Characterization of Early Stage Coal Oxidation and Effects of Drying and Supercritical CO2 Pretreatment on Chemical Structure of Coals

Characterization of Early Stage Coal Oxidation and Effects of Drying and Supercritical CO2 Pretreatment on Chemical Structure of Coals
Author: Guang Shi
Publisher:
Total Pages: 364
Release: 2010
Genre:
ISBN:

To obtain representative temperature-programmed desorption (TPD) profiles of young oxidized chars up to 1650°C with minimal reactor wall interferences, the chemistry and physics of four ceramic materials has been critically reviewed. A two-staged experimental apparatus is then uniquely designed to produce chars in an Al 2 O 3 flow reactor with 1 to 21% O 2 followed by in-situ TPD with a SiC tube. Comparison of TPD profiles of oxidized chars with those from pyrolyzed chars and ashes suggests early stage char oxidation is profoundly influenced by oxygen from three sources: organics oxygen, mineral matters and gas phase O 2 . Young chars oxidized at 1000°C with less than 0.3 s residence time shows CO desorption peaks during TPD at three distinct temperatures: 730, 1280, and 1560°C. The peaks at 730°C are mainly caused by incomplete devolatilization. The peaks at 1280°C represent mainly desorption of stable surface oxides and incomplete devolatilization. Increasing the gas phase oxidants notably increases the amount of stable surface oxides. The broad peaks between 1400 and 1650°C are attributed to the reactions of oxidants decomposed from minerals and carbon in the char or SiC tube. Gas-phase oxygen shifts these reactions to lower temperatures. Detailed oxygen balance based on the CO and CO 2 yields and elemental compositions of both pyrolysis and oxidized chars reveals that oxygen uptakes are very high, +0.056 mg O per mg of carbon, in chars derived from bituminous coal, while lignite chars show negative oxygen uptake, -0.020 mg O per mg of carbon, in char. Indeed, lignite char seems to possess little amount of stable surface oxides other than those contributed by the minerals. The extensive emissions of CO from lignite chars during TPD seem to suggest that either O 2 or minerals promotes the oxygen transfer on char surface and subsequent carbon oxidation. The studies on the ignition, devolatilization and combustion kinetics of chars in oxy-coal combustion reflect the fundamental importance of oxidant-activated mechanisms in the early stage of char oxidation. Independently, temperature-programmed desorption (TPD) has revealed sensitive characteristics of chars oxidized by 1-21% O 2 . It demonstrated the existence of stable surface oxides that desorb between 1100-1650°C. Interactions between CO 2 and coal have been gaining interests due to its application in geologic sequestration of CO 2 and methane recovery in coalmines. Recently, we reported the changes in combustion behaviors, including NO emissions and carbon burnout, and physical structures of coals after treatment. The objective of the third part of my work is to investigate the changes in chemical structure of coals after supercritical CO 2 treatment. We found that drying and pretreatment can alter the CO and CO 2 emissions during coal pyrolysis. FTIR analysis shows that oxygen functional groups were found to be significantly changed after drying and/or pretreatment by supercritical CO 2 for both bituminous coal and lignite. These phenomena may significantly affect the conversion of coal gasification and liquefaction.

The Structure and Reaction Processes of Coal

The Structure and Reaction Processes of Coal
Author: K.Lee Smith
Publisher: Springer Science & Business Media
Total Pages: 482
Release: 2013-06-29
Genre: Science
ISBN: 148991322X

Founded on the work of the renowned Advanced Combustion Engineering Research Center, the authors document and integrate current knowledge of the organic and inorganic structure of coal and its reaction processes. With the urgent need for cleaner, more efficient use of this worldwide fuel, their work will set a clear course for future research.

Characterization of Early Stage Coal Oxidation and Effects of Gas Residence Time on NO(x) Reduction in Oxy-coal Combustion

Characterization of Early Stage Coal Oxidation and Effects of Gas Residence Time on NO(x) Reduction in Oxy-coal Combustion
Author: Shaolong Wan
Publisher:
Total Pages: 352
Release: 2009
Genre:
ISBN:

Abstract: This first part of this work reports our first study on the deactivation of young chars in flame conditions. The quantity and strength of surface oxides on young chars are monitored in situ by temperature-programmed desorption (TPD) up to 1700 °C. Search of the oxygen source for the huge amount of CO production at 1700 °C reveals that commonly adopted alumina tubes and support materials decompose to Al 2 O(g) and emit a notable amount of O 2 at temperatures above 1300 °C. Thus, different reactor materials are examined Alumina appears suitable for the oxidation part of the experiments while SiC appears acceptable for TPD. Oxygen from the gas phase, organic portions of the coal and minerals in the coal has been found to have profound influence on the formation and desorption of stable surface oxides in the early stages of coal combustion. In an attempt to isolate the effects of minerals, demineralized coals (DMC) are oxidized in O 2 with a contact time less than 1 second. Young chars derived from both demineralized lignite and bituminous coals show low and flat TPD profiles over a wide temperature range, signifying the minerals' catalytic activities in forming stable surface oxides for both coals. In the third part of this work, the dispersion of CO and CO 2 from temperature-programmed desorption (TPD) of char before they reach the mass spectrometer (MS) is sequentially examined by a set of methods. The Taylor-Aris criterion assures that an axially dispersed, plug-flow model is sufficient to determine the dispersion effects. A novel tracer experiments are performed to determine the residence time distribution (RTD) of the product. Finally, fast Fourier transform (FFT) is also conducted to reconstruct the actual product evolution. This analysis suggests that the dispersion does not severely distort the measured desorption and oxidation rate constants reported previously. A gravity-driven particle feeder has been modified to achieve sustained operation at steady rates. A solenoid with high power output and a secondary reservoir are used. The secondary reservoir can be refilled during the operation without disturbing the feed rate. Test results showed both good long-term and short-term stability. We evaluate the potential benefits of long residence time of gas in a recycle system on NO reduction in oxy-coal combustion. In both single-pass and recycle tests, residence time within a range of 0.36 to 2.0 seconds shows only minimal benefits on NO reduction. The reverse Zeldovich mechanism appears not a governing factor up to 1700 °C, which is close to the peak temperature in practical boilers. The equilibrium concentrations of NO are much lower than those experimentally observed. Thus, NO reduction in oxy-coal combustion is kinetically controlled, not thermodynamically controlled.

Effects of Low-temperature Catalytic Pretreatments on Coal Structure and Reactivity in Liquefaction. Technical Progress Report, July--September 1993

Effects of Low-temperature Catalytic Pretreatments on Coal Structure and Reactivity in Liquefaction. Technical Progress Report, July--September 1993
Author:
Publisher:
Total Pages: 58
Release: 1994
Genre:
ISBN:

In this quarter, progress has been made in the following two aspects: (1) spectroscopic and chemical reaction studies on the effects of drying and mild oxidation of a Wyodak subbituminous coal on its structure and pretreatment/liquefaction at 350°C; and (2) effects of dispersed catalyst and solvent on conversion and structural changes of a North Dakota lignite. Drying and oxidation of Wyodak subbituminous coal at 100-150°C have been shown to have significant effects on its structure and on its catalytic and non-catalytic low-severity liquefaction at 350°C for 30 min under 6.9 MPa H2. Spectroscopic analyses using solid-state 13C NMR, Pyrolysis-GC-MS, and FT-IR revealed that oxidative drying at 100-150°C causes the transformation of phenolics and catechol into other related structures (presumably via condensation) and high-severity air drying at 150°C for 20 h leads to disappearance of catechol-like structure. Increasing air drying time or temperature increases oxidation to form more oxygen functional groups at the expense of aliphatic carbons. Such a clearly negative impact of severe oxidation is considered to arise from significantly increased oxygen functionality which enhances the cross-link formation in the early stage of coal liquefaction. Physical, chemical, and surface physicochemical aspects of drying and oxidation and the role of water are also discussed. A North Dakota lignite (DECS-1) coal was studied for its behaviors in non-catalytic and catalytic liquefaction. Reactions were carried out at temperatures between 250 and 450°C. Regardless the reaction solvents and the catalyst being used, the optimum temperature was found to be 400°C. The donor solvent has a significant effect over the conversion especially at temperatures higher than 350°C.

Effects of Low-temperature Catalytic Pretreatments on Coal Structure and Reactivity in Liquefaction

Effects of Low-temperature Catalytic Pretreatments on Coal Structure and Reactivity in Liquefaction
Author:
Publisher:
Total Pages: 86
Release: 1992
Genre:
ISBN:

During this quarterly period progress has been made in the following three subjects related to the effects of low-temperature thermal and catalytic pretreatments on coal structure and reactivity in liquefaction. First, the liquefaction behavior of three bituminous coals with a carbon content ranging from 77% to 85% was evaluated spectroscopically by [sup 13]C NMR and pyrolysis/gas chromatography/mass spectrometry to delineate the structural changes that occur in the coal during liquefaction. Complementary data includes ultimate and proximate analysis, along with optical microscopy for maceral determinations. Even though these are all bituminous coals they exhibit quite different physical and chemical characteristics. The coals vary in rank, ranging from HvC b to HvA b, in petrographic composition, different maceral percentages, and in chemical nature, percent of carbon and of volatiles. It is these variations that govern the products, their distribution, and conversion percentages. Some of the products formed can be traced to a specific maceral group. Second, pyrolysis-GC-MS and FTIR techniques were used to characterize Wyodak coal before and after drying in vacuum and in air and the residues from its thermal and catalytic liquefactions. The analysis of the air-dried coal shows a decrease in the phenolic type structures in the coal network and increase in the carbonyl structures as the oxidative drying proceeds. An enhanced decrease in the carbonyl structure is observed in the liquefaction residues from the raw coal as compared to that of the vacuum dried coal. The analyses of the liquefaction residues of the air-dried coal show an increase in the ether linkages which may have a negative impact on liquefaction. The extent of the solvent adduction also increases during liquefaction with the extent of oxidation of the coal. Finally, the effects of reaction conditions were investigated on conversion of low-rank coals using a Texas subbituminous coal.