Process for reduction of gaseous sulfur compounds

Details Process for reduction of gaseous sulfur compounds Process for reduction of gaseous sulfur compounds

2002-06-27

2003-04-01

Bos, Steven (Department: 1754)

Catalyst, solid sorbent, or support therefor: product or process

Solid sorbent

C502S325000, C502S337000, C502S338000, C502S340000, C502S345000, C502S350000, C502S406000, C502S414000, C502S415000, C502S517000, C502S527120, C502S527130, C502S527140, C502S527240

Reexamination Certificate

active

06541419

ABSTRACT:

BACKGROUND OF THE INVENTION
1. Field of the Invention
The invention relates to a process for the reduction of the level of gaseous sulfur compounds, e.g., H
2
S, in a gaseous stream by contacting the stream with a sorber capable of absorbing such compounds under sulfur sorbing conditions.
2. Discussion of the Prior Art
In many applications, it is well known that it is desirable to reduce the level of gaseous sulfur compounds such as H
2
S, COS, mercaptans, etc. Many applications, e.g., fuel cells, require that the gaseous sulfur compounds in a raw fuel stream (e.g., naphtha, LPG, town gas, etc.) be reduced to as low a level as practicable in order to avoid poisoning the environment or catalysts such as steam reforming catalysts, water-gas shift catalysts, etc. Furthermore, fuel cell electrodes will rapidly become inactivated as the result of high levels of gaseous sulfur compounds in the fuel stream since the electrodes invariably contain precious metal components, e.g., platinum, which are extremely sensitive to the presence of sulfur compounds.
There are many prior art processes involving hydrogenation desulfurization in which the sulfur compounds in the raw fuel stream are decomposed by hydrogenolysis at temperatures of e.g., 350 to 400° C. in the presence of e.g., Ni—Mo or Co—Mo catalysts and thereafter the resultant H
2
S is then absorbed on a bed of ZnO at temperatures of e.g., 300 to 400° C. However, in these processes, the level of the H
2
S in the treated steam is still too high, e.g., 100 ppm and higher. However, it is well known that if the gas steam contains gaseous sulfur compounds in as little a level as 0.25 to 25 ppm, about 90% of the surface of a steam reforming catalyst such as Ru or Ni will be covered with the sulfur compounds, thereby resulting in a rapid deterioration of the catalyst. Furthermore, the prior art processes are typically not capable of reducing the level of gaseous sulfur compounds to very low levels, e.g., 100 ppb and lower since the prior art sorbers are used under conditions where severe pressure drops would otherwise occur if the flow rate of the raw fuel gaseous stream is significantly increased in order to improve the sorbing reaction rate.
Therefore, there is a need for a process which will “polish” a desulfurized fuel stream containing on the order of 25 ppm gaseous sulfur compounds such as H
2
S and further reduce the level of such compounds in an efficient manner to a level of less than 100 ppb for a period of at least one hour, i.e. before “breakthrough” commences. For the purposes of this invention, “breakthrough” shall be understood to mean that the level of the gaseous sulfur compounds commences rising above 100 ppb.
DETAILED DESCRIPTION OF THE INVENTION
The invention relates to an improved process for the reduction of gaseous sulfur compounds, e.g., H
2
S present in a gaseous stream, especially in a gaseous steam which has been pre-treated to reduce the level of gaseous sulfur compounds below 25 ppm. The improvement resides in contacting the stream with a sorber capable of absorbing such compounds under sulfur sorbing conditions, with the sorber being present in the form of one or more layers on the surface of a monolith carrier.
It was found that in the first 30 minutes of use at 400° C., bed of zinc oxide pellets allowed 20% of an 8 ppm H
2
S stream to break through. In contradistinction, when a monolith carrier containing 15% by weight of the zinc oxide content of the pellet bed, less than 5% of the original concentration of the H
2
S was allowed to pass through. In particular, it was found that highly dispersed zinc oxide present as multiple layers on a monolith carrier such as cordierite reduces the concentration of hydrogen sulfide in a gas stream to a much greater extent than almost 10 times the amount of zinc oxide in pellet form in a bed. The monolith coated with zinc oxide represent a device with a fraction of the back pressure of a bed of finely divided zinc oxide. Although the hydrogen sulfide capacity of the zinc oxide-coated monolith carrier is a fraction of that of the zinc oxide pellets, the former is capable of reducing the hydrogen sulfide concentration by ≧95% as compared to a reduction in hydrogen sulfide of 70-90% using zinc oxide pellets.
The layers of the sorber on the monolith carrier are such that the layers will have a total thickness of at least about 3g/in
3
of the carrier, preferably at least 3.5 g/in
3
of the carrier. Preferably, the sorber will be present in the form of at least three layers on the surface of the monolith carrier. It is also preferred that the sorber be present on the surface of the monolith carrier in the form of particles having an average particle size of 90% <10&mgr;.
Typically, the sorber will comprise one or more metal compounds wherein the metal is selected from the group consisting of zinc, calcium, nickel, iron, copper and mixtures thereof. The preferred metal is zinc and the preferred metal compounds are zinc oxide and zinc titanate.
The process of the present invention operates most efficiently when the gaseous sulfur compound in the gaseous stream prior to contact with the sorber is primarily H
2
S present in an initial concentration of about 0.15 to about 25 ppm, preferably 0.25 to 10 ppm, and the stream is passed into contact with the sorber at a volumetric hourly rate of about 500 to about 100,000 volumes, preferably 2,500 to 15,000 volumes, per volume of monolith carrier.
Typically, the process of the present invention will result in a reduction of the H
2
S from its initial concentration to a level of less than 100 ppb for a period of at least one hour, preferably less than 50 ppb for at least 4 hours.
The sorber is disposed on the surface of a monolith carrier, preferably of the type comprising one or more monolithic bodies having a plurality of finely divided gas flow passages extending therethrough. Such monolith carriers are often referred to as “honeycomb” type carriers and are well known in the prior art. A preferred form of the carrier is made of a refractory, substantially inert, rigid material which is capable of maintaining its shape and a sufficient degree of mechanical conditions at high temperatures of about 1450° C. Typically, a material is selected for use as the carrier which exhibits a low thermal coefficient of expansion, good thermal shock resistance and preferably low thermal conductivity.
Two general types of materials of construction for monolith carriers are known. One is a ceramic-like porous material composed of one or more metal oxides, e.g., alumina, alumina-silica, alumina-silica-titania, mullite, cordierite, zirconia, zirconia-ceria, zirconia-spinel, zirconia-mullite, silicon-carbide, etc. A particularly preferred and commercially available material for use as the carrier for the present invention is cordierite, which is an alumina-magnesia-silica material.
Monolith carriers are commercially available in various sizes and configurations. Typically, the monolithic carrier would comprise, e.g., a cordierite member of generally cylindrical configuration (either round or oval in cross section) and having a plurality of parallel gas flow passages of regular polygonal cross sectional extending therethrough. The gas flow passages are typically sized to provide from about 50 to about 1,200, preferably 200-600, gas flow channels per square inch of face area.
The second major type of preferred material of construction for the monolith carrier is a heat- and oxidation-resistant metal, such as stainless steel or an iron-chromium alloy. Monolith carriers are typically fabricated from such materials by placing a flat and a corrugated metal sheet one over the other and rolling the stacked sheets into a tubular configuration about an axis parallel to the configurations, to provide a cylindrical-shaped body having a plurality of fine, parallel gas flow passages, which may range, typically, from about 200 to about 1,200 per square inch of face area.
The monolith carrier may also be present in the form of a ceramic or metal foam. Monolith carrie

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