<p>Steam Mass Cases</p>

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In Pakistan Furnace units are consuming a max. of 50t/d Cl2 (g) 0.5Cl2 + 0.5H2 == HCl

so HCl produced 36.5 35.5 / 50 * tonne day / * ton day / 56.668

For SGL

Ecosyn disadvantage external absorber Heat_Efficiency_Transfer 0.6 :

Heat_for_Steam 0.5 kw * kg / 1 * hr * :

ton/day of HCl fluctuation HCl_Production 30 tonne day / * (55 tonne day / * (35 tonne day / * range : tonne day / 30354045505561 mat

Heat_HCl_Production Heat_for_Steam Heat_Efficiency_Transfer * HCl_Production * : 375 kw * 437.5 kw * 500 kw * 562.5 kw * 625 kw * 687.5 kw * 61 mat

How much steam is produced per day @10barg

4.3 is the heat capacity, entering water temperature is 30, 2778 is steam enthalpy at 10barg Steam_Calc m 4.3 kJ kg Δ°C * / * 100 °C * 30 °C * - (* (2778 kJ kg / * + (* :

<p>Steam Mass Cases</p>

Steam_Mass 1 el Steam_Calc 375 kW * ≡ m solve maple : 0.122 kg s / * 11 mat

Steam_Mass 2 el Steam_Calc 437.5 kW * ≡ m solve maple : 0.1218 kg s / * 0.1421 kg s / * 21 mat

Steam_Mass 3 el Steam_Calc 500 kW * ≡ m solve maple : 0.1218 kg s / * 0.1421 kg s / * 0.1624 kg s / * 31 mat

Steam_Mass 4 el Steam_Calc 562.5 kW * ≡ m solve maple : 0.1218 kg s / * 0.1421 kg s / * 0.1624 kg s / * 0.1827 kg s / * 41 mat

Steam_Mass 5 el Steam_Calc 625 kW * ≡ m solve maple : 0.1218 kg s / * 0.1421 kg s / * 0.1624 kg s / * 0.1827 kg s / * 0.203 kg s / * 51 mat

Steam_Mass 6 el Steam_Calc 687.5 kW * ≡ m solve maple : 0.1218 kg s / * 0.1421 kg s / * 0.1624 kg s / * 0.1827 kg s / * 0.203 kg s / * 0.2233 kg s / * 61 mat

This is for 10barg saturated steam. If the steam pressure is reduced so will be its enthalpy (2778
used in Steam_Calc eq.) & higher quantity we will achieve. Steam_Mass tonne hr / 0.438 0.512 0.585 0.658 0.731 0.804 61 mat