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2005 TAG Meeting Evaluation of Thermal Processes for CCA Wood Disposal in Existing Facilities Anadi Misra1, Brajesh Dubey1, Chang-Yu Wu1, Timothy Townsend1,

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Presentation on theme: "2005 TAG Meeting Evaluation of Thermal Processes for CCA Wood Disposal in Existing Facilities Anadi Misra1, Brajesh Dubey1, Chang-Yu Wu1, Timothy Townsend1,"— Presentation transcript:

1 2005 TAG Meeting Evaluation of Thermal Processes for CCA Wood Disposal in Existing Facilities Anadi Misra1, Brajesh Dubey1, Chang-Yu Wu1, Timothy Townsend1, Helena Solo-Gabriele2 1University of Florida 2University of Miami Aerosol and Particulate Research Laboratory November 8, 2018

2 Aerosol and Particulate Research Laboratory
Overview Background Methodology Task 1: Inventory of Combustion Facilities Task 2: Survey of Arsenic air pollution control technologies Task 3: Screening of potential materials for minimizing leaching Results and Discussions Summary and Future Work Why is the disposal of CCA wood through thermal processes an issue ? Proposed solution Aerosol and Particulate Research Laboratory November 8, 2018

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Background: CCA Wood Currently not considered hazardous under Resource Conservation & Recovery Act (RCRA) which monitors hazardous waste Disposed alongside other wood waste in Construction & Demolition (C & D) debris landfill ~ 60% is burned to produce energy Aerosol and Particulate Research Laboratory November 8, 2018

4 Background: Problems with incineration of CCA Wood
Heavy Metal Emissions from combustion Leaching of Heavy Metals from Ash into Groundwater Rain Volatilization and entrainment, metals in submicron range, difficult to capture, Contaminated Soil Ground Water National Physical Lab: Aerosol and Particulate Research Laboratory November 8, 2018

5 Aerosol and Particulate Research Laboratory
Proposed Solution Use mineral sorbents (e.g. lime) for Preventing emission of metals Preventing leaching of metals from incinerator ash Many sorbents have good capture efficiency with respect to metal emissions ( Venkatesh et al, 1996, Kenjiro et al, 2004)  so we have focused on the leaching behavior of CCA metals on interaction with sorbents Activated Carbon Injection : Aerosol and Particulate Research Laboratory November 8, 2018

6 Aerosol and Particulate Research Laboratory
Methodology Task 1: Inventory of Existing Major Wood-Fired Capable Facilities Task 2: Survey of Available Arsenic Air Pollution Control Technologies Task 3: Screening of Potential Materials for Preventing Heavy Metal Leaching from Incineration Product Task 1 was reported in the last TAG meeting too. Thanks to FDEP officials. As is much more volatile and has been reported to be the main metal in leaching. Then state that there is limited resource and time for this project. So, we only focus on As for this project. Aerosol and Particulate Research Laboratory November 8, 2018

7 Task 1: Inventory of Combustion Facilities in Florida
Type Max. Heat input rate Types of fuels used Air pollution control devices Cement Kiln (7) MMBtu/hr Coal (bituminous usually), whole tires, propane, natural gas, petroleum coke, propane, No. 2 fuel oil, residual fuel oil, No. 6 fuel oil Baghouses, ESPs Coal Fired (14) Coal (bituminous , pulverized, latex coated, mixed with petroleum coke), natural gas, Nos.1,2 & 6 fuel oil, carbonaceous fuel, Briquette Mixture, refuse derived fuel (RDF) Cold side & Hot side ESP, flue gas desulphurization (FGD) unit, wet caustic scrubber , Selective Non Catalytic Reduction system (SNCR) , spray dryer absorber, and fabric filter baghouse The details are available on our website Aerosol and Particulate Research Laboratory November 8, 2018

8 Task 1: Inventory of Combustion Facilities in Florida (cont.)
Type Max. Heat input rate Types of fuels used Air pollution control devices Wood Fired (31) MMBtu/hr carbonaceous fuel (bagasse, wood chips, rice hulls), natural gas, bark and primary clarified wood fibers, dry wood waste, combination of waste wood and paper( with some lesser amounts of peanut hulls, lumber, oily rags, oil soaked peat moss) MSW, Coal, No. 2 & 6 fuels, oil soaked paper towels, biomass, sugar mill waste, tires, landfill gas. fly ash arrestor, wet caustic scrubber , SNCR, Multicyclone, ESP, venturi scrubber, multiple tube dry collectors, Joy type Impingement Scrubber, spray dryer absorber, fabric filter WTE (14) MMBtu/hr MSW fabric filter baghouse, spray dry absorbers, activated carbon injection system, SCNR , dry scrubber, mercury abatement systems, ESP There are a lot more wood fired boilers, and their capacities are typically smaller. So, from the data, we can see there are many types of fuels used which will definitely affect the chemistry of CCA metals in the combustion system and therefore their fate. Also, the air pollution control devices are very different from one category to the other. Aerosol and Particulate Research Laboratory November 8, 2018 Back

9 Task 2: Arsenic Pollution Control Technologies
Reduction in emissions Co-incineration along with dilution Low temperature pyrolysis Capture of emissions Combination of filters and scrubbers Sorbent injection combined with filtration Briefly discuss the pros and cons of these technologies. Do not just read your text. Ultimately, you want to lead to sorbent injection as the best choice.Also briefly metion other industries that have arsenic as a focus metal to deal with. Pyrolysis Furnace Econ Systems: Baghouse Aerosol and Particulate Research Laboratory November 8, 2018 Back

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Task 3: Screening of Potential Materials for Preventing Heavy Metal Leaching from Incineration Product Evaluate Potential mineral sorbents in combustion environments Analysis of Ash by Toxicity Characteristic Leaching Procedure (TCLP) for leaching properties X-Ray Diffraction (XRD) to identify the crystalline composition Aerosol and Particulate Research Laboratory November 8, 2018

11 List of Sorbents Used in Experiments
Name of Sorbent Chemical formula Alumina Al2O3 Attapulgite Clay* Si16Mg H3.6O 5.9 Calcium Hydroxide Ca(OH)2 Cement* Si9Al3Ca 29.3 S0.8 H3Fe1O57 Diatomaceous Earth* Si106Al4.6Ca 0.3 Mg0.5Fe2O229.5 Ferric Oxide Fe2O3 Kaolin H2Al2Si2O8-H2O Magnesium Hydroxide Mg(OH)2 Silica SiO2 *Approximate molecular formula based on % composition. Varies according to mineral composition Aerosol and Particulate Research Laboratory November 8, 2018

12 Experimental Procedure
Prepared a spike sample of CCA metals having same concentration as that of CCA Type C chemical (47.5% CrO3, 18.5% CuO & 34% As2O5) Heated sorbent and spike sample at 700oC, 900oC & 1100oC for 30 minutes Analysis of the residue TCLP Leaching tests Speciation characterization by XRD Aerosol and Particulate Research Laboratory November 8, 2018

13 Results: Arsenic Retention in Residue
Ca(OH)2 , Cement and Mg(OH)2 show over 98% retention for As at both temperatures Alumina & Diatomaceous Earth show over 80% retention at 900oC This is a separate question from the presentation, but related to your study. Will a higher Cu content result in lower As leaching? Please also check the soluability of CuCr2O4 and Cu3(AsO4)2. Aerosol and Particulate Research Laboratory November 8, 2018

14 Results: Arsenic Leaching from Residue
Cement, Ca(OH)2 and Mg(OH)2 leach less than 5 mg/l of arsenic in both cases All other sorbents exceed the TC limit for leaching Aerosol and Particulate Research Laboratory November 8, 2018

15 Results: Chromium Retention in Residue
Alumina, Silica, Kaolin & Diatomaceous Earth show over 90% retention for Cr at both temperatures Attapulgite Clay shows higher Cr retention at 900oC Ca(OH)2 and Cement show negligible retention Aerosol and Particulate Research Laboratory November 8, 2018

16 Results: Chromium Leaching from Residue
Alumina and Silica leach less than 5 mg/l of Cr at both temperatures Kaolin leaches less than 5 mg/l of Cr at 900oC All other sorbents exceed the TC limit at both temperatures Diatomaceous Earth doesn’t work well in either case Aerosol and Particulate Research Laboratory November 8, 2018

17 Results: Copper Retention in Residue
All sorbents except silica and attapulgite clay show ~80% or greater retention at both temperatures Cement, Ca(OH)2 , Mg(OH)2 show over 98% retention at both temperatures and Kaolin at 900oC Aerosol and Particulate Research Laboratory November 8, 2018

18 Aerosol and Particulate Research Laboratory
Major XRD Results The major metal-mineral compounds formed in spike samples are Cu3(AsO4)2 , Ca3(AsO4)2 CuHAsO4, CaCrO4 etc., when Cement and Ca(OH)2 are used CuCr2O4, ,when Alumina and Silica are used Cu has high affinity for forming compounds The difference in efficiency can be due to the different speciation products observed in the residue It is possible that these compounds have low solubility, hence are less leachable. Remember to point to the symbols when you define the species in the figure to guide your audience. Aerosol and Particulate Research Laboratory November 8, 2018

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Summary Cement, Ca(OH)2 & Mg(OH)2 are good at retaining and preventing leaching of As & Cu Alumina & Silica are good at retaining and preventing leaching of Cr The variation in metal-metal and metal-mineral compounds being formed could be the major reason for different retention capabilities. Understanding their interaction will provide solution to the challenging issue of CCA wood disposal. Aerosol and Particulate Research Laboratory November 8, 2018

20 Aerosol and Particulate Research Laboratory
How can we utilize this study for effective control of heavy metals during combustion of CCA wood? Provide Ca-based sorbent A possible strategy involving Cement, Ca-based sorbents to chemically adsorb arsenic in air stream Alumina, Silica to retain chromium in feed As in gas phase Cr in feed Provide alumina/silica Potentially viable option for disposal: Cement kiln Coal-fired power plants equipped with SO2 scrubbers Steel mills Since, arsenic is the only metal which vaporizes in usual combustion environments (< 1200oC), so, Refresh their memory about the excellent performance of each sorbent with specific metal. 1. The major constituent of coal ash is alumino-silicate. Hence, co-burning with coal has the advantage with no need for extra alumina/silica. 2. The arsenice containing flue gas will pass the kiln where cement material is roasting. Your Phase 1 results clear show its beauty of scrubbing As out of flue gas. There is no need for adding Ca-based sorbent. Cement itself is a Ca-based sorbent. The great thing about the use of the cement process is that essentially you don't need to add anything else; thus, you can reduce the cost and it's really easy to adopt. Additionally, it will be good to show the flow direction of As and Cr. Aerosol and Particulate Research Laboratory November 8, 2018

21 Aerosol and Particulate Research Laboratory
Acknowledgements Financial Support by Florida Center for Solid and Hazardous Waste Management Grant# Major Analytical Instrumentation Center, Department of Material Science and Engineering, UF Particle Engineering Research Center, UF Officials at Florida Department of Environmental Protection (FDEP) Mr. Henry Gotsch, Florida Rock Industries Inc. Sang-Rin Lee, Clarkson University Aerosol and Particulate Research Laboratory November 8, 2018

22 Aerosol and Particulate Research Laboratory
Thank You Aerosol and Particulate Research Laboratory November 8, 2018

23 Aerosol and Particulate Research Laboratory
Aerosol and Particulate Research Laboratory November 8, 2018


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