United States Air and Energy Engineering Environmental Protection Research Laboratory Agency Research Triangle Park NC 27711 Research and Development EPA/600/S7-87/007 May 1987 oEPA Project Summary Lime and Cement Industry Particulate Emissions: Source Category Report, Volume II. Cement Industry John S. Kinsey The objective of this study was to de- velop particulate emission factors based on cutoff size for inhalable parti- cles for the cement industry. After a review of available information charac- terizing particulate emissions from ce- ment plants, the data were summa- rized and rated in terms of reliability. Size specific emission factors were de- veloped from these data for the major processes used in the manufacture of cement. A detailed process description was presented with emphasis on fac- tors affecting the generation of emis- sions. A replacement for Section 8.6 (Portland Cement Manufacturing) of EPA report AP-42, A Compilation of Air Pollutant Emissions Factors, was pre- pared, containing the size specific emis- sion factors developed during this pro- gram. This Project Summary was devel- oped by EPA's Air and Energy Engineer- ing Research Laboratory, Research Triangle Park, NC, to announce key findings of the research project that is fully documented in a separate report of the same title {see Project Report or- dering information at back). Introduction The purpose of this program was to summarize the best available informa- tion on emissions of inhalable particu- late matter in the cement industry. The main objective of the program was to develop reliable size-specific emission factors for the various processes used in the production of cement. Both uncon- trolled and controlled emission factors are presented in the report. The uncon- trolled factors represent emissions which would result if the particulate control device (baghouse, ESP, etc.) were bypassed, and the controlled fac- tors represent emissions emanating from a particular type of control system. The size-specific emission factors are generally based on the results of simul- taneous sampling at the inlet and outlet of the control device(s), utilizing a vari- ety of particle sizing techniques. Other objectives of this program were to present current information on the ce- ment industry as well as prepare a re- placement for Section 8.6 in EPA report AP-42, "A Compilation of Air Pollutant Emissions Factors." The above objectives were met by a thorough literature search which in- cluded: Data from the inhalable particulate characterization program. Fine Particle Emissions Inventory System (FPEIS). AP-42 background file at EPA's Of- fice of Air Quality Planning and Standards (OAQPS). State and local air pollution control agencies. Various industry sources (e.g., Portland Cement Association). The emission data contained in the reference documents were reviewed, analyzed, summarized, and ranked ac- cording to the criteria established by OAQPS as published in the EPA report, "Technical Procedures for Developing ------- AP-42 Emission Factors and Preparing AP-42 Sections," April 1980. After rank- ing the data, emission factors were cal- culated using the highest quality data available. The quality of the data used to develop each emission factor is indi- cated by the emission factor rating. Process control system operating data as well as general industry infor- mation were also obtained and summa- rized as general background informa- tion. It was not part of this program to provide detailed engineering analyses, product specifications, or a detailed evaluation of trends in the industry. Summary of Results Portland cement manufacture ac- counts for about 98% of the cement pro- duction in the U.S. The more than 30 raw materials used to make cement may be divided into four basic compo- nents: lime (calcareous), silica (siliceous), alumina (argillaceous), and iron (ferriferous). In the dry process, the moisture con- tent of the raw material is reduced to less than 1%, either before or during the grinding operation. The dried materials are then pulverized and fed directly into a rotary kiln. The material is dried, de- carbonated, and calcined as it travels through the heated kiln and finally burns to incipient fusion and forms the clinker. The clinker is cooled, mixed with about 5% gypsum by weight, and ground to the final fineness. The product, cement, is then stored for later packaging and shipment. In the wet process, a slurry is made by adding water to the initial grinding op- eration. Proportioning may take place before or after the grinding step. After the materials are mixed, the excess water is removed and final adjustments are made for the desired composition. This final homogeneous mixture is fed to the kilns as a slurry (30-40% mois- ture) or as a wet filtrate (about 20% moisture). The burning, cooling, addi- tion of gypsum, and storage are then carried out as in the dry process. Particulate matter is the primary emission in the manufacture of Portland cement. Emissions also include the nor- mal tombustion products of the fuel used for heat in the kiln and drying op- erations, including nitrogen oxides and small amounts of sulfur oxides. Dust sources at cement plants are: (1) quarrying and crushing, (2) raw ma- terial storage, (3) grinding and blending (dry process only), (4) clinker produc- tion and cooling, (5) finish grinding, and (6) packaging. The largest single point of emissions is the kiln, which may be considered to have three units: the feed system, the fuel firing system, and the clinker cooling and handling system. Additional sources of dust are quarry- ing, raw material and clinker storagj piles, conveyors, storage silos, loading/ unloading facilities, and paved/unpaved roads. Depending upon the emission, the temperature of the effluents in the plant in question, and the particulate emis- sion standards in the area, the cement industry generally uses mechanical col- lectors, electrostatic precipitators, fabric filters, or combinations of these to con- trol emissions. The total mass uncontrolled emission factors for cement manufacturing are presented in Table 1, and controlled emission factors are presented in Table 2. Size-specific emission factors for ce- ment kilns are presented in Table 3, and for cement clinker coolers, in Table 4. Table 1. Uncontrolled Emission Factors for Cement Manufacturing' Emission Factor Rating: E Sulfur dioxidec Mineral Gas Oil Coal Nitrogen Particulateb sourced combustion combustion combustion oxides Lead Process kg/Mg lb/ton kg/Mg lb/ton kg/Mg lb/ton kg/Mg lb/ton kg/Mg lb/ton kg/Mg lb/ton kg/Mg lb/ton Dry process kiln 128 256 5.4 10.8 Neg Neg 2.2S 4.4S 3.6S 7.2S 1.4 2.8 0.06 0.12 Wet process kiln 120 240 5.4 10.8 Neg Neg 2.2S 4.4S 3.6S 7.2S 1.4 2.8 0.05 0.10 Clinker cooler' 4.6 9.2 Dryers, grinders, etc.f Wet process 16.0 32.0 NA NA NA NA NA NA NA NA NA NA 0.01 0.02 Dry process 48.0 96.0 NA NA NA NA NA NA NA NA NA NA 0.02 0.04 'Units of clinker produced, assuming 5% gypsum in finished cement. Includes fuel combustion emissions, which should not be calculated separately. Neg = negligible. S = % sulfur in fuel. Dash = no data. NA = not applicable. bEmission Factor Rating: B cFactors account for reactions with alkaline dust, with no controls. One test series for gas- and oil-fired wet process kilns, with limited data, suggests that 21-45% of S02 can be removed by reactions with the alkaline filter cake, if baghouses are used. dFrom sulfur in raw materials, which varies with their sources. Factors account for some residual sulfur, because of its alkalinity and affinity for S02. *Emission Factor Rating: D. 'Units of cement produced. 2 ------- Table 2. Controlled Particulate Emission Factors for Cement Manufacturing' Particulate _ . . Emission Control kg/Mg lb/ton factor Type of source technology clinker clinker rating Wet process kiln Baghouse ESP 0.57 0.39 1.1 0.78 C C Dry process kiln Multiclone Multiclone + ESP Baghouse 130" 0.34 0.16 260" 0.68 0.32 D C B Clinker cooler Gravel bed filter ESP Baghouse 0.16 0.048 0.010 0.32 0.096 0.020 C D C Primary limestone crusherc Baghouse 0.00051 0.0010 D Primary limestone screenc Baghouse 0.00011 0.00022 D Secondary limestone screen and crusher0 Baghouse 0.00016 0.00032 D Conveyor transferc Baghouse 0.000020 0.000040 D Raw mill systemc-d Baghouse 0.034 0.068 D Finish mill system" Baghouse 0.017 0.034 C *Units of kg particulete/Mg (lb particulate/ton) of clinker produced, except as noted. ESP = electrostatic precipitator. b Based on a single test of a dry process kiln fired with a combination of coke and natural gas. Not generally applicable to a broad cross section of the cement industry. cUnits of mass of pollutant/mass of raw material processed. dlncludes mill, air separator, and weigh feeder. *Includes mill, air separator(s), and one or more material transfer operations. Units of cement produced. Table 3. Size Specific Particulate Emission Factors for Cement Kilns' Emission Factor Rating: D Cumulative mass % < stated size" Cumulative emission factor < stated size' Particle size Iv-ml Uncontrolled Dry process kiln with multiclone'1 Wet process kiln with ESP Baghouse Uncontrolled Wet Dry process process Dry process with multiclone'1 Wet process with ESP Baghouse Wet process kiln Dry process kiln Wet process kiln Dry process kiln Wet process Dry process kg/Mg lb/ton kg/Mg lb/ton kg/Mg lb/ton kg/Mg lb/ton kg/Mg lb/ton kg/Mg lb/ton 2.6 7.0 18 3.8 64 NA 46 8.4 17 23 46 5.0 10 0.25 0.60 NA NA 0.073 0.15 S.0 20 NA 14 83 NA 77 24 48 19 38 0.32 0.64 NA NA 0.13 0.26 10.0 24 42 24 85 NA 84 29 58 54 108 32 64 0.33 0.66 NA NA 0.14 0.28 1S.0 35 44 31 91 NA 89 43 86 57 114 41 82 0.36 0.72 NA NA 0.16 0.30 20.0 67 NA 38 98 NA 100 68 136 49 98 0.39 0.78 NA NA 0.16 0.32 Total mass emission factor 120 240 128 266 130 260 0.39 0.78 0.67 1.1 0.16 0.32 'ESP « electrostatic precipitator. NA = not available. Dash « no data. *Aerodynamic diameter. Percentages rounded to two significant figures. «Units of weight of particulata/unit weight of clinker produced, assuming 5% gypsum in finished cement Rounded to two significant figures. *Based on a single test, and should be used with caution. 3 ------- Table 4. Size Specific Emission Factors for Clinker Coolers Emission Factor Rating: E Cumulative mass % Cumulative emission factor < stated sizeb < stated sizec Particle sizea (Vm/ Uncontrolled Gravel bed filter Uncontrolled kg/Mg lb/ton Gravel bed filter kg/Mg lb/tan 2.5 0.54 40 0.025 0.050 0.064 0.13 5.0 1.5 64 0.067 0.13 0.10 0.20 10.0 8.6 76 0.40 0.80 0.12 0.24 1S.0 21 84 0.99 2.0 0.13 0.26 20.0 34 89 1.6 3.2 0.14 0.28 Total mass emission factor 4.6 9.2 0.16 0.32 "Aerodynamic diameter. bRounded to two significant figures. cUnit weight of pollutant/unit weight of clinker produced. Rounded to two significant figures- John S. Kinsey is with Midwest Research Institute, Kansas City, MO 64110.. Dale L. Harmon is the EPA Project Officer (see below). The complete report, entitled "Lime and Cement Industry Particulate Emissions: Source Category Report, Volume II. Cement Industry," (Order No. PB 87- 168 654/AS; Cost: $36.95, 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 Project Officer can be contacted at: Air and Energy Engineering Research Laboratory U.S. Environmental Protection Agency Research Triangle Park, NC 27711 United States Onter for Environmental Research Environmental Protection Information Agency Cincinnati OH 45268 Official Business Penalty for Private Use S300 EPA/600/S7-87/007 ------- |