United States Environmental Protection Agency Hazardous Waste Engineering Research Laboratory Cincinnati OH 45268 Research and Development EPA/600/S2-85/082 Dec. 1985 ŁEPA Project Summary Interim Report on PIC Minimization in a Research Combustor Laurel J. Staley A series of five organic compounds (1,1,2,2-tetrachloroethane, trichloro- ethylene, Freon-113, carbon tetrachlo- ride and chlorobenzene) were burned in heptane in a 100,000 Btu/hour water- jacketed research combustor in order to determine what, if any, PICs (Prod- ucts of Incomplete Combustion) formed under conditions of extreme flame quenching. For each test, excess air levels were varied from 120% of the- oretical air to 240% of theoretical air which, for the combustor used, repre- sented the limits of flame stability. Re- sults show that PICs do not always occur predictably, but are very much in- fluenced by the POHC (Principal Or- ganic Hazardous Constituent) being burned. Where they do occur, however, the emission levels of PICs increase with increasing levels of excess air, over the range of air levels investigated. This report covers the period of January-March 1985, and the work was completed as of March 31, 1985. This Project Summary was devel- oped by EPA's Hazardous Waste Engi- neering Research Laboratory, Cincin- nati, OH, to announce key findings of the research project that is fully docu- mented in a separate report of the same title (see Project Report ordering infor- mation at back). Introduction Although the Resource Conservation and Recovery Act regulations require 99.99% Destruction and Removal Effi- ciency (ORE) with respect to Principal Organic Hazardous Constituents (POHCs), those chemical contami- nants within a hazardous waste stream that are burned by an incinera- tor, there is also a concern about Prod- ucts of Incomplete Combustion (PICs). These latter compounds are formed even as the POHCs in the incinerator are destroyed. They can be more toxic than the original feed chemicals. Thus, under those unwanted combus- tion conditions that favor the forma- tion of PICs, hazardous waste inciner- ation may give rise to a potentially serious air pollution problem. The purpose of the work described in the full report is to identify certain sets of conditions under which PICs form or are more prevalent so that future work can focus on how and why they form and how to minimize their formation. Contained within the full report is a de- scription of the combustor and auxiliary equipment used in the study, a descrip- tion of the experiments conducted, and discussions of the results and the impli- cations of the work. The work described is preliminary and rather limited; all conclusions are tentative and subject to verification. Experimental Design Figure 1 is a sketch of the Turbulent Flame Reactor (TFR) which was used to conduct the experimentation. The purpose of the experiment was to determine those operating regimes which allowed (1) incomplete burning of POHCs, and (2) formation of significant levels of PIC. A further objective was to compare the POHC and PIC levels thus produced with concentrations that result from flameout. The above objectives were accom- plished by burning five compounds (trichloroethylene (TCE), carbon tetra- chloride, tetrachloroethane, chloroben- zene and Freon-113) in a series of five separate combustion tests. For each of the five tests, the compound of interest was present as a 2.0 mole percent solu- tion in heptane in the combustor feed. ------- To CO CO2 + 0 Monitors To TENAX (Heated Line) To THC Monitor -Ov N. X \ ^x - T.C. for Exhaust Gas Temp ' H20 Air (From Compressor) Swirl Vane Adjustment IT a Heptane & Waste Compound Figure 1. Turbulent flame reactor. In a sixth test, Freon-113 and chloro- benzene were burned together to deter- mine if there were any mixture effects which influenced POHC destruction and/or PIC formation. For this test, both Freon-113 and chlorobenzene were present at the same concentrations (two mole percent each) as when they were burned separately. This resulted in a total POHC concentration of four mole percent for this test. In each test, the firing rate of heptane/ POHC was held constant while the com- bustion air flow rate was varied to pro- duce (CO) levels which spanned the range of observable values. At five or sometimes six different sets of operat- ing conditions corresponding to five or six different CO levels, Tenax trap sam- ples were taken for purposes of deter- mining POHC destruction and PIC for- mation. At one point during each test, the flame was purposely extinguished dur- ing a sampling run. Sampling contin- ued. Theoretically, when the flame goes out, there should be a discharge of soot and PIC-laden exhaust gas from the re- actor. The objective was to sample this emission and measure the unburned POHCs as well as to determine the types and levels of PICs produced during this "upset" condition. (It should be noted that all discharges from the TFR were scrubbed and filtered through an acti- vated carbon filter to remove pollutants prior to discharge to the atmosphere.) Results and Conclusions The DREs achieved throughout this test series exceeded 99.99% in 62.5% of the tests. For the remaining tests, ORE exceeded 99.9% except for the three times (two of which were flameouts) in which the ORE was slightly less than 99.9%. Fuel-lean combustion resulted in the highest levels of PICs and unburned POHCs. Emission levels of PICs and POHCs increased with increasing ex- cess air levels. One explanation for this trend is that the temperature drop brought about by flooding the TFR with excess cold combustion air quenched the combustion reactions before they could reach completion. Stable com- bustion intermediates present when the reaction was quenched (either POHCs or PICs) were emitted in the discharge. POHC and PIC levels produced under relatively fuel-rich combustion condi- tions were consistently low even though elevated carbon monoxide lev- els indicated that combustion condi- tions were poor. Even though the POHCs were apparently destroyed, it is conceivable that PICs may still be form- ing under these conditions. The PICs produced under relatively fuel-rich con- ditions could possibly be different from those produced under fuel-lean condi- tions and perhaps were not detectable using the methods and equipment used to analyze the samples generated dur- ing this study. Types and amounts of PICs produced during flameouts were not appreciably different from those produced during fuel-lean operation. This is significant. Flameouts are momentary upsets which result in the production of a finite amount of POHC- and PIC-laden ex- haust gas. Excessively fuel-lean com- bustion, however, often results in a stable though inefficient flame which can emit POHC- and PIC-laden gases for hours. In two cases, these experiments have identified hard-to-burn POHCs that con- tradict previous expectations of inciner- ability based on heats of combustion and degree of halogenation. On the basis of the limited data gathered in these tests, no conclusions can be drawn regarding the setting of poten- tially new criteria for choosing POHCs and predicting which PICs can form ------- under a particular set of combustion conditions. Yet these results and those of other researchers in the field may be the basis for developing a more accu- rate way of identifying "hard-to-burn" POHCs and predicting PIC formation. ------- The EPA author, LaurelJ. Staleyfalso the EPA Project Officer, see below), is with Hazardous Waste Engineering Research Laboratory, Cincinnati, OH 45268. The complete report, entitled "Interim Report on PIC Minimization in a Research Combustor," (Order No. PB 85-233 336/AS; Cost: $7.00, subject to change) will be available only from: National Technical Information Service 5285 Port Royal Road Springfield, VA 22161 Telephone: 703-487-4650 The EPA Project Officer can be contacted at: Hazardous Waste Engineering Research Laboratory U.S. Environmental Protection Agency Cincinnati, OH 45268 United States Environmental Protection Agency Center for Environmental Research Information Cincinnati OH 45268 BULK RATE POSTAGE & FEES P EPA PERMIT No. G-35 Official Business Penalty for Private Use $300 EPA/600/S2-85/082 ------- |