 (T-273.15)\) (19) \(\kappa =0.443+1.9\times {10}^{-4}(T-273.15)\) (20) \(\rho =2090-0.636 (T-273.15)\) (21) \(\mu =2.2714\times {10}^{-2}-1.2\times {10}^{-4}\left(T-273.15\right)+2.281\times {10}^{-7}{\left(T-273.15\right)}^{2}-1.474\times {10}^{-10}{\left(T-273.15\right)}^{3}\) (22) | 533–873 | |
Sodium33 | \({c}_{p}=1658.2-0.8479T+4.4541\times {10}^{-4} {T}^{2}-2.9926\times {10}^{6} {T}^{-2}\)(23) \(\kappa =124.67-0.11381 T+5.5226\times {10}^{-5} {T}^{2}-1.1842\times {10}^{-8} {T}^{3}\) (24) \(\rho =219+275.32\left(1-\frac{T}{2503.7}\right)+511.58{\left(1-\frac{T}{2503.7}\right)}^{0.5}\) (25) \(\mu =Exp\left(-6.4406-0.3958 ln\left(T\right)+\frac{556.835}{T}\right)\) (26) | 371–1255 | |
Syltherm 80015 | \({c}_{p}=1.7075 T+1574.3\) (27) \(\kappa =0.000188 T+0.138769\) (28) \(\rho =-0.001 {T}^{2}-0.5325 T+919.01\) (29) \(\mu =26.67122 {T}^{-1.917}\) (30) | 425–630 | |
Gases | Aira | \({c}_{p}=1.573\times {10}^{-10} {T}^{4}-5.773\times {10}^{-7} {T}^{3}+0.0006741 {T}^{2}-0.09144 T+1002\) (31) \(\kappa =9.518\times {10}^{-12} {T}^{3}-3.695\times {10}^{-8} {T}^{2}+8.724\times {10}^{-5} T+0.01312\) (32) \(\rho =7.051\times {10}^{-13} {T}^{4}-2.875\times {10}^{-9} {T}^{3}+4.557\times {10}^{-6} {T}^{2}-0.003584 T+1.505\) (33) \(\mu =-3.105\times {10}^{-22} {T}^{6}+1.49\times {10}^{-18} {T}^{5}-2.869\times {10}^{-15} {T}^{4}+2.833\times {10}^{-12} {T}^{3}-1.521\times {10}^{-9} {T}^{2}+4.527\times {10}^{-7} T-3.054\times {10}^{-5}\) (34) | 300–1300 |
Carbon dioxide33 | \({c}_{p}=651+0.918 T-3.32\times {10}^{-4} {T}^{2}\) (35) \(\kappa =-1.1\times {10}^{-2}+9.74\times {10}^{-5} T-1.57\times {10}^{-8} {T}^{2}\) (36) \(\rho =\frac{P}{{R}_{C{O}_{2}} T}\) (37) \(\mu =5.94\times {10}^{-7}+5.3\times {10}^{-8} T-1.23\times {10}^{-11}{T}^{2}\) (38) | 300–1300 | |
Helium33 | \({c}_{p}=5183+8.97\times {10}^{-3} T-2.58\times {10}^{-6} {T}^{2}\) (39) \(\kappa =7.08\times {10}^{-2}+3.33\times {10}^{-4} T-3.91\times {10}^{-8} {T}^{2}\) (40) \(\rho =\frac{P}{{R}_{He} T}\) (41) \(\mu =8.64\times {10}^{-6}+4.23\times {10}^{-8} T-4.7\times {10}^{-12} {T}^{2}\) (42) | 300–1300 | |
Hydrogen33 | \({c}_{p}=14994-1.72 T+1.72\times {10}^{-3} {T}^{2}\) (43) \(\kappa =5.94\times {10}^{-2}+4.32\times {10}^{-4} T+3.6\times {10}^{-8} {T}^{2}\) (44) \(\rho =\frac{P}{{R}_{H2} T}\) (45) \(\mu =3.69\times {10}^{-6}+1.97\times {10}^{-8} T-3.08\times {10}^{-12} {T}^{2}\) (46) | 300–1000 |