Sulfur plant temperature control

Claim 2

In a Claus process for the production of sulfur wherein a gaseous stream comprising hydrogen sulfide is combined with a source of oxygen in a flame zone in proportions to convert, by combustion, sufficient hydrogen sulfide to sulfur dioxide to form, with hydrogen sulfide added in a thermal conversion zone, a reaction gas stream wherein the mole ratio of hydrogen sulfide to sulfur dioxide is about 2:1, passing the reactive gas stream through the thermal converison zone where at a temperature above the dew point of sulfur, sulfur is thermally formed by reaction of a portion of the hydrogen sulfide with sulfur dioxide, from which the formed sulfur is condensed to form a residual gas stream, and wherein additional sulfur is formed by passing the residual gas stream through a plurality of catalytic conversion stages in series, and wherein the residual as stream is heated to a temperature sufficient to initiate catalytic reaction of hydrogen sulfide and sulfur dioxide prior to each stage, and formed sulfur is condensed following each catalytic conversion stage in a sulfur condensation stage, the improvement which comprises heating the residual gas stream to the catalytic initiation temperature by indirect heat exchange with high pressure steam generated by indirect flash heating of water in the flame zone to form steam at a pressure of at least about 600 psig, the quantity of steam formed being sufficient to at least heat the residual gas stream between each sulfur condensation and catalytic sulfur formation stage to a temperature required to initiate the catalytic reaction of sulfur dioxide with hydrogen sulfide to form elemental sulfur.

Claim 3

The process of claim 1 wherein steam of about 1000 psig is generated in the flame zone.

Claim 4

A process for the production of sulfur comprising: a. combining a gaseous stream including hydrogen sulfide with a source of oxygen in a flame zone in proportions to convert, by combustion, sufficient hydrogen sulfide to sulfur dioxide to form, with the hydrogen sulfide added in a thermal conversion zone, a reactive gas stream wherein the mole ratio of hydrogen sulfide to sulfur dioxide is about 2:1; b. passing the reactive gas stream through the thermal conversion zone; c. thermally forming sulfur by reaction of a portion of the hydrogen sulfide with sulfur dioxide in the thermal conversion zone at a temperature above the dew point of sulfur, wherein the temperature in the thermal conversion zone is maintained with cooling water; d. condensing the formed sulfur to form a residual gas stream; e. forming and condensing additional sulfur in a plurality of catalytic conversion stages and condensing stages in series by i. heating by indirect heat exchange with high pressure steam the residual gas stream to a temperature sufficient to initiate catalytic reaction of hydrogen sulfide and sulfur dioxide before each of the pluralities of catalytic conversion stages in series, wherein the high pressure steam is generated by indirect flash heating of water in the flame zone to form a steam at a pressure of at least about 600 psig, the source of the water being the water used to cool the thermal conversion zone, the quantity of stream formed being sufficient to at least heat the residual gas stream between each sulfur condensation stage and each catalytic sulfur formation stage to a temperature required to initiate the catalytic reaction of sulfur dioxide with hydrogen sulfide to form elemental sulfur: ii. forming additional sulfur in the plurality of catalytic conversion stages by passing the heated gas stream over a Claus catalyst; and iii. condensing formed sulfur following each catalytic conversion stage in a sulfur condensation stage.

Claim 5

A process for the production of sulfur comprising: a. combining a gaseous stream including hydrogen sulfide with a source of oxygen in a flame zone in proportions to convert, by combustion, sufficient hydrogen sulfide to sulfur dioxide to form, with the hydrogen sulfide added in a thermal conversion zone, a reactive gas stream wherein the mole ratio of hydrogen sulfide to sulfur dioxide is about 2:1; b. passing the reactive gas stream through the thermal conversion zone; c. thermally forming sulfur by reaction of a portion of the hydrogen sulfide with sulfur dioxide in the thermal conversion zone at a temperature above the dew point of sulfur, wherein the temperature in the thermal conversion zone is maintained with cooling water; d. condensing the formed sulfur to form a residual gas stream; e. forming and condensing additional sulfur in a plurality of catalytic conversion stages and condensing stages in series by i. heating by indirect heat exchange with high pressure steam the residual gas stream to a temperature sufficient to initiate catalytic reaction of hydrogen sulfide and sulfur dioxide before each of the pluralities of catalytic conversion stages in series, wherein the high pressure steam is generated by indirect flash heating of water in the flame zone to form a steam at a pressure of at least about 600 psig, the source of the water being the water used to cool the thermal conversion zone, the quantity of stream formed being sufficient to at least heat the residual gas stream between each sulfur condensation stage and each catalytic sulfur formation stage to a temperature required to initiate the catalytic reaction of sulfur dioxide with hydrogen sulfide to form elemental sulfur: ii. forming additional sulfur in the plurality of catalytic conversion stages by passing the heated gas stream over a Claus catalyst; and iii. condensing formed sulfur following each catalytic conversion stage in a sulfur condensation stage.

Claim 6

The process of claim 3 wherein the steam, after it heats the residual gas stream by indirect heat exchange, is utilized to cool the thermal conversion zone.

Claim 7

The process of claim 3 wherein steam of about 1000 psig is generated in the flame zone.

Claim 8

The process of claim 3 wherein the water in the flame zone is supplemented by makeup water.

Claim 9

In a Claus process for the production of sulfur wherein a gaseous stream comprising hydrogen sulfide is combined with a source of oxygen in a flame zone in proportions to convert, by combustion, sufficient hydrogen sulfide to sulfur dioxide to form, with hydrogen sulfide added in a thermal conversion zone, a reaction gas stream wherein the mole ratio of hydrogen sulfide to sulfur dioxide is about 2:1, passing the reactive gas stream through the thermal conversion zone where at a temperature above the dew point of sulfur, sulfur is thermally formed in a thermal conversion zone by reaction of a portion of the hydrogen sulfide with suflur dioxide with attendant cooling and generation of low pressure steam to remove reaction exotherm of the thermal conversion zone, from which the formed sulfur is condensed to form a residual gas stream, and wherein additional sulfur is formed by passing the residual gas stream through a plurality of catalytic conversion stages in series, and wherein the residual gas stream is heated to a temperature sufficient to initiate catalytic reaction of hydrogen sulfide and sulfur dioxide prior to each stage, and formed sulfur is condensed following each catalytic conversion stage in a sulfur condensation stage, the improvement which comprises heating the residual gas stream to the catalytic initiation temperature by indirect heat exchange with high pressure steam generated by indirect flash heating of water in the flame zone to form high pressure steam at a pressure of at least about 600 psig, the quantity of high pressure steam formed being from 5 to 50% of the low pressure steam and sufficient to heat the residual gas stream between each sulfur condensation and catalytic sulfur formation stage to a temperature required to initiate the catalytic reaction of sulfur dioxide with hydrogen sulfide to form elemental sulfur.

Claim 10

In a Claus process for the production of sulfur wherein a gaseous stream comprising hydrogen sulfide is combined with a source of oxygen in a flame zone in proportions to convert, by combustion, sufficient hydrogen sulfide to sulfur dioxide to form, with hydrogen sulfide added in a thermal conversion zone, a reaction gas stream wherein the mole ratio of hydrogen sulfide to sulfur dioxide is about 2:1, passing the reactive gas stream through the thermal conversion zone where at a temperature above the dew point of sulfur, sulfur is thermally formed in a thermal conversion zone by reaction of a portion of the hydrogen sulfide with suflur dioxide with attendant cooling and generation of low pressure steam to remove reaction exotherm of the thermal conversion zone, from which the formed sulfur is condensed to form a residual gas stream, and wherein additional sulfur is formed by passing the residual gas stream through a plurality of catalytic conversion stages in series, and wherein the residual gas stream is heated to a temperature sufficient to initiate catalytic reaction of hydrogen sulfide and sulfur dioxide prior to each stage, and formed sulfur is condensed following each catalytic conversion stage in a sulfur condensation stage, the improvement which comprises heating the residual gas stream to the catalytic initiation temperature by indirect heat exchange with high pressure steam generated by indirect flash heating of water in the flame zone to form high pressure steam at a pressure of at least about 600 psig, the quantity of high pressure steam formed being from 5 to 50% of the low pressure steam and sufficient to heat the residual gas stream between each sulfur condensation and catalytic sulfur formation stage to a temperature required to initiate the catalytic reaction of sulfur dioxide with hydrogen sulfide to form elemental sulfur.

Claim 11

A process for the production of sulfur comprising: a. combining a gaseous stream including hydrogen sulfide with aa source of oxygen in a flame zone in proportions to convert, by combustion, sufficient hydrogen sulfide to sulfur dioxide to form, with the hydrogen sulfide added in a thermal conversion zone, a reactive gas stream wherein the mole ratio of hydrogen sulfide to sulfur dioxide is about 2:1; b. passing the reactive gas stream through the thermal conversion zone; c. thermally forming sulfur in the thermal conversion zone by reaction of a portion of the hydrogen sulfide with sulfur dioxide in the thermal conversion zone at a temperature above the dew point of sulfur, wherein the temperature in the thermal conversion zone is maintained with generation of low pressure steam from cooling water; d. condensing the formed sulfur to form a residual gas stream; e. forming and condensing additional sulfur in a plurality of catalytic conversion stages and condensing stages in series by i. heating by indirect heat exchange with high pressure steam the residual gas stream to a temperature sufficient to initiate catalytic reaction of hydrogen sulfide and sulfur dioxide before each of the pluralities of catalytic conversion stages in series, the high pressure steam being generated by indirect flash heating of water in the flame zone to form a steam at a pressure of at least about 600 psig, the source of the water being the water used to cool the thermal conversion zone, the quantity of steam formed being from 5 to 50% of the low pressure steam generated in the thermal conversion zone and sufficient to heat the residual gas stream between each sulfur condensation stage and each catalytic sulfur formation stage to a temperature required to initiate the catalytic reaction of sulfur dioxide with hydrogen sulfide to form elemental sulfur; ii. forming additional sulfur in the plurality of catalytic conversion stages by passing the heated gas stream over a Claus catalyst; and iii. condensing formed sulfur following each catalytic conversion stage in a sulfur condensation stage.

Claim 12

A process for the production of sulfur comprising: a. combining a gaseous stream including hydrogen sulfide with aa source of oxygen in a flame zone in proportions to convert, by combustion, sufficient hydrogen sulfide to sulfur dioxide to form, with the hydrogen sulfide added in a thermal conversion zone, a reactive gas stream wherein the mole ratio of hydrogen sulfide to sulfur dioxide is about 2:1; b. passing the reactive gas stream through the thermal conversion zone; c. thermally forming sulfur in the thermal conversion zone by reaction of a portion of the hydrogen sulfide with sulfur dioxide in the thermal conversion zone at a temperature above the dew point of sulfur, wherein the temperature in the thermal conversion zone is maintained with generation of low pressure steam from cooling water; d. condensing the formed sulfur to form a residual gas stream; e. forming and condensing additional sulfur in a plurality of catalytic conversion stages and condensing stages in series by i. heating by indirect heat exchange with high pressure steam the residual gas stream to a temperature sufficient to initiate catalytic reaction of hydrogen sulfide and sulfur dioxide before each of the pluralities of catalytic conversion stages in series, the high pressure steam being generated by indirect flash heating of water in the flame zone to form a steam at a pressure of at least about 600 psig, the source of the water being the water used to cool the thermal conversion zone, the quantity of steam formed being from 5 to 50% of the low pressure steam generated in the thermal conversion zone and sufficient to heat the residual gas stream between each sulfur condensation stage and each catalytic sulfur formation stage to a temperature required to initiate the catalytic reaction of sulfur dioxide with hydrogen sulfide to form elemental sulfur; ii. forming additional sulfur in the plurality of catalytic conversion stages by passing the heated gas stream over a Claus catalyst; and iii. condensing formed sulfur following each catalytic conversion stage in a sulfur condensation stage.