FABRIC
FILTER      
NEWSLETTER   

May 1999
No. 283

Coal Technology for the Next Century

Recently, the U.S. Dept. of Energy unveiled a new concept, "Vision 21" — a futuristic way of combining high-efficiency power technologies with advanced coal processing technologies and environmental controls to create a near-zero discharge, multi-product energy complex. A presentation at the 24th International Technical Conference on Coal Utilization & Fuel Systems outlined one conceptualization of a Vision 21 Plant that focuses on production of hydrogen from coal. The information was provided by Joseph Badin of Energetics, Incorporated, Michael DeLallo and Michael Rutkowski of Parsons Corp., and Jerome Temchin of the U.S. Dept. of Energy. The concept can help assure that coal can remain competitive with natural gas as a fuel for baseload electricity generation for existing and new power plants. It can also provide a feedstock for chemical and liquid fuels production, even if emissions of carbon dioxide must be controlled.

Vision 21 is intended to develop the enabling technologies to allow the private sector to combine high-efficiency power technologies with advanced coal processing technologies and environmental control systems. Research on the Vision 21 enabling technologies is expected to result in technology options that could be introduced to the marketplace by 2020.

For the longer term, new technologies are being developed to separate hydrogen from syngas, resulting in the potential for hydrogen production at costs competitive with natural gas. These technologies include inorganic membranes to separate hydrogen from CO2, high-temperature particulate filters, advanced turbine systems (ATS) and lower cost air separation technologies such as ion transfer membranes. A conceptual plant design was prepared, which utilizes some of the new technology to provide a basis for producing lower cost hydrogen from coal.

The system utilizes a high-temperature, high-pressure gasifier, a high-temperature particulate filter and an advanced turbine system expander for power generation. The key process is the hydrogen separation device, based on an inorganic membrane under development by Oak Ridge National Laboratory.

The high-pressure syngas produced in the gasifier is quenched to 1905°F as a result of adjustments in the second stage of the gasifier, thereby eliminating the requirement for a fire tube heat exchanger. The hot raw gas is cleaned of larger particulates in a cyclone and has a considerable amount of steam added, ensuring adequate water content for the high-temperature shift reaction to occur, while reducing temperature to 1456°F. Following the cyclone, the gas is cleaned of remaining particles with a ceramic candle filter. The gas enters the hydrogen separation device (HSD) at 1456°F and leaves the HSD at 1823°F as a result of the exothermic shift reaction. The hydrogen produced from the HSD is 99.5 percent pure, and goes through a heat recovery steam generator (HRSG) and cooler, resulting in hydrogen at 100°F and 15 psia. Product hydrogen is compressed to 346 psia.

After establishing a baseline design for production of hydrogen utilizing membrane technology, additional conceptual plant designs utilizing variations in the technology can be prepared. Included in the design variations being pursued are: 

Hydrogen production utilizing a lower temperature gas and ceramic filter (about 1000°F) ahead of the HSD. This approach places less stress on the ceramic filter and ensures precipitation of alkali metal compounds prior to contact in the ATS turbine expander.

Hydrogen production utilizing hot gas desulfurization and a ceramic filter ahead of the HSD. This concept protects the HSD and the turbine from alkali and sulfur compounds and produces a marketable sulfur by-product.

Although ceramic candle filters remain the most promising candidates for hot gas particulate removal, both durability and long-term stability must be proven.

Long-term durability at 1000° F has not been fully demonstrated, but the Piñon Pine IGCC demonstration plant should provide these data. As operating data become available, the upper limit of ceramic filters in reducing conditions should increase. Filters can already be recommended for use at 1200°F in reducing atmospheres. The filter for this application was assumed to operate at 1455°F in a reducing atmosphere.

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