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A.A. Lizzio

Publications and source records attributed to A.A. Lizzio.

13 recordsLinked to original sources
USGS2000

High temperature hydrogen sulfide adsorption on activated carbon - I. Effects of gas composition and metal addition

Various types of activated carbon sorbents were evaluated for their ability to remove H2S from a simulated coal gas stream at a temperature of 550 ??C. The ability of activated carbon to remove H2S at elevated temperature was examined as a function of carbon surface chemistry (oxidation, thermal desorption, and metal addition), and gas composition. A sorbent prepared by steam activation, HNO3 oxidation and impregnated with Zn, and tested in a gas stream containing 0.5% H2S, 50% CO2 and 49.5% N2, had the greatest H2S adsorption capacity. Addition of H2, CO, and H2O to the inlet gas stream reduced H2S breakthrough time and H2S adsorption capacity. A Zn impregnated activated carbon, when tested using a simulated coal gas containing 0.5% H2S, 49.5% N2, 13% H2, 8.5% H2O, 21% CO, and 7.5% CO2, had a breakthrough time of 75 min, which was less than 25 percent of the length of breakthrough for screening experiments performed with a simplified gas mixture of 0.5% H2S, 50% CO2, and 49.5% N2.

Carbon↗
USGS1997

Production of activated char from Illinois coal for flue gas cleanup

Activated chars were produced from Illinois coal and tested in several flue gas cleanup applications. High-activity chars that showed excellent potential for both SO 2 and NO x removal were prepared from an Illinois No. 2 bituminous coal. The SO 2 (120 °C) and NO x (25 °C) removal performance of one char compared favorably with that of a commercial activated carbon (Calgon Centaur). The NO x removal performance of the same char at 120 °C exceeded that of the Centaur carbon by more than 1 order of magnitude. Novel char preparation methods were developed including oxidation/thermal desorption and hydrogen treatments, which increased and preserved, respectively, the active sites for SO 2 and NO x adsorption. The results of combined SO 2 /NO x removal tests, however, suggest that SO 2 and NO x compete for similar adsorption sites and SO 2 seems to be more strongly adsorbed than NO. A low-activity, low-cost char was also developed for cleanup of incinerator flue gas. A three-step method involving coal preoxidation, pyrolysis, and CO 2 activation was used to produce the char from Illinois coal. Five hundred pounds of the char was tested on a slipstream of flue gas from a commercial incinerator in Germany. The char was effective in removing >97% of the dioxins and furans present in the flue gas; mercury levels were below detectable limits.

Energy and Fuels↗
USGS1997

Adsorbed natural gas storage with activated carbons made from Illinois coals and scrap tires

Activated carbons for natural gas storage were produced from Illinois bituminous coals (IBC-102 and IBC-106) and scrap tires by physical activation with steam or CO 2 and by chemical activation with KOH, H 3 PO 4 , or ZnCl 2 . The products were characterized for N 2 -BET area, micropore volume, bulk density, pore size distribution, and volumetric methane storage capacity ( V m / V s ). V m / V s values for Illinois coal-derived carbons ranged from 54 to 83 cm 3 /cm 3 , which are 35−55% of a target value of 150 cm 3 /cm 3 . Both granular and pelletized carbons made with preoxidized Illinois coal gave higher micropore volumes and larger V m / V s values than those made without preoxidation. This confirmed that preoxidation is a desirable step in the production of carbons from caking materials. Pelletization of preoxidized IBC-106 coal, followed by steam activation, resulted in the highest V m / V s value. With roughly the same micropore volume, pelletization alone increased V m / V s of coal carbon by 10%. Tire-derived carbons had V m / V s values ranging from 44 to 53 cm 3 /cm 3 , lower than those of coal carbons due to their lower bulk densities. Pelletization of the tire carbons increased bulk density up to 160%. However, this increase was offset by a decrease in micropore volume of the pelletized materials, presumably due to the pellet binder. As a result, V m / V s values were about the same for granular and pelletized tire carbons. Compared with coal carbons, tire carbons had a higher percentage of mesopores and macropores.

Energy and Fuels↗
USGS1997

Adsorption of SO 2 onto oxidized and heat-treated activated carbon fibers (ACFs)

A series of activated carbon fibers (ACFs) and heat-treated oxidized ACFs prepared from phenolic fiber precursors have been studied to elucidate the role of pore size, pore surface chemistry and pore volume for the adsorption of SO 2 and its catalytic conversion to H 2 SO 4 . For untreated ACFs, the initial rate of SO 2 adsorption from flue gas was shown to be inversely related to pore size. At longer times, the amount of SO 2 adsorbed from flue gas was dependent on both the pore size and pore volume. Oxidation of the ACFs, using an aqueous oxidant, decreased their adsorption capacity for SO 2 from flue gas due to a decrease in pore volume and repulsion of the SO 2 from acidic surface groups. If these samples were heat-treated to desorb the oxygen containing function groups, the amount of SO 2 adsorption increased. This increase in adsorption capacity was directly correlated to the amount of CO 2 evolved during heat-treatment of the oxidized ACFs. The amount of SO 2 adsorbed for these samples was related to the pore size, pore surface chemistry and pore volume. This analysis is explained in more detail in this paper.

Carbon↗
USGS1996

Effect of surface area and chemisorbed oxygen on the SO2 adsorption capacity of activated char

The objective of this study was to determine whether activated char produced from Illinois coal could be used effectively to remove sulfur dioxide from coal combustion flue gas. Chars were prepared from a high-volatile Illinois bituminous coal under a wide range of pyrolysis and activation conditions. A novel char preparation technique was developed to prepare chars with SO2 adsorption capacities significantly greater than that of a commercial activated carbon. In general, there was no correlation between SO2 adsorption capacity and surface area. Temperature-programmed desorption (TPD) was used to determine the nature and extent of carbon-oxygen (C-O) complexes formed on the char surface. TPD data revealed that SO2 adsorption was inversely proportional to the amount of C-O complex. The formation of a stable C-O complex during char preparation may have served only to occupy carbon sites that were otherwise reactive towards SO2 adsorption. A fleeting C(O) complex formed during SO2 adsorption is postulated to be the reaction intermediate necessary for conversion of SO2 to H2SO4. Copyright ?? 1996 Elsevier Science Ltd.

Fuel↗
USGS1996

Application of thermal analysis techniques in activated carbon production

Thermal analysis techniques have been used at the ISGS as an aid in the development and characterization of carbon adsorbents. Promising adsorbents from fly ash, tires, and Illinois coals have been produced for various applications. Process conditions determined in the preparation of gram quantities of carbons were used as guides in the preparation of larger samples. TG techniques developed to characterize the carbon adsorbents included the measurement of the kinetics of SO2 adsorption, the performance of rapid proximate analyses, and the determination of equilibrium methane adsorption capacities. Thermal regeneration of carbons was assessed by TG to predict the life cycle of carbon adsorbents in different applications. TPD was used to determine the nature of surface functional groups and their effect on a carbon's adsorption properties.

ACS Division of Fuel Chemistry, Preprints↗