Ok, now I have a better idea. You want to produce steam by utilizing hot water. The theoretical calculation will be,
693000 kJ/hr = m(kg/hr)x4.2 kJ/kg0Cx230C
So the mass flow rate of hot water will be 7173.91 kg/hr or 1.99 kg/hr (~1.99 Lit/sec). This calculation considers supply of 1000C feed water.
If your water temperature is 300C and you want to use a dT of 230C, then the hot water flowrate should be 8086 kg/hr or 2.25 L/s for steam at 1 atmosphere.
You have some important things to check.
1. Is overall heat transfer coefficient of the heat exchanger is sufficient to produce the steam quantity required?
2. Is it primarily designed for similar application? (steam formation near the pipe wall will reduce the overall heat transfer coefficient)
3. Dryness fraction of steam produced in the above manner will be low and subsequently the humidified air temperature will drop down. You have to provide reheating.
Regards,