US 4,332,774 AGranted

Manufacture of hydrogen sulfide

AssigneesHome Oil Company Limited, Morrison-Knudsen Company, Inc.

InventorsIan Drum, Richard S. Madenburg, Douglas M. Paulsrude, Carroll H. Sherman, Frank G. Turpin, Gerry A. Wheatcroft

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Abstract

Methods and apparatus adaptable to continuous production of hydrogen sulfide from chemical reaction of sulfur with various gaseous sulfur-reducing reactants selected from hydrocarbons, carbon monoxide, carbon-containing compounds such as carbon disulfide, hydrogen, of mixtures of such gases are provided utilizing a fired process sulfur heater to vaporize liquid sulfur feed stock. Control of the temperature of the sulfur vapors and the amount of liquid sulfur feed are used to modulate sulfiding reaction temperatures. Viscosity of the liquid sulfur feed stock is modified by contact with product gases in order to facilitate flow rate control as liquid sulfur is pumped into the sulfur vaporizer where its temperature increases above about 300.degree. F. Steam for hydrolysis purposes is introduced with the sulfur vapors, to augment temperature modulation of the sulfiding reactions, and/or with the reductant gas to assist in heat recovery from the reaction product gases. The system is operated at pressures above atmospheric as determined by a back pressure established in removing hydrogen sulfide product gases. Controlled movement of reactants and reaction product gases through the system is achieved without mechanical flow control equipment in any of the relatively high temperature zones approaching sulfiding reaction temperatures or sulfur vaporizing temperature.

Apparatus for producing hydrogen sulfide by reaction of sulfur with a gaseous sulfur reductant feedstock selected from various sulfur reductant feedstocks including hydrogen, hydrocarbons, carbon-containing gases such as carbon monoxide, and mixtures thereof, comprising in combination

an interconnected system for combining sulfur, sulfur reductant feedstock and steam for reaction to produce hydrogen sulfide,
a source of gaseous sulfur reductant feedstock having a predetermined temperature,
vaporizer and superheater means including separately controllable heat source means for vaporizing liquid sulfur and superheating such sulfur vapors,
means for supplying liquid sulfur at a predetermined temperature,
means for delivering such liquid sulfur into the vaporizer and superheater means,
means for quantitatively controlling delivery of liquid sulfur to the vaporizer and superheater means,
means for supplying steam at a predetermined temperature,
means for introducing steam into the vaporizer and superheater means to be superheated with the sulfur vapors,
means for introducing steam with the sulfur reductant feedstock,
means for delivering sulfur vapors, steam and sulfur reductant feedstock into a vessel means for premixing sulfur vapors, steam and sulfur reductant feedstock before introduction into a catalytic reaction zone,
catalytic reaction means connected to such premixing vessel means for receiving and reacting sulfur vapors, steam and sulfur reductant feedstock to produce reaction product including hydrogen sulfide,
means for controlling such heat source means to control heat input into the vaporizer and superheater means to balance the heat input into the catalytic reaction means from the steam, sulfur and sulfur reductant feedstock,
means for cooling reaction product,
means for delivering reaction product from the catalytic reaction means to the means for cooling reaction product, and
means for delivering cooled reaction product including hydrogen sulfide from the means for cooling reaction product.

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Abstract

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