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Title: Coal dissolution studies: particle size distribution in coal-derived liquids as a function of degree of coal conversion

Abstract

Exploratory studies were conducted to assess the effect of the degree of coal conversion (i.e., a decrease in the amount of pyridine insolubles) in reacted coal - athracene oil mixtures. Particle size distribution data on the reacted mixtures show that the percentage of particulates < 10 ..mu.. in diameter increases gradually with conversion up to a conversion of about 85%. At higher conversions, the percentage of particulates < 10 ..mu.. in diameter increases dramatically in a near-step, function-like manner. The presence of small particulates are known to be a major cause of the low-filtration rates of coal liquefaction streams. Filtration experiments on the mixtures confirm that a relationship exists between filtration rates and conversion. Thus, the results of this work bear directly on the optimal design of two-stage liquefaction processes and could lead to improved design of processes such as SRC-I.

Authors:
; ;
Publication Date:
Research Org.:
Oak Ridge National Lab., TN (USA)
OSTI Identifier:
6277886
Report Number(s):
ORNL/TM-6681
DOE Contract Number:
W-7405-ENG-26
Resource Type:
Technical Report
Country of Publication:
United States
Language:
English
Subject:
01 COAL, LIGNITE, AND PEAT; COAL; DISSOLUTION; COAL LIQUIDS; FILTRATION; COAL LIQUEFACTION; PARTICLE SIZE; CARBONACEOUS MATERIALS; ENERGY SOURCES; FOSSIL FUELS; FUELS; LIQUEFACTION; SEPARATION PROCESSES; SIZE; THERMOCHEMICAL PROCESSES; 010405* - Coal, Lignite, & Peat- Hydrogenation & Liquefaction; 010402 - Coal, Lignite, & Peat- Purification & Upgrading

Citation Formats

Gilliam, T.M., Brand, J.I., and Rodgers, B.R. Coal dissolution studies: particle size distribution in coal-derived liquids as a function of degree of coal conversion. United States: N. p., 1979. Web. doi:10.2172/6277886.
Gilliam, T.M., Brand, J.I., & Rodgers, B.R. Coal dissolution studies: particle size distribution in coal-derived liquids as a function of degree of coal conversion. United States. doi:10.2172/6277886.
Gilliam, T.M., Brand, J.I., and Rodgers, B.R. Tue . "Coal dissolution studies: particle size distribution in coal-derived liquids as a function of degree of coal conversion". United States. doi:10.2172/6277886. https://www.osti.gov/servlets/purl/6277886.
@article{osti_6277886,
title = {Coal dissolution studies: particle size distribution in coal-derived liquids as a function of degree of coal conversion},
author = {Gilliam, T.M. and Brand, J.I. and Rodgers, B.R.},
abstractNote = {Exploratory studies were conducted to assess the effect of the degree of coal conversion (i.e., a decrease in the amount of pyridine insolubles) in reacted coal - athracene oil mixtures. Particle size distribution data on the reacted mixtures show that the percentage of particulates < 10 ..mu.. in diameter increases gradually with conversion up to a conversion of about 85%. At higher conversions, the percentage of particulates < 10 ..mu.. in diameter increases dramatically in a near-step, function-like manner. The presence of small particulates are known to be a major cause of the low-filtration rates of coal liquefaction streams. Filtration experiments on the mixtures confirm that a relationship exists between filtration rates and conversion. Thus, the results of this work bear directly on the optimal design of two-stage liquefaction processes and could lead to improved design of processes such as SRC-I.},
doi = {10.2172/6277886},
journal = {},
number = ,
volume = ,
place = {United States},
year = {Tue May 01 00:00:00 EDT 1979},
month = {Tue May 01 00:00:00 EDT 1979}
}

Technical Report:

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  • Particle size distribution data on slurries of reacted coal-anthracene oil mixtures indicate that the fraction of particles with diameters <10 ..mu.. increases steadily to 20% at a conversion of 85%; at higher conversions, it increases very rapidly to 60%. Filtration of the slurries suggests a relationship between overall filtration rate and conversion.
  • An experimental apparatus was constructed to perform hydrodesulfurization studies on coal-derived oils. The trickle flow reactor was constructed to achieve isothermal operation along the length of the catalyst bed. The equipment was capable of operating from 77 to 950/sup 0/F, from 0 to 1800 psig, and from 0.05 to 15.0 volume hourly space times. Reducing the most frequent catalyst pore diameter from 33 to 25 A was found to have a detrimental effect on desulfurization as predicted from previous work on petroleum feeds. Pressure was determined to have an effect on desulfurization in the range of 500 to 1000 psigmore » with a decreasing effect beyond 1000 psig. Temperature data were found to best fit a kinetic model developed by assuming desulfurization as a number of simultaneous first order reactions. Changing catalyst particle size and hydrogen rate caused no significant increase in desulfurization. (auth)« less
  • A dispersed water phase can be used to separate mineral matter from coal-derived liquids. A dispersed water phase can either be used to fully distribute the particles to that phase, to collect them at the water/oil interface, or to act as a bridging medium for further agglomeration. Extensive studies were conducted on mineral matter removal from solvent-refined coal. The mineral matter in coal-derived liquids has an asphaltic and preasphaltic coating which dominates its wetting characteristics. This was confirmed by three phase contact angle measurements and the electrical charge characteristics of the mineral matter in solvent-refined coal. Either surfactant wetting agentsmore » or a pH of 9 to 10 in the water phase can be used to wet the mineral matter of particles and to promote their association with the water phase. Particle transfer studies of asphaltic coated particles in model liquids such as xylene indicate that partial detergency of the asphaltic coatings occurs. This mechanism accounts for the fact that the extent of mineral matter separation decreases with mixing time in the water/oil/particle system. A mathematical model and experimental data on electrical coalescence of water droplets in oil suspension is primarily due to the enhanced electric field and corresponding rupture of the oil film between water droplets at drop separations which are greater than those when coalescence is done in the absence of an electric field. A patent resulted from this work on an improved electrostatical coalescence device which used combined AC and DC electric fields in conjunction with hyrophilic electrodes. Six appendices have been entered individually.« less
  • The following activities in regard to the development of micromolecular probe distillation in combination with field-ionization mass spectrometry (FI/MS) for quantitative analysis are reported. The temperature-control module for the direct-introduction probe was received and successfully interfaced to both the probe and the NOVA 3/12. Both temperatures and FI/MS data were minicomputer acquired for probe distillation of a 19 component synthetic blend, a asphaltene-acid fraction, and the base fraction from an anthracene-oil sample. The acquired temperatures and FI/MS data for the 19 component blend were processed on the IBM 370/158 to obtain a quantitative distribution which is in excellent agreement withmore » both the known composition and the one obtained from the FI/MS data acquired using the batch-inlet system for sample introduction. Development of algorithms for correlating the acquired temperatures with the acquired FI/MS data using the NOVA 3/12 and for preparing the correlated data for remote job entry to the IBM 370/158 were initiated. The DS-50S data acquisition system/CEC 21-110B double-focusing mass spectrometer combination was extensively utilized to acquire (1) sensitivities for field ionization of saturates and aromatics, (2) FI/MS data for determining the weight percents of the individual homologs present in the aromatic fractions from the oils and asphaltenes isolated from a COED liquid, (3) FI/MS data for the quantitative analysis of GPC fractions obtained from separation of a hydrotreated shale oil, and (4) FI/MS data for the molecular-ion group-type analysis of saturate fractions from petroleum and shale oil.« less