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State Key Laboratory of Coal Conversion, Institute of Coal Chemistry, Chinese Academy of Sciences, Taiyuan, Shanxi 030001, China
To improve the economy of the hydropyrolysis process by reducing the cost of hydrogen, it has been suggested that cheaper hydrogen-rich gases (such as coke-oven gas, synthesis gas) could be used instead of pure hydrogen. Pyrolysis of Chinese Xianfeng lignite was carried out with real coke-oven gas (COG) and synthesis gas (SG) as reactive gases at 0.1–5 MPa and at a final temperature up to 650°C with a heating rate of 5–25°C min−1 in a 10 g fixed-bed reactor. The results indicate that it is possible to use COG and SG instead of pure hydrogen in hydropyrolysis, but that the experimental conditions must be adjusted to optimize the yields of the valuable chemicals."
Another point to be made is that the Chinese researchers seem to indicate that "recycling" the synthesis gas derived from the coal decomposition back into the pyrolysis of more coal also improves the hydrogenation process.
But, definitely: A coal-use by-product of steel-making, coke-oven gas, which was once a troublesome and polluting effluent, can be collected and added to coal as an additional raw material which enhances and improves the conversion of coal into liquid fuel.
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The signing ceremony certified that the blended FT and JP-8 fuel is safe for operational use in all B-52H aircraft and marked the formal conclusion of testing.
"The demonstration approach approved by Secretary Wynne in April 2006 identified five execution steps," said Maj. Gen. Curtis Bedke, Air Force Flight Test Center commander. "The final execution step began on Sept. 19, 2006. A B-52 was flown at Edwards with two engines running synthetic fuel and the remaining six engines on JP-8 fuel. On Dec. 19 2006, the B-52 was flown with all eight engines on the FT blend."
The B-52H was chosen as the test platform because of key advantages such as its eight engines, he said. The fuel system can simultaneously isolate, carry and manage both a test fuel and the standard JP-8 fuel.
The Air Force plans to test and certify every airframe to fly on a domestically produced synthetic fuel blend by early 2011.
"When I asked that this development be done, the people at Wright-Patterson Air Force Base, Ohio, and the Air Force Flight Test Center were excited to push this technology on behalf of the Air Force and America," said Secretary Wynne.
Every time the price of fuel goes up $10, it costs $600 million for the Air Force, he said.
"It causes angst to know that we're faced with a commodity that some might use against us," Secretary Wynne said. "We want to provide our nation a look forward to something else and to essentially join with numerous researchers who are looking for alternatives whether it is ethanol, switch grass, biomass or Fischer-Tropsch and finding the solution. I think it is going to be a tremendous partnership across the board."
One of the things planners are looking forward to is a clean coal to liquid manufacturing process, he said.
"It may involve several manufacturing steps to essentially neutralize carbon usage and get us to what we want," Secretary Wynne said. "We want a synthetic blend that will not interrupt the flow of fuel in our aircraft and airfields and will be a viable substitute."
A 50 percent blend appears to be the right answer, he said.
There are universities across the country trying to determine why we stopped at 50 percent, Secretary Wynne said.
"So the question is how do you bring this all to fruition?" he said. "For many years into the future, it is going to be very difficult to get more than a 50/50 blend on a real basis and not in a laboratory."
Testers are very pleased with the FT fuel's performance thus far, he said. The fuel may also reduce maintenance needs.
The next aircraft to be certified for FT fuel is the C-17 Globemaster III.
"This will be a bridge into the commercial arena," Secretary Wynne said. "We are being watched by many of our airline colleagues who are not only partnering with us, but researching our data. We have developed a rigorous process to qualify this fuel and any manufactured, processed synthetic fuel and blend."
The Air Force manual is being rewritten to highlight that there is a process to qualify alternative fuels within the Air Force, he said.
Recently, the Air Force ordered 281,000 gallons of synthetic fuel for further testing on the C-17 and B-1 Lancer engines in the coming year. NASA is also interested in synthetic fuels and will receive 9,000 gallons of synthetic fuel from the Air Force so they can begin evaluating its use in various engines and systems.
"This is the tip of the spear for national energy independence and cleaner energy," Secretary Wynne said. "It is doing well for the Air Force and the nation.""--
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Stream | Destination | Typical quantities, based on 1 million tons per year coke |
Coke Oven Gas | Used as fuel gas at the coke oven battery and steel works | 50 million std.cu.ft./day |
Flushing Liquor | Recirculated back to the coke oven battery | Varies with plant design |
Waste Water | Discharged to treatment plant | Varies with plant design |
Tar | Sold as product | 29,000 gallons/day |
Ammonia/Ammonium Sulfate | Sold as product | 12 tons/day (as ammonia) |
Light Oil (if recovered) | Sold as product | 12,500 gallons/day |
Sulfur/Sulfuric Acid (if gas is desulfurized) | Sold as product | Varies with coal properties and local requirements |
"The 120 000 t/a methanol project based on coke oven gas designed by the Second Design Institute of Chemical Industry started production in Kingboard (Hebei) Coking Co., Ltd. on Sept. 5. The product reached the standard for AA-grade products in the United States. The capacity of this unit is 40 000 t/a higher than the first methanol unit based on coke oven gas in China complete in Qujing, Yunnan province in December 2004."
What all this adds up to is this:
In both indirect and direct (i.e., WVU's West Virginia Process) technologies for converting coal into liquid hydrocarbons suitable for fuel and plastics manufacturing, the coal, and it's intermediate products, must be "hydrogenated". WVU, in their direct coal liquefaction technique, as we understand it, use the solvent tetralin as the hydrogen donor.
Indirect CTL processes, such as Fischer-Tropsch and Bergius, use hydrogen derived from the coal itself, but there isn't enough to "go around". Much carbonaceous "slag" is generated, and a lot of the carbon is wasted. It has been suggested, perhaps in some places experimented with or reduced to practice, that the inclusion of biomass, or even pure hydrogen electrolyzed from water, could enable the necessary hydrogenation.
Herein, we have illustrated the possibility that an otherwise objectionable, hydrogen-rich by-product of coal use in the steel industry, coke oven flue gas, can be captured and recycled, as is, according to the above citation, apparently being done in China, into the process of converting coal into liquid hydrocarbon fuels.
We'll note also the co-production of fertilizer (ammonia), as well as other materials from which potential fuels could be derived - tar and light oil - in the coke-making process.
So, the possibility exists, as might be being realized in China, given the steel-making companies publicly known to be involved in their massive CoalTL industrialization program, to site, in an efficient and environmentally-beneficial way, a coal-to-liquid conversion facility next to a steel mill with an integral coking plant, to utilize coke oven gas as a co-feed in the synthesis of liquid hydrocarbon fuels, such as methanol, from coal.
As we've said many times: Our use of coal doesn't generate pollutants, just valuable by-products.
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"The purpose of this document is to provide information on Lurgi Coal Gasification Plants, their emissions, control technologies which can be used to control emissions, and the environmental and economic impacts of applying these control technologies. This document is being issued to assist State, local, and Regional EPA enforcement personnel in the determination (on a case-by-case basis) of the best available control technology for Lurgi Coal Gasification Plants.
Descriptors: | Air pollution; Coal gasification; Desulfurization |
Date: Reference #: | 1978 A.78.5 |
Availability: | Yes |
EPA Office: | Office of Air and Radiation |
Office Suboffice: | Office of Air Quality Planning and Standards |
Office Division: | Emission Standards and Engineering Division |
EPA Author: | NR |
Document Type: | Cost Analysis |
Contractors: | NR |
Document Status: | Final |
Pages: | 118 |
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"Title | Quantitative investigations into the environmental impact of coal gasification and hydrogenation plants |
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Creator/Author | Juentgen, H. ; van Heek, K.H. ; Kirchhoff, R. ; Klein, J. |
Publication Date | 1983 Feb 01 |
OSTI Identifier | OSTI ID: 5176028 |
Other Number(s) | Journal ID: CODEN: CHIUA |
Resource Type | Journal Article |
Resource Relation | Journal Name: Chem. Ind. (Duesseldorf); (Germany, Federal Republic of); Journal Volume: 35 |
