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Converting Waste Agricultural Biomass into a Resource - UNEP

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capability for both chemical and energy recovery, have minimal<br />

environmental impact, have a scale-up and turndown capability to meet<br />

current and future mill needs, allow the mill to continue as a zero effluent<br />

operation, and be affordable.<br />

The spent liquor gasifier is designed to processes 115 Metric tons per day of<br />

black liquor solids (at 40% moisture content). The chemicals are recovered<br />

and sent to the mill for pulping and the energy is recovered as steam which<br />

offsets the production of steam using purchased natural gas. The process<br />

started up in September of 2003. The project completed its performance test<br />

in April of 2005 and it completed air emissions testing in October 2006<br />

thereby transitioning from commissioning to full commercial operation. The<br />

gasifier has logged more than 18,000 hours of operation.<br />

Georgia-Pacific Corporation, Big Island, Virginia<br />

Georgia-Pacific Corporation, one of the world’s largest paper companies. The<br />

Big Island mill produces 900 tons per day of linerboard from OCC and 600<br />

tons per day of corrugating medium from mixed hardwoods semi-chem<br />

pulp. The project was environmentally driven and displaced two 50 year-old<br />

smelters that provided chemical recovery but no energy recovery. The project<br />

was funded 50% by the U.S. Department of Energy as a demonstration<br />

project for low temperature spent liquor gasification. The system was<br />

designed to process 200 tons per day of black liquor solids (at 40% moisture).<br />

Starting in the first quarter of 2004, Georgia-Pacific commissioned TRI’s<br />

steam reforming spent liquor gasification process at its Big Island, Virginia<br />

mill. The start-up and operation of the reformer system was not nearly as<br />

successful as the similar system at Norampac, and in October of 2006,<br />

Georgia-Pacific decided to no longer continue operation of their reformers.<br />

Their decision was based on the expected cost of modifying the reformer to<br />

improve performance. In contrast to Norampac, GP’s system was designed by<br />

another engineering company and incorporated significantly different process<br />

designs than those implemented by TRI at Norampac.<br />

Suppliers<br />

TRI<br />

3700 Koppers Street, Suite 405 Baltimore, MD 21227<br />

Telephone: 410-525-2400 Fax: 410-525-2408<br />

36

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