of water from second gas stream 116 second reheater 22 increased the temperature of second dry gas stream 120 to a temperature of 215 u00b0 c to produce second hot dry gas stream 122 third adsorber 30 produced 3 0 kgmol hr 53 3 kg hr of water from third gas stream 126 third reheater 32 increased the temperature of third gas stream 126 to a temperature of 205 u00b0 c to produce third hot dry gas stream 132 the total sulfur recovered was 3206 3 0 kg hr for a total conversion of sulfur of 100 0 wt example 1 4 is a hysys simulation according to fig6 having one adsorber upstream of the final claus catalytic stage first reheater 12 increased the temperature of first gas stream 106 to a temperature of 235 u00b0 c to produce first hot wet gas stream 212 second reheater 22 increased the temperature of second gas stream 116 to a temperature of 215 u00b0 c to produce second hot wet gas stream 222 first adsorber 10 removed 98 1 kgmol hr 1767 0 kg hr of water from third gas stream 126 third reheater 32 increased the temperature of first dry gas stream 110 to a temperature of 205 u00b0 c to produce first hot dry gas stream 132 the total sulfur recovered was 3202 6 kg hr for a total conversion of 99 9 wt the.