Coal to Clean Syngas
The various downstream uses of syngas require that most of the contaminants present in raw syngas be removed to very low levels prior to use. Many of these contaminants can contribute to erosion, corrosion, and loss of strength in gas turbine components, and can act as poisons to the catalysts often used in syngas conversion and utilization processes. These same contaminants include or result in regulated air pollutants such as SOx, NOx, particulates, and mercury and other trace metals, which must be removed to increasingly low levels to meet stringent regulatory limits on air emissions.
Conventional methods for removing sulfur and other contaminants from syngas typically rely on chemical or physical absorption processes operating at low temperatures. However, after contaminant removal, the gas has to be reheated prior to its use in a gas turbine or other chemical synthesis process; in the case of downstream hydrogen production, additional steam needs to be added back to the syngas. These process swings adversely impact the plant's thermal efficiency and cost. Techno-economic analysis shows that gas-cleaning processes amenable to higher operating temperatures could significantly reduce this efficiency loss and improve the gasification plant's commercial viability. It is also critical that, while improving efficiency and reducing cost, the gas cleaning removes a wide variety of coal contaminants (including hydrogen sulfide, ammonia, hydrogen chloride, and carbonyl sulfide, as well as various forms of trace metals, including arsenic, mercury, selenium, and cadmium) to extremely low levels. Accordingly, the R&D approach in this area focuses on the development of high-efficiency processes that operate at moderate to high temperatures and provide multi-contaminant control to meet the highest environmental standards.
||RTI pilot-scale unit at Eastman Chemical Company gasifier. (Eastman Company)
High-temperature Syngas Cleanup Technology
Research Triangle Institute (RTI) is leading a project at Tampa Electric Company's (TECO) 250-megawatt (MW) Polk Power Station – an integrated gasification combined cycle (IGCC) plant located near Tampa, Florida. The project involves development of the High Temperature Desulfurization Process, which is a sorbent-based technology operating at relatively high syngas temperatures for removing hydrogen sulfide and carbonyl sulfide from syngas, down to a total sulfur level of less than one part per million, from a slip stream of coal-derived syngas at elevated temperature produced by the utility's coal gasifier. Scale-up for a 50-MWe demonstration size unit is underway. Pure, marketable solid sulfur will be created from the sulfur captured. Carbon dioxide will be captured using an activated MDEA system, with the intention of accelerating commercial deployment of these technologies for gasification of coal and petroleum coke. However, RTI's system (referred to as a warm syngas cleaning system) is capable of achieving very high levels of sulfur removal in syngas produced from the gasification of high-sulfur fuels. The activated MDEA process can then be applied to the low-sulfur syngas stream to capture carbon dioxide for sequestration, and, simultaneously, remove any trace sulfur from the syngas.
RTI has begun another project which considers integrated application of advanced technologies, including RTI’s warm gas cleanup technology in concert with other technologies, specifically Pratt Whitney Rocketdyne's Advanced Gasifier Pilot Plant Definition.
In a separate project but also assuming a basis of PWR's Advanced Gasifier Pilot Plant, Gas Technology Institute (GTI) will attempt to demonstrate the potential of a metal-polymeric membrane for hydrogen separation from syngas produced using the PWR advanced gasifier concept, with feed consisting of coal and natural gas.
Warm Gas Multi-Contaminant Removal System
Two warm gas multi-contaminant removal system projects are in development and are designed to be used after the bulk warm gas sulfur removal step. NETL's ORD Warm Gas Cleanup project targets suitable levels of trace contaminant capture from syngas, essentially by developing sorbents capable of removing EPA designated toxic trace contaminants (mercury, arsenic, selenium, phosphorus, antimony, and cadmium) from high temperature syngas (up to 550°F). Focus is on testing and developing palladium sorbents for the capture of the trace metals. Similarly, TDA Research, Inc. is working to remove anhydrous ammonia (NH3), mercury (Hg), and trace contaminants from coal- and coal/biomass-derived syngas using a high-capacity, low-cost sorbent.
Hydrogen is often the desired product of the gasification process, given its importance as primary feedstock for fuels synthesis, fertilizer and chemicals synthesis, or power generation in 90% CO2 capture scenarios. In this case, inexpensive post-gasification separation of hydrogen from CO2 following (or along with) the shifting of gas composition is needed. For effective integration with advanced gasification technologies, and to realize the full advantages of high-temperature gas cleaning technologies, hydrogen and CO2 separation must be accomplished at high process temperatures. High temperature operation also offers the possibility of enhancing the water-gas-shift process through integration with advanced membranes operating at similar temperatures. Technologies that are capable of producing both hydrogen and CO2 at high pressure can avoid significant recompression costs that would further enhance plant economics, particularly in the case of carbon storage which requires very high compression of the CO2.
The hydrogen transport membrane, which uses metal or metal alloy materials with surface exchange catalysts to separate hydrogen from CO2, is being aggressively developed. Several projects have developed hydrogen membranes that have achieved fluxes and hydrogen purity high enough to encourage continued development of this cutting edge technology. These technologies operate at higher process temperatures designed to integrate at increased efficiency with advanced warm syngas cleanup technologies. This also offers the possibility of enhancing water gas shift through integration with advanced membranes, since both processes operate at similar temperatures.
The primary technical challenges for membrane-based technologies include optimization of the composition and microstructure of membrane materials, development of thin defect-free membrane films for enhancing flux, development of robust seals, ability to accommodate contaminants in the syngas, and operation at high-permeate pressures.
Praxair and Worcester Polytechnic Institute are developing an integrated, cost-effective hydrogen production and separation process that employs palladium and palladium-alloy membranes.
High Hydrogen, Low Methane Syngas from Low-Rank Coals for Coal-to-Liquids Production
Southern Research Institute is investigating high-temperature steam reforming catalysts for use under the severe conditions of reforming tar, light hydrocarbons, ammonia, and methane found in raw synthesis gas from the gasification of low-rank coals in gasifiers such as TRIG and Lurgi fixed bed gasifiers. This would have the benefits of improving H2 yield, reducing water gas shift requirements, and reducing downstream gas cleanup requirements and would facilitate increase use of abundant low-rank coal for power generation and fuels synthesis.
Advanced Acid Gas Separation Technology for Clean Power and Syngas Applications
As an alternative to conventional acid gas removal (AGR), Air Products is developing a two process block, proprietary technology called Sour Pressure Swing Adsorption to remove CO2 (at a purity sufficient for sequestration) and H2S from syngas. This is expected to have significantly lower capital cost than conventional AGR technology. Air Products will do some slipstream testing on actual syngas at the National Carbon Capture Center as part of this project.
||Water-Gas Shift Vessel at the National Carbon Capture Center
Reduction of Steam Use in Water-Gas Shift (WGS)
One of the efforts at the National Carbon Capture Center at the Power Systems Development Facility involves testing of improved WGS catalysts. Results and analyses support reduction of steam-to-carbon monoxide ratios, thereby reducing steam requirement for IGCC cycles, which in turn will reduce the cost of electricity with CO2 capture.
Long-term candle filter tests (Transport Gasifier)
Researchers at the National Carbon Capture Center at the Power Systems Development Facility are utilizing the transport gasifier for testing and evaluating a particulate control device (PCD) in ongoing, long-term operation and filter element testing using a variety of fuels including coal/biomass mixtures to characterize the performance of the different technology units, their integration, and balance-of-plant processes.
Advanced Reactor Design for Integrated WGS/Pre-combustion CO2 Capture
Researchers are developing a method to produce high-hydrogen syngas utilizing a warm gas CO2 scrubber integrated with a water-gas shift catalyst, enabling economic capture of greater than 90% of the carbon emissions. Also, they are assessing the technical and economic feasibility for using this technology in IGCC and coal to chemicals plants using low-rank coal and woody biomass as feedstocks.
As part of the support for the Syngas Processing key technology, studies are being conducted to provide unbiased comparisons of competing technologies, determine the best way to integrate process technology steps, and predict the economic and environmental impacts of successful development.
Recently Completed Projects
Other key technologies within Gasification Systems include the following: