U.S. patents available from 1976 to present.
U.S. patent applications available from 2005 to present.

Coal gasification process

Patent 4692172 Issued on September 8, 1987. Estimated Expiration Date: Icon_subject February 10, 2006. Estimated Expiration Date is calculated based on simple USPTO term provisions. It does not account for terminal disclaimers, term adjustments, failure to pay maintenance fees, or other factors which might affect the term of a patent.

Patent References

1799885

1955574

2644745

Production of reducing gas
Patent #: 4277365
Issued on: 07/07/1981
Inventor: Paull ,   et al.

Partial oxidation process Patent #: 4400180
Issued on: 08/23/1983
Inventor: Marion ,   et al.

Inventors

Application

No. 06/827858 filed on 02/10/1986

US Classes:

48/197R, PROCESSES252/373, Carbon-oxide and hydrogen containing48/203, Producer48/206Continuous

Examiners

Primary: Kratz, Peter

Attorney, Agent or Firm

International Class

C10J 3/46 (20060101)

Abstract

Low sulfur, iron and calcium containing solid carbonaceous fuel having a high melting point ash is mixed with a sufficient amount of iron sulfide containing material or supplemental iron and sulfur containing reactant materials that react in the reaction zone to produce iron and sulfur containing compounds. The mixture of materials is reacted in a free-flow gasifier by partial oxidation to produce a raw gas stream of synthesis gas, reducing gas or fuel gas, containing entrained particulate matter including molten slag. By the process, sufficient iron and sulfur are in the reaction zone so that the melting point of the fuel ash is decreased, and the mole ratio H2 S/H2 +CO in the raw gas stream is greater than 0.01. Further, the amount of iron in the molten ash is greater than 10.0 wt. %, and preferably at least 14 wt. % of the molten ash. By this means, the fluid temperature of the molten ash entrained in the raw gas stream is reduced at least 100° F. less than the fluid temperature of the fuel ash without the addition of iron and sulfur, and the gasifier may be operated in the molten slagging mode at a lower temperature. Further, coal wash tailings containing iron sulfides may be disposed of as a portion of the feed to the gasifier in an environmentally acceptable manner; and useful by-product sulfur may be recovered.

Other References

  • Lowry, Chemistry of Coal Utilization, vol. 1, pp. 565-571, 1945
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