Steam Reforming of Rapid Pyrolysis Char from Brown and Sub-bituminous
Coals
J Hayashi, H Takahashi, M Iwatsuki, K Morishita Hokkaido Universtiy,
Japan; C Li Monash University, Melbourne; A Tstsumi and T Chiba University
of Tokyo, Japan
Steam gasification of nascent rapid pyrolysis char from low-rank coals
was studied at 1123 – 1223 K employing a novel drop-tube/fixed-bed reactor,
into which a small amount of pulverized coals was injected and it was rapidly
pyrolyzed on a filter as a gas/solid separator. The volatiles were
swept in-situ out of the reaction zone through the filter by a forced flow
of atmospheric nitrogen/stream (47/53 in vol/vol) while the particles remaining
on the filter being exposed to the flow for a desired period. Char
from Yallourn brown coal underwent so rapid steam gasification at 1173
K that its conversion reached 26 and 32% on the basis of carbon in the
nascent char in 5 and 10 s, respectively. It was also found that
the gasification decelerates drastically at the char conversion around
80%, leaving residue much less reactive that the initial char. Char from
Taiheiyo sub-bituminous coals was also steam-gasified rapidly and its conversion
reached about 70 and 80% in 60 s at 1173 and 1223 K, respectively.
The results of the rate analysis suggested that the rapid pyrolysis of
the coals forms so-called ‘rapid carbon’ in nascent char that transforms
into less reactive material in a few hundred seconds at 1173 K
Estimation of Pore Size for Low Rank Coals Sorbing Water Based on
its Molecular Mobility
N Kudo, J Hayashi, and T Chiba Hokkaido University, Japan
and K Norinaga Tohuku University Japan
This paper proposes an application of proton magnetic resonance relaxation
analysis (MRRA) for estimating the size of pores in water-sorbing coals
on the basis o f the transverse relaxation characte4ristics of water condensed
in the po4res as the molecular probe. Raw Yallourn brown coal (water
content; 1.46 g-water/g-mf coal and Beulah Zap lignite (0.53) were employed
as the starting materials and were partially or completely dried at 303K.
The samples with known water contents were subjected to the MRRA using
a Carr-Purcel/Meiboom-Gill(CPMG) pulse sequence. The results of the
analysis revealed that the initial amplitude of the CPMG signal corresponds
quantitatively to the total amount of ‘mobile’ proton. It was also
found that there are three components with different relaxation times (T2)
that are attributed to free water, pore water (freezable bound water and
non-freezable water) and mobile coal hydroxyls/carboxyles. The relaxation
characteristics the components where further analyzed based on a theory
proposed by Brownstein and Tarr, and finally the following conclusions
could be reached. (i) pores filled with pore water are slit-like rather
than cylindrical in shape; (ii) the dimensions of pores are about 3 nm
and 2 nm for the raw Yallourn and Beulah Zap, respectively; (iii) the pore
dimension decreases linearly with the content of pore water.
The Future of Brown Coal Drying Technologies for Power Generation
Comparison of Products from Various Processes
G Favas, A Chaffee and W Jackson Monash University,
Melbourne
The deregulation of the Australian electrical supply industry, the
increase in competition between all electricity generators (hydro-electricity,
natural gas, black and brown coal) across the national grid and the need
to reduce greenhouse emissions have necessitated improvements in brown
coal utilisation for power generation. The competitiveness of brown coal
power generation will in large part depend on the implementation of energy
efficient drying technologies for existing brown coal boilers, which currently
burn coal with a moisture content of 60%.
Three major drying technologies, Steam Drying (SD), Hydrothermal Dewatering
(HTD) and Mechanical Thermal Expression (MTE), were investigated in batch
and bench scale units.
Steam drying is an evaporative drying technology that utilises superheated
steam to remove water from high moisture coals at much lower temperatures
than HTD and MTE; however, the metal ash forming elements remain in the
final product. HTD and MTE are non-evaporative energy efficient drying
technologies that remove water from the coal as a liquid, thus saving energy.
An added advantage of these process is that some of the water soluble inorganics,
in particular Na, are leached out from the coal, thus decreasing the inorganic
content of the product coal. The temperatures used in the HTD process are
higher than in SD and MTE (i.e. up to 320°C). In HTD, soluble organic
material can also leach out into the wastewater that, therefore, may require
substantial treatment. In the MTE process, in addition to heat, a mechanical
force is also applied to the system to facilitate the removal of water
and destroy the internal pore structure of the coal. A disadvantage of
this system is the high mechanical forces (e.g., 12MPa); but processing
temperatures are much lower (180°C to 200°C) than for HTD.
Products from each process have been subjected to a range of analyses,
including proximate and ultimate analysis, the composition of the inorganics,
helium density, surface area (CO2 adsorption), pore volume (mercury porosimetry)
and calorific value. The effectiveness of each of the drying technologies
in relation to the chemical and physical structure of the coal has been
evaluated.
Production of High Quality Coal Product from a Low Quality Coal using
a Modified Hydrothermal Dewatering Technique
G Favas and W Jackson Monash University, Melbourne
A novel method of producing a very low porosity coal material from
highly porous Latrobe Valley raw brown coals has been developed using a
combination of hydrothermal and evaporative drying. Low porosity coal was
made in three different batch autoclave systems at temperatures of 320°C.
Higher temperatures (up to 350°C) gave a small additional decrease
in porosity but these conditions were found undesirable as the water vapour
pressure and the loss of organic material were significantly increased.
Residence times as low as 5min were found to be sufficient to give a densified
coal product. The total organic carbon leached into the wastewater during
the process was significantly lower than under pure hydrothermal dewatering
conditions. The low porosity coal product was found to give a coal water
mixture with a maximum coal concentration for a pumpable slurry of greater
than 60%wt.d.b. in comparison to 45%wt.d.b. using conventional hydrothermal
dewatering. This paper will discuss the method of preparation, the chemical
transformations of the raw coal and the production of very highly concentrated
coal water slurries, with and without the use of chemical additives.
Bound Water in Brown Coal
L Clemow W Jackson, CRC for clean power from lignite, Monash University,
Melbourne;
R Sakurovs CSIRO Division for Energy Technology, Sydney; and D Allardice
Allardice Consulting Victoria
A well known characteristic of brown coals is their strong affinity
to water, which is demonstrated by their high moisture content as mined,
high monolayer water capacity and high non-freezing water content.
It is therefore important to establish how these quantities relate to the
coal structure. For several coals, monolayer water capacity was measured
by equilibration at 15% relative humidity at 30°C and the non-freezing
water content by 1H nuclear magnetic resonance spectroscopy (nmr) and differential
scanning calorimetry (DSC). These properties have been correlated
with structural characteristics of the same coals (elemental analysis,
carboxyl and phenol content determined by aqueous titration). It
was found that both of these properties and their ratio were primarily
dependent on the carboxylic acid concentration of the coal. The phenol
groups were less significant in this regard. Therefore to improve
the characteristics of brown coals, attention should be concentrated on
processes which enhance decarboxylation.
The Chemistry of Coal-Water Interactions: and Theoretical and Experimental
Investigations
A Chaffee, T Vu CRC for Clean Power from Lignite, Melbourne; and
I Yarovshy RMIT University, Melbourne
Compared to other coals, Victorian lignite is remarkably clean, typically
possessing low concentrations of inorganics and mineral matter. Unfortunately,
the high moisture content (60 – 70% wet basis) means that a pre-drying
process is required to remove most of the water in the coal prior to combustion.
Drying processes that remove the water evaporatively require substantial
energy, reducing the efficiency of power generation from this fuel.
To assist the optimisation of drying processes it is important that
details of the coal structure and coal-water interactions be understood
in as full detail as possible.
Since lignite is a very complex heterogeneous material, the complexity
of the problem has been reduced through the use of ‘megafossil’ samples
taken from the coal. Megafossils are the discrete macroscopic remains of
wood, leaves, resins, etc that can be visually identified and hand-picked
from the coal seam. Such megafossils are chemically less heterogeneous
than lignite as a whole.
The physical structure of these fossil woods has been probed by techniques
such as helium pycnometry, mercury porosimetry and gas adsorption. Likewise,
the organic structure has been probed by elemental analysis, DRIFT-IR,
SS-NMR and TGA. On the basis of these results, structural models of fossil
wood are constructed and coal-water interactions are simulated. The
simulated results are compared with measured isotherms of water adsorption.
Upgrading of Coal Derived Oil as Transportation Fuels
S Azuma and S Wasaka New Energy and Industrial Technology Development
Organization, Japan
The New Energy and Industrial Technology Development Organization (NEDO)
has been developing coal liquefaction technology as part of the “New Sunshine
Programs” planned by the Agency of Industrial Science and Technology, a
division of the Ministry of International Trade and Industry in Japan.
The developed “NEDOL” process showed advantages such as applicability to
a wide range of coal ranks, a high oil yield and reliability of plant facilities.
Parallel to the development of the coal liquefaction process, development
of product upgrading technology has been proceeding to make use of the
liquefied products as transportation fuels. Based on the laboratory
study of the upgrading process, a 40 bbl/d process development unit (PDU)
was designed and constructed. The PDU is composed of a two-stage
hydrotreating unit, an atmospheric distillation unit and a reforming unit
to produce gasoline and diesel fractions. First-stage hydrotreating
of coal derived crude oil was carried out successfully in the PDU.
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