SBIR-STTR Award

Chemical coal cleaning at low caustic/coal ratios
Award last edited on: 2/20/02

Sponsored Program
SBIR
Awarding Agency
DOE
Total Award Amount
$530,101
Award Phase
2
Solicitation Topic Code
-----

Principal Investigator
Sac Nguyen

Company Information

Pacific Creative Research

5450 University Avenue Suite D
San Diego, CA 92105
   (619) 229-0051
   N/A
   N/A
Location: Single
Congr. District: 51
County: San Diego

Phase I

Contract Number: ----------
Start Date: 00/00/00    Completed: 00/00/00
Phase I year
1990
Phase I Amount
$49,981
Coal will be chemically cleaned using sodium hydroxide ascaustic at temperatures of 350' to 390'C, using caustic-to-coalratios of 2:1 and lower. Recent experience in 10 lb/hr kiln runshas shown that ratios in the range of 2:1 to 1:1 may cause a pastymass to form that sticks to the reactor wall and prevents heattransfer for reactants subsequently passing through the kiln. InPhase I experiments will be run that test the viscosity of lowcaustic-to-coal ratios at several temperatures to determine if aregime exists that is chemically and mechanically operable forcleaning coal. A laboratory-scale, stirred batch reactor will beconstructed for conducting tests to determine the limits ofcaustic-to-coal ratios that give good operability, as a guide forkiln runs. The product coal quality attained, sulfur, ash,volatiles content, Btu/lb, and surface area will be determined. Correlations will be developed relating reactor conditions,temperature and caustic-to-coal ratio, with product quality forcleaned coal product.Anticipated Results/Potential Commercial Applications as described by the awardee:Molten caustic leaching (MCL) is the onlyforeseeable cleaning method available for new plants to burn lowsulfur coal in compliance with the New Source PerformanceStandards. Because the economics of the present technologies arequestionable, no plan exists to commercialize MCL; new ideas areneeded. Continuous kiln tests give low sulfur product only whenhigher caustic-to-coal ratios are used. A test plan is plannedusing lower ratios that could lead to less expensive treatingconditions.

Phase II

Contract Number: ----------
Start Date: 00/00/00    Completed: 00/00/00
Phase II year
1991
Phase II Amount
$480,120
This project is to develop a technology under which coal will be chemically cleaned using sodium hydroxide as caustic at temperatures of 330ø to 390øC, using caustic-to-coal ratios of 1:1 and lower. Recent experiments in Phase I have shown that ratios in the range of 0.50:1 to 1.0:1 are as effective as 2.0:1 for molten-caustic leaching of coal. No problems due to crusting or viscosity of low caustic/coal ratios were encountered at any temperature in the range of 271ø to 390øC and the system was both mechanically and chemically operable for the cleaning of coal in a laboratory-scale, stirred, dry mix, batch reactor. In Phase II, additional testing will be conducted at low caustic-to-coal ratios and moderate temperatures to study the effect of residence time on sulfur removal, as a guide for subsequent kiln runs. Product yield, sulfur, ash, volatiles content, and Btu/lb will be determined. Correlations will be developed relating reactor conditions with product quality for cleaned coal product. This investigation will conclude with kiln tests at conditions selected from the laboratory work to prove the efficacy of low caustic-to-coal ratios to produce chemically cleaned coal meeting the New Sources Performance Standards (NSPS).Anticipated Results/Potential Commercial Applications as described by the awardee:Molten-caustic leaching is the only foreseeable technique for cleaning coal so that its sulfur level meets NSPS requirements. Success in laboratory work at low NaOH/coal ratios is strong evidence that it has commercial potential. Larger scale kiln tests are needed to prove the validity of this technolo