Method of optimizing the operation of claus units
A catalytic method for treating an H 2 S/SO 2 mixture for producing liquid sulphur including the following steps: a) at least one step of heating the mixture containing H 2 S/SO 2 to a temperature Tc; b) at least one step of catalytically reacting the heated mixture obtained in a) in the presence of at least one catalyst and at least one step of recovering the exiting mixture containing gaseous sulphur; and c) at least one step of converting the gaseous sulphur contained in the exiting mixture obtained at step b) into liquid sulphur, wherein between step b) and step c), the temperature Ts of said exiting mixture and the dew point Tr of the gaseous sulphur contained in said exiting mixture are measured and in that the heating temperature Tc of step a) is adjusted so that the temperature Ts is 5° C. to 30° C. above the dew point Tr.
1. A catalytic process carried out in at least three catalytic reactors connected in a sequence for treating a mixture of H 2 S and of SO 2 issued from a first combustion stage of a Claus process in order to produce liquid sulfur, said process comprising the following steps:
a) at least one step of heating the mixture comprising the SO 2 and the H 2 S to a temperature Ts,
b) at least one step of catalytically reacting the heated mixture obtained in a) in the presence of at least one catalyst and at least one stage of recovering the outlet mixture comprising gaseous sulfur,
c) at least one step of converting the gaseous sulfur present in the outlet mixture obtained in stage b) to liquid sulfur,
wherein between step b) and step c) for at least one of the last two catalytic reactors, measuring the temperature To of said outlet mixture and the dew point temperature Td of the gaseous sulfur present in said outlet mixture, and
adjusting the heating temperature Ts of step a) so that the temperature To is greater than the dew point temperature Td by 5° C. to 30° C.
2. The process as claimed in claim 1 , wherein the heating temperature Ts of step a) is adjusted so that said temperature To is greater than the dew point temperature Td by 5° C. to 20° C.
3. The process as claimed in claim 1 , wherein the heating temperature Ts of step a) is adjusted so that said temperature To is greater than the dew point temperature Td by 5° C. to 10° C.
4. A device for the implementation of the catalytic process according to claim 1 in at least three catalytic reactors for treating a mixture of H 2 S and SO 2 in order to produce liquid sulfur, said device comprising:
at least one means for heating the mixture comprising the SO 2 and the H 2 S to a temperature Ts;
at least one means for catalytically reacting the heated mixture obtained at the outlet of the heating means in the presence of at least one catalyst and at least one means for recovering an outlet mixture comprising gaseous sulfur;
at least one means for converting the gaseous sulfur present in the outlet mixture to liquid sulfur, and for at least one of the last two catalytic reactors a device for measuring the dew point temperature of the sulfur.
5. The device as claimed in claim 4 , wherein the device for measuring the dew point temperature of the sulfur is a calorimetric probe.
6. The device as claimed in claim 4 , wherein the device for measuring the dew point temperature of the sulfur is a magnetic probe.