gas model: split up gas compressibility into a file of its own

The gas compressibility is such a specialized thing that I really prefer
having it separate.

This keeps Robert's Redlich-Kwong equation as-is, but let's experiment
with other models soon...

Signed-off-by: Linus Torvalds <torvalds@linux-foundation.org>
Signed-off-by: Dirk Hohndel <dirk@hohndel.org>

1 files changed, 0 insertions, 43 deletions

diff --git a/subsurface-core/dive.c b/subsurface-core/dive.c
index 4108c0942..083767582 100644
--- a/subsurface-core/dive.c
+++ b/subsurface-core/dive.c
@@ -846,49 +846,6 @@ static void update_min_max_temperatures(struct dive *dive, temperature_t tempera
 	}
 }
 
-/*
- * This gives an interative solution of hte Redlich-Kwong equation for the compressibility factor
- * according to https://en.wikipedia.org/wiki/Redlich–Kwong_equation_of_state
- * in terms of the reduced temperature T/T_crit and pressure p/p_crit.
- *
- * Iterate this three times for good results in our pressur range.
- *
- */
-
-double redlich_kwong_equation(double t_red, double p_red, double z_init)
-{
-	return (1.0/(1.0 - 0.08664*p_red/(t_red * z_init)) -
-		 0.42748/(sqrt(t_red * t_red * t_red) * ((t_red*z_init/p_red + 0.08664))));
-}
-
-/*
- * At high pressures air becomes less compressible, and
- * does not follow the ideal gas law any more.
- */
-#define STANDARD_TEMPERATURE 293.0
-
-double gas_compressibility_factor(struct gasmix *gas, double bar)
-{
-	/* Critical points according to https://en.wikipedia.org/wiki/Critical_point_(thermodynamics) */
-
-	double tcn2 = 126.2;
-	double tco2 = 154.6;
-	double tche = 5.19;
-
-	double pcn2 = 33.9;
-	double pco2 = 50.5;
-	double pche = 2.27;
-
-	double tc, pc;
-
-	tc = (tco2 * get_o2(gas) + tche * get_he(gas) + tcn2 * (1000 - get_o2(gas) - get_he(gas))) / 1000.0;
-	pc = (pco2 * get_o2(gas) + pche * get_he(gas) + pcn2 * (1000 - get_o2(gas) - get_he(gas))) / 1000.0;
-
-	return (redlich_kwong_equation(STANDARD_TEMPERATURE/tc, bar/pc,
-				       redlich_kwong_equation(STANDARD_TEMPERATURE/tc, bar/pc,
-							      redlich_kwong_equation(STANDARD_TEMPERATURE/tc, bar/pc,1.0))));
-}
-
 int gas_volume(cylinder_t *cyl, pressure_t p)
 {
 	double bar = p.mbar / 1000.0;