United States Environmental Protection Agency Hazardous Waste Engineering Research Laboratory Cincinnati OH 45268 Research and Development EPA/600/S2-86/038 Sept. 1986 Project Summary Interim Report on Non-Flame Hazardous Waste Thermal Destruction M. Malanchuk The thermal decomposition of toxic organic compounds is being investi- gated in a laboratory system dedicated to the non-flame mode/zone of the combustion process. The early phase of this study has focused on three com- pounds: pentachloronitrobenzene (a fungicide), chloroform (a ubiquitous in- dustrial compound) and heptane. The results of the third compound, heptane, are preliminary to those sought for a mixture of two or more compounds such as chloroform, a toxic substance, and heptane, a combustion process fuel. The data of this report were collected during the period January - June 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 orderirtg infor- mation at back). Introduction In the thermal destruction of haz- ardous organic waste material; the in- teractions of the gaseous components in the post-flame or the non-flame zone of the combustion process make an im- portant contribution to the overall re- sults. The thermal decomposition in those zones can range from simple py- rolysis in an oxygen-deficient atmos- phere as might occur in a boiler, to a thermal-oxidative treatment with a con- siderable excess of oxygen as can occur in a liquid injection incinerator sup- ported by a secondary combustion zone or supply of air. A laboratory unit, identified as the Thermal Decomposition Unit-Gas Chro- matograph (TDU-GC), has been used to investigate key thermal decomposition factors of the post-flame zone, such as time of exposure and temperature, and their impact upon the effluent decom- position products. The TDU-GC was de- veloped at the University of Dayton Re- search Institute (UDRI) and has been applied by Institute personnel over the past several years to study many differ- ent organic compounds. The TDU-GC at the U.S. Environmen- tal Protection Agency (EPA) Center Hill Facility has been used thus far to inves- tigate pentachloronitrobenzene (PCNB) and also chloroform in order to deter- mine the level of reproducibility as mea- sured by the comparison of these find- ings to those reported by the UDRI for the same compounds. The thermal decomposition of hep- tane was also investigated in a prelimi- nary step to determine the effect of its presence upon chloroform decomposi- tion; this simulates the use of heptane as a co-fired fuel or solvent for a haz- ardous waste constituent such as chlo- roform. Experimental Procedure The principal equipment used in this study was the TDU-GC system, a closed in-line system consisting of two basic units, the thermal reactor and the ana- lyzer, a gas chromatograph. These units are shown in Figure 1. 1. The thermal reactor incorporates a capillary quartz tube within a furnace with three heating zones that are inde- ------- Sample Figure 1. Basic schematic of TDU-GC system. pendently controlled to produce tem- peratures up to 1150°C in the central zone for thermally decomposing the sample compound in its gaseous state. A tubular quartz extension at the en- trance of the furnace transfers the feed gas from the larger-bore sample inser- tion chamber. That chamber is fitted with any one of several probes adapted to handle gas, liquid or solid samples. A temperature programmer controls the heating jacket on the insertion chamber, for converting the liquid and solid sam- ples to the vapor phase at selected ele- vated temperatures. The vapor or gas is conveyed to the reactor by a controlled flow of carrier gas which is selected ac- cording to the nature of the atmosphere required in the high-temperature zone of the reactor. According to the temper- ature and pressure measured in the re- actor tube, the carrier gas flow is regu- lated at the instrument console to result in a precise residence time of the vapor- ized/gaseous sample in the closely- controlled high-temperature zone. The gaseous emissions from the reac- tor pass through a capillary tube into an in-line tubular trap controlled to sub- ambient temperatures as low as -50°C and colder. The trap is located inside the wall of the gas chromatograph (GC) and is very short (several mm) section of the extension of the GC capillary column into the 30:1 splitter tubing. 2. The gas chromatograph is fitted with a fused silica capillary column leading to a flame ionization detector (FID). Heating the trap transfers, via the 30:1 splitter, the smaller stream of trapped emissions sample to the front end of the capillary column which itself is at the sub-ambient temperature. Upon injection of the sample into the GC, as initiated by the switch on the supporting computer, the temperature program for the capillary column con- trols the separation of the components of the reactor emissions sample and their ensuing detection and measure- ment by the FID. The computer coupled with a re- corder provides a means of storing the output from the FID and of depicting it in a chromatogram as well as in a tabu- lation of the various peak areas. 3. The Principal Organic Hazardous Constituent (POHC) material under in- vestigation was introduced into the in- sertion chamber as a gas, liquid or solid. The more volatile, low molecular weight compounds were generally fed by syringe to the TDU-GC system as gaseous samples prepared at known concentrations. For various organic liquids, nanoliter quantities were injected directly into the insertion chamber where the sample was converted to the vapor form by a programmed temperature increase that provided transfer by the carrier gas into the thermal reactor. 4. Samples of organic solids were de- posited as measured amounts in solu- tion onto the end of the "solids" probe. Evaporation of the solvent left a residue which in the confines of the insertion chamber was transformed to the vapor state for transfer into the thermal reac- tor by the carrier gas. Results TDU-GC test run series were made on (1) pentachloronitrobenzene (PCNB) as a single component feed, (2) chloro- form, also as a single component feed, and (3) chloroform in solution with "fuel" heptane constituting the bulk of the organic feed. The results for PCNB are presented in Figure 2 as a plot of reactor effluent con- centrations vs. exposure temperature. Curve A in that figure shows the in- crease in decomposition of the POHC material, the feed PCNB, in an oxidative atmosphere with increasing tempera- ture. Curves B, C, D present the concen- trations for the more abundant PICs that were produced in the thermal treatment process. PIC component B was subse- quently identified as hexachloroben- zene (HCB). Chloroform in the predominantly oxi- dative atmosphere produced major quantities of several PICs. These are identified in Figure 3 as hexachloro- ethane (C2CI6), tetrachloroethylene (C2CI4) and carbon tetrachloride (CCI4). The highest reactor temperature inves- tigated was 625°C, at which level essen- tially total destruction (>99.99% DE) of the POHC (chloroform) had occurred. Chloroform as one of several organic compounds that might be found in a feed mixture in an actual incinerator, was selected for mixture (solution) in "fuel" heptane to undergo thermal de- composition treatment. Initially, hep- tane alone was investigated at various temperatures to characterize its decom- position, Figure 4. The high tempera- ture of 675° was considered adequate to bracket the high for total chloroform de- composition, namely the 625°C ob- served in Figure 3. When a three weight percent of chloroform was added to the heptane, its products, as observed for pure chloroform in Figure 3, were com- pletely masked by the peaks of "pollutant" components present in the heptane. Those pollutants were domi- nant even at a low, non-decomposing temperature, 300°C, for heptane. Discussion The test runs with PCNB and with pure chloroform were made primarily to check for inter-laboratory reproduci- bility. The PCNB results from the present study yielded a decomposition curve for PCNB that closely matched that re- ported by the University of Dayton Research Institute (UDRI). The hex- achlorobenzene formation/decomposi- tion profile, Curve B of Figure 2 also closely matched that reported by UDRI. The results for pure chloroform showed very good agreement with those presented by UDRI in some of ------- IUU 50 •S T §> i" £ § £ » 10 it ' *-2 |f u / || 0.5 0 | i p Is ai $ a 0.05 i2 'o 0.01 , - • , • ^^ '^ 1 \ 1 V ^ A. fl A c f Jk^ ; M\ i/ L- // /f •> \i : *• 'ii y '/ i i i i i j r r- A—Pentachloronitrobenzene \ -• — »•-• B—Hexachlorobenzene, PIC #1 -•— «-r-»- C—PICH2 ^__>.^. _ _.- „_ ... . I ... 1 200 300 700 500 2. 400 500 600 Exposure Temperature, °C Thermal treatment of pentachloronitrobemene. PCNB (i, = 2.0 sec). 900 0.01 200 300 400 500 fiOO Exposure Temperature, °C Figure 3. Thermal treatment of chloroform (i, = 2.0 sec). 70O 800 9OO their earlier work with toxic organic compounds, not only for the feed mate- rial but also for the three major PICs shown in Figure 3. It is evident, from the chlorine-saturated state of each of the PIC molecules (CCI4, C2C\4, C2C\e) identi- fied in major concentrations, that the hydrogen atom present in the parent chloroform molecule is being thor- oughly eliminated from the organic product species. Figure 5 presents the data for chloroform on a linear scale, in contrast to the semi-log scale of Fig- ure 3; it readily shows the comparative amounts of compounds present in the emissions from the thermal reactor. It is evident from Figure 5 that the concen- tration of the hexachloroethane (C2Cle) has peaked at a temperature (~570°C) where the tetrachloroethylene (C2CI4) and carbon tetrachloride (CCI4) are only beginning to form. In light of the effective masking of the GC peaks for chloroform and its prod- ucts by the heptane source pollutants, the results are limited to a decomposi- tion profile for heptane. Figure 4. The moderate slope of the decomposition curve at the high temperatures indi- cates the more refractory nature of the compound, so that by 675°C, a full 125°C after the start of decomposition at 550°C, a little more than one percent of the heptane still persists in the effluent stream from the reactor. Conclusions and Recommendations The Thermal Decomposition Unit-Gas Chromatograph (TDU-GC) system has been used in obtaining thermal decom- position profiles for several organic compounds associated with the inciner- ation of toxic/hazardous organic waste substances. The system has been used success- fully to demonstrate reproducibility of results consistent with the findings of other investigations using similar equipment. From the experience with heptane as a component in the feed, it appears nec- essary, for accurate measurement of the effects of feed composition, to limit mixtures to a very few, perhaps only two, compounds that are individually "clean" in any GC analysis. For more fully characterizing the ther- mal reactor emissions with respect to PICs, more extensive procedures in- volving additional instrumentation is needed to identify and quantify PIC compounds. A Mass Selective Detector ------- 100 so JO •I 5 .5 0. I 0.1 O.OS 0.01 200 300 400 500 600 Exposure Temperature, °C Figure 4. Thermal treatment of heptane (i, = 2.0 sec). 700 800 900 (MSD) dedicated to the TDU-GC system is the instrument of choice, both for ac- curacy of determinations and for vol- ume of work that can be expedited. ------- 100 90 80 70 60 1 50 I 40 30 20 10 •*——t- CWC/3 —-»-•--• CzC/4 -°—"—* CC/4 -I 200 300 400 500 500 700 SOO SOO Exposure Temperature. °C Figure 5. Thermal treatment of chloroform (i, = 2.0 sec). The EPA author M. Maltnchuk is with the Hazardous Waste Engineering Research Laboratory, Cincinnati, OH 45268. The complete report, entitled "Interim Report on Non-Flame Hazardous Waste Thermal Destruction," (Order No, PB 86-176 435/AS; Cost: $9.95, 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 author 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 PA EPA PERMIT No. G-35 Official Business Penalty for Private Use $300 EPA/600/S2-86/038 0000329 PS 60604 * U S GOVERNMENT PRINTING OFFICE, 1986 — 646-017/47153 ------- |