I actually just built a model from scratch, very easy to do. Although, I did have a starting place from a pump curve as the flow was between a vacuum pump, condenser, and dryer. Darcy-Weinbach,  simplified Bernoulli, or other will give you a very good estimate for both flow rate and subsequent pressure drop and vice versa. The model works pretty well with what is observed in the process as well. 
	
		
	
	
		
			
				Density of Air
		
		
			
				Viscosity of Air
		
		
			
				Density of Steam
		
		
			
				Viscosity of Steam
		
		
			
				Percent Air
		
		
			
				Percent Steam
		
		
			
				Density of Mixture
		
		
			
				Viscosity of Mixture
		
		
			
				Length
		
		
			
				Diameter
		
		
			
				Roughness
		
		
			
				Flow Rate
		
		
			
				Velocity
		
		
			
				Re
		
		
			
				Friction Factor
		
		
			
				Pressure Losses
		
		
			
				Major Losses
		
		
			
				Minor Losses
		
		
			
				Total Losses
		
		
			
				P2
		
	
 
Used these variables. Derived from equations, process data, ANSI, Crane's flow manual, and Perry's. Once you have these values or the equations to solve for these values it should be plug and chug.