Production of formaldehyde from carbon oxides and H2S

Organic compounds -- part of the class 532-570 series – Organic compounds – Sulfur containing

Reexamination Certificate

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Details

C568S060000, C568S069000, C568S470000

Reexamination Certificate

active

06410793

ABSTRACT:

BACKGROUND OF THE INVENTION
1. Field of the Invention
This invention broadly relates to a process for producing formaldehyde from a gas stream containing a mixture of hydrogen sulfide (G
2
S) and a carbon oxide, wherein the carbon oxide is selected from carbon monoxide (CO), carbon dioxide (CO
2
) and mixtures thereof. More particularly, this invention provides a method wherein a gas stream containing a carbon oxide and hydrogen sulfide is first passed in contact with a catalyst comprising a supported metal oxide of a metal selected from the group consisting of vanadium (V), niobium (Nb), molybdenum (Mo), chromium (Cr), rhenium (Re), tungsten (W), manganese (Mn), titanium (Ti), zirconium (Zr) and tantalum (Ta) and mixtures thereof to convert said carbon oxide and hydrogen sulfide to methyl mercaptans, (primarily methanethiol (CH
3
SH) and a small amount of dimethyl sulfide (CH
3
SCH
3
)), and the methyl mercaptans are then passed in contact with a catalyst comprising certain supported metal oxides or certain bulk metal oxides in the presence of an oxidizing agent and for a time sufficient to convert at least a portion of the methyl mercaptans to formaldehyde (CH
2
O) and sulfur dioxide (SO
2
).
2. Description of Related Art
Ratcliffe et al., U.S. Pat. No. 4,570,020 describes a catalytic process for producing methanethiol (CH
3
SH) from a gaseous feed comprising a mixture of carbon monoxide (CO) and hydrogen sulfide (H
2
S). Gases containing H
2
S are often considered an unwanted waste stream. According to the patent, the gaseous mixture is contacted, at a temperature of at least about 225° C. with a catalyst comprising a metal oxide of a metal selected from the group consisting of vanadium (V), niobium (Nb), and tantalum (Ta) and mixtures thereof supported as an oxide layer on titania. The methanethiol is disclosed as being useful as an odorant or tracer for natural gas and as a raw material for making methionine, fungicides and jet fuel additives.
The art has also identified methyl mercaptans, such as methanethiol (CH
3
SH) and dimethyl sulfide (CH
3
SCH
3
), as hazardous pollutants, and has suggested a variety of ways for their destruction. Noncatalytic gas phase oxidation of such reduced sulfur compounds has been shown to produce primarily sulfur oxide and carbon oxide products. A. Turk et al.,
Envir. Sci. Technol
23:1242-1245 (1989). Investigators have observed that oxidation in the presence of single crystal metal surfaces (Mo, Ni, Fe, Cu) results in the formation of methane and ethane, nonselective decomposition to atomic carbon, gaseous hydrogen and the deposition of atomic sulfur on the metal surface via a stoichiometric reaction (See Wiegand et al.,
Surface Science,
279(1992): 105-112). Oxidation of higher mercaptans, e.g., propanethiol on oxygen-covered single crystal metal surfaces (Rh), produced acetone via a stoichiometric reaction at low selectivity and accompanied by sulfur deposition on the metal surface (See Bol et al.,
J. Am. Chem. Soc.,
117(1995): 5351-5258). The deposition of sulfur on the metal surface obviously precludes continuous operation.
The art also has disclosed using catalysts comprising a two-dimensional metal oxide overlayer on titania and silica supports, e.g., vanadia on titania, for catalytically reducing NO
x
by ammonia to N
2
and H
2
O in the presence of sulfur oxides. Bosch et al.,
Catal. Today
2:369 et seq. (1988). Thus, such catalysts are known to be resistant to poisoning by sulfur oxides. It also is known that such catalysts, as well as certain bulk metal oxides catalysts, can be used to oxidize methanol to formaldehyde selectively. Busca et al,
J. Phys. Chem.
91:5263 et seq. (1987).
Applicant recently made the discovery that a supported metal oxide catalyst can be used to oxidize methyl mercaptans, such as methanethiol (CH
3
SH) and dimethyl sulfide (CH
3
SCH
3
), selectively to formaldehyde in a continuous, heterogenous catalytic process without being poisoned by the reduced sulfur. On the basis of that discovery, applicant has envisioned the present process as a way of converting gaseous streams containing carbon oxide and hydrogen sulfide to formaldehyde.


REFERENCES:
patent: 4544649 (1985-10-01), Wachs
patent: 4570020 (1986-02-01), Ratcliff et al.
patent: 4668825 (1987-05-01), Ratcliffe
patent: WO98/17618 (1998-04-01), None
CA:105:45264 abs of FR2567513, Jan. 1986.*
Hawley's Condensed Chemical Dictionary ed Richard Lewis Sr. 12th ed, 1993.*
Turk, et al., “Ammonia Injection Enhances Capacity of Activated Carbon for Hydrogen Sulfide and Methyl Mercaptan,” Enviro. Sci. Technol., vol. 23, No. 10, 1242-1245, 1989.
Weigand, et al., “The Local Structure of Absorbed methyl Thiolate: The Reactions of Methanethiol on Mo(110),” Surface Science, vol. 279, 105-112, 1992.
Bol and Friend, “The Effects of Oxygen on Selectivity: The Reactions of 2-Propanethiolate on Oxygen-Covered Rh(111),” J. Am. Chem. Soc., vol. 117, 5351-5358, 1995.
Busca, et al., “Mechanism of Selective Methanol Oxidation Over Vanadium Oxide-Titanium Oxide Catalysts: A FT-IR and Flow Reactor Study,” J. Phys. Chem., vol. 91, 5263-5269, 1997.
Jehng, et al., “Surface Modified Niobium Oxide Catalyst: Synthesis, Characterization, and Catalysis,” Applied Catalysis A, vol. 83, 179-200, 1992.
Kim and Wachs, “Surface Chemistry of Supported Chromium Oxide Catalysts,” Journal of Catalysis, vol. 142, 166-171, 1993.
Jehng and Wachs, “Molecular Design of Supported Niobium Oxide Catalysts,” Catalysis Today, vol. 16, 417-426, 1993.
Kim and Wachs, “Surface Rhenium Oxide-Support Interaction for Supported Re2O7Catalysts,” Journal of Catalysis, vol. 141, 419-429, 1993.
Deo, et al., “Physical and Chemical Characterization of Surface Vanadium Oxide Supported on Titania: Influence of Titania Phase (Anatase, Rutile, Brookite and B),” Applied Catalysis A, vol. 91, 27-42, 1992.
Deo and Wachs, “Reactivity of Supported Vanadium Oxide Catalysts: The Partial Oxidation of Methanol,” Journal of Catalysis, vol. 146, 323-334, 1994.
Deo and Wachs, “Effect of Additives on the Structure and Reactivity of the Surface Vanadium Oxide Phase in V2O5/TiO2Catalysts,” Journal of Catalysis, vol. 146, 335-345, 1994.
Jehng, et al., “Surface Chemistry of Silica-Titania-Supported Chromium Oxide Catalysts,” J. Chem Soc. Faraday Trans., vol. 91(5), 953-961, 1995.
Kim, et al., “Molecular Structures and Reactivity of Supported Molybdenum Oxide Catalysts”, Journal of Catalysis, vol. 146, 268-277, 1994.
Banares, et al., “Molybdena on Silica Catalysts: Role of Preparation Methods of the Structure-Selectivity Properties for the Oxidation of Methanol,” Journal of Catalysis, vol. 150, 407-420, 1994.
Jehng and Wachs, “The Molecular Structures and Reactivity of V2O5/TiO2/SiO2Catalysts,” Catalyst Letters, vol. 13, 9-20, 1992.
Arora, et al., “Surface Aspects of Bismuth—Metal Oxide Catalysts”, Journal of Catalysis, vol. 159, 1-13, 1996.
Abstract No. 066367, “Photooxidation of Dimethyl Mechanism Evaluation”, Chemical Abstracts, vol. 114, No. 8, 1991 & J. Atmos. Chem., vol. 11, No. 4, 365-99.

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