[0001] This invention relates to a fuel composition and to a method of manufacturing a fuel
composition. The invention may have specific application in making carbonaceous fuel
supplies, such as coal, which are located in remote areas available to populous areas.
More particularly, this invention relates to transportable fuel compositions, and
to methods of making such compositions.
[0002] Over 200 billion tons of economically recoverable coal exists in the United States
of America. This represents enough to last the United States for at least three centuries
at the current consumption rate. It has been estimated that coal could provide as
much as one-half of the new energy sources required between now and the year 2000.
Even though coal represents 60% of the domestic fossil energy resources of the United
States, it currently supplies less than 20% of the energy production. A number of
factors have combined to create this disparity. Even with the abundance of coal energy
it has not heretofore been competitive with, nor as easily utilized as, hydrocarbon
containing fuels such as oil, natural gas and the like.
[0003] One important use of United States coal resource is in stationary power conversion
facilities such as plants producing electricity or process heat which do not require
the scarce liquid and gaseous hydrocarbon fuels. Stationary power conversion facilities
can operate using coal leaving the liquid and gaseous hydrocarbon fuels to transportation
and certain residential/commercial uses. Use of coal in stationary power facilities
requires either transportation of the solid fuel to the power facility or utilization
of the solid fuel at the mine site. Utilization at the mine site to produce electricity
is not always efficient due to transmission and/or conversion losses. Production of
electrical energy at other than the mine site requires transportation of the coal.
Coal is currently shipped by rail in unit trains. However the required handling is
cumbersome, wasteful and expensive. The current U.S. rail capacity is inadequate to
move the tonnage required to supplant existing use of more costly and scarce liquid
fuels.
[0004] A further attendant problem with the use of solid fuels generally, and coal specifically,
is that not all solid fuels contain the same mixture of constituents. For example
western U.S. coal, while being low in sulfur, is also low in BTU per unit weight and
has a high water content. Eastern U.S. coal on the other hand haa a higher sulfur
and BTU content per unit weight but lower water. Each requires specific pollution
control equipment and a certain boiler system. Therefore, coal is not as uniform a
fuel as is, for example, #6 fuel oil or the like.
[0005] Additionally, coal from whatever source contains various pollutants which heretofore
have been difficult or impossible to remove. The nature and amount of these depends
upon the geographical area from which the coal is mined. Ash, sulfur, and nitrogen
comprise the most objectionable of these pollutants.
[0006] Recently developed process technology permits the conversion of coal to synthetic
liquid or gaseous fuels at the mine site. While this "synfuel" is more easily transported
than coal, the conversion process is capital intensive and requires a great deal of
water. Despite the high processing costs, the resultant synfuel, like crude oil derived
fuels, is valuable as a transportation fuel.
[0007] In addition to being useful as transportation fuels, hydrocarbon containing fuels,
including synfuels, are likewise valuable as feedstock for the manufacture of chemical
synthetics including all types of plastics, elastomers, resins, polymers and the like.
It would therefore appear advantageous to ulitize coal for stationary energy needs
while utilizing the liquid crude supply and synfuels for transportation as well as
feedstock purposes.
I
[0008] In order to move coal over long distances, methods have been proposed for creating
so-called "coal slurries" which comprise a pulverized, comminuted or ground coal admixed
with water, and which may contain various additives to, for example, increase the
wetability of the coal. This slurry, while capable of being transmitted by pipeline,
requires special pipelines and pumping equipment. Aqueous coal slurries have additional
drawbacks. First the water which is necessary to slurry the coal is in short supply
at the geographic region of the western U.S. coal reserve. Second, water must be removed
from the slurry prior to introduction of the fuel into a furnace or boiler.
[0009] Non-aqueous or hydrocarbon containing liquid can also be used as the transmission
medium to form a slurry of pulverized coal. These slurries still have attendant problems.
Non-aqueous coal slurries also require special pipelines and pumping equipment. Since
coal is still the main fuel constituent in such slurries, furnace and stack modifications
are still required to burn coals from different regions. Non-aqueous fractions, unlike
aqueous solutions, tend to solubilize constituents as well as impurities in the coal.
This renders the slurrying liquid substantially unusable as a feedstock for many chemical
syntheses. Additionally, burning of the slurry mixture results in emission of the
pollutants present in the coal.
[0010] Coke is an expensive product which is produced from metallurgical coal. Methods have
been proposed for producing coke slurry by adding coke which has been formed by conventional
specialized coke production techniques, to certain hydrocarbon materials. Coke is
an agglomerated material which has poor fluidity. It does, therefore, not form a readily
transportable slurry which can be effectively conveyed in conventional pipeline systems.
Coke, being an agglomerated product, tends to settle out. Coke particles, because
of their surface and geometric characteristics, and because of their agglomerated
structure, do not roll over each other and do not pack effectively.
[0011] Thus it would be highly advantageous to have a fuel mixture easily prepared from
coal which would be transportable using existing pipeline systems; which would be
burnable in substantially all existing boiler systems with little or no modification
regardless of the region from which the solid fuel was obtained; which would be high
in BTU content per unit volume; and which would be low in ash, sulfur and nitrogen
pollutants.
[0012] According to one aspect of this invention there is provided a fuel composition comprising
a liquid-solid admixture including a portion of a particulate coal char material dispersed
in an amount of a liquid organic material effective to produce a fluidic, combustible,
transportable composition.
[0013] The invention further extends to a method of producing a fuel composition, which
comprises admixing a coal char with an amount of a liquid organic material effective
to produce a fluidic transportable, combustible composition.
[0014] In one embodiment of the invention the coal char may be produced by the pyrolytic
destructive distillation of a carbonaceous material in the absence of oxygen, and
the liquid organic material may be derived entirely or at least partially from the
pyrolytic destructive distillation.
[0015] In an alternative embodiment of the invention, the liquid organic material may be
a lower chain alcohol of from 1 to about 4 carbon atoms.
[0016] It has been discovered that such an admixture of a particulate coal char and a liquid
organic fraction yields a transportable fuel composition which has high BTU per unit
volume, is low in pollutants, and can be a generally universal fuel for most boilers
with little or no modification.
[0017] The composition of this invention is formed to create a composition which has fluidic
characteristics such that it can be transported by certain existing pipeline facilities.
[0018] The liquid organic fraction which acts as a continuous phase in the admixture does
not contain the impurities of the prior art slurries and thus is capable of being
separated from the liquid-solid mixture prior to the ignition of the char. The separated
liquid is then available for use as a feedstock for synthesis of chemical compounds.
[0019] Economically, the liquid organic fraction is derived during the pyrolysis of the
coal. Advantageously both the char and the liquid organic fraction are beneficiated.
The fuel composition of the instant invention can be produced by subjecting coal to
pyrolytic destructive distillation in the absence of oxygen to produce a particulate
char which is admixed in suitable proportions with a liquid organic fraction to produce
a liquid/solid fluidic mixture.
[0020] In accordance with one aspect of the invention the combustible liquid-solid mixture
is produced by first subjecting coal to pyrolytic destructive thermal distillation
in the absence of oxygen to produce a coal char. The char is then pulverized or otherwise
ground to produce a particulate matter. The particulate matter is then beneficiated
to produce a substantially pollutant-free char material. The lower boiling organic
fraction obtained from the pyrolysis of coal is admixed with the particulate beneficiated
char in proportions so as to form the fluidic, solid-liquid, combustible fuel mixture.
Advantageously, the lower boiling organic fraction used does not contain sulfur or
nitrogen pollutants.
[0021] In accordance with another embodiment, the beneficiated particulate char is admixed
with a lower chain alcohol which is produced by well known synthetic methods utilizing
coal and water or natural gas.
[0022] The utilization of char allows a high packing of the solid particulate matter for
a given fluidity of the mixture. Thus not only does one obtain the aforementioned
advantages but the energy requirement necessary to pump a single BTU of fuel energy
is significantly reduced.
[0023] In a further advantageous embodiment the ground, beneficiated char is sized to yield
a particulate distribution which is bi-modal or tri-modal: The use of a bi-modal or
tri-modal particulate char distribution greatly enhances the packing of the solid.
[0024] A preferred embodiment of the invention is now described by way of example with reference
to the accompanying drawing. The drawing is a flow diagram of one embodiment of the
process of the instant invention.
[0025] The drawing shows a schematic of process steps for producing a coal derived fuel
composition of the instant invention wherein raw coal 12 from a coal mine 10 is conveyed
continuously to a crusher means 14. Within crusher means 14 the raw coal 12 is fragmented
to parti- cles in the range of 1/2" to 1/4" (12 to 6 mm) in diameter to produce a
crushed coal product 16. The crushed coal 16 is conveyed continuously to a pyrolytic
destructive distillation means 18 which preferably contains a preheating chamber to
remove moisture and entrained gases. The pyrolytic destructive distillation means
18 provides for thermal destructive distillation of the coal in the absence of oxygen
to produce a char portion 20 and a liquid organic fraction 34. The char portion 20
is continously conveyed to a grinding means 22. Within the grinding means 22 the char
is pulverized or otherwise comminuted to produce a ground char product 24 which is
inherently spherical in shape. The ground char 24 is conveyed to a beneficiation means
26. Within the beneficiation means 26 the ground char 24 is beneficiated by removal
of undesirable constituents and pollutants such as sulfur and ash. The open pore structure
of the char facilitates this process. The beneficiated char 28 is conveyed to a particulate
sizing means 30. Within the sizing means 30 the particulate is mechanically separated
by particle size to produce a sized distribution of particulate char. The sized char
mixture 32 is continously conveyed to a mixing means 42.
[0026] The liquid organic fraction 34 is conveyed from the pyrolytic destructive distillation
means 18 to a separation means 36 where the higher boiling fraction 38 containing
the bulk of the nitrogen is separated for example by distillation from the remainder
and conveyed to storage for use directly as a chemical reagent and feedstock. Within
the separation means 36, the lower boiling fraction 40 is rendered substantially free
of combined and entrained materials which on combustion would produce sulfur oxides,
nitrogen oxides, and like pollutants. The lower boiling pollutant free fraction 40
is continuously conveyed to the mixing means 42. Within the mixing means 42 the char
mixture 32 and the liquid lower boiling fraction 40 are combined in appropriate proportions
to produce the easily transportable char containing fuel composition 44 of the instant
invention which is passed to storage 46 for distribution by pipeline or tanker vehicle
in a manner similar to crude oil.
[0027] The coal that can be employed in accordance with the instant invention can be generally
termed "combustible carbonaceous material". It is any of the combustible, carbon containing
materials that will undergo pyrolytic destructive distillation to form char. Such
materials comprise carbon containing shales, anthrasite coal, bituminous coal, and
all of the soft coals, lignites, and the like.
[0028] The mining and preparation of coal is fully described in Kirk-Othmer ENCYCLOPEDIA
OF CHEMICAL TECHNOLOGY, second edition, Anthony Standin, editor, Interscience Publishers,
New York, 1969, vol. 5, pp. 606-676. The coal is mined from a coal mine by either
strip or underground methods as appropriate and well known in the art.
[0029] The raw coal material 12 is preferably subjected to preliminary crushing to reduce
the particle size. Particle sizes of from 1/2" (12mm) to about 1/4" (6mm) in lateral
dimension (diameter) are found useful, with particles of about 3/8" (4mm) being preferred.
The need for size reduction and the size of the reduced material will depend upon
the pyrolytic conditions utilized as well as the composition of the coal material.
The crushing and/or grinding is preferably accomplished with impact mills such as
counterrotating cage mills, hammer mills of the like. This is done to impart an impact
type shock to the coal to separate material along natural planes, faulted surfaces,
solution channels and the like. Within the crusher means 14 the coal is sized by,
for example, rough screening and gangue material is removed to assure a more uniform
product for pyrolysis. Advantageously, carbonaceous fines and the like are readily
utilized and can be separated from the macro coal particles and conveyed directly
to the pyrolytic destructive distillation means 18. The macro coal particles are passed
continously through a preheater within pyrolytic destructive distillation means 18
which is operated at 150° to 220°F (65° to 104°C) in order to remove gases and moisture.
This is a well known process and is of value in that the BTU content of the resultant
coal per unit weight is increased. This preheating also removes certain entrained
gases which may have further value as fuel for the pyrolysis step.
[0030] The pyrolytic destructive distillation means 18 can be any pyrolysis apparatus which
is well known in the art. Preferably, the pyrolysis is performed in a continuous process.
As the crushed coal 16 is heated in the absence of oxygen, the entrained materials
are vaporized and collected. Lower boiling organic fractions including hydrocarbons,
cyclics, and aromatics as well as higher boiling organic fractions are emitted from
the coal leaving a char material of essentially carbon which is of a porous structure
and substantially spherical in shape. Included in the emitted constituents are the
nitrogen containing polluting compounds such as pyridine, piperazine and the like.
[0031] The char 20 is continually conveyed to the grinding means 22. The grinding means
22 reduces the char to a suitable fineness to facilitate beneficiation and subsequent
sizing for use in the fuel admixture. Any conventional crushing and grinding means,
wet or dry, may be employed. This would include ball grinders, roll grinders, rod
mills, pebble mills and the like. Advantageously, the particles are sized within the
grinding means 22 and recycled to produce a uniform distribution of particles. The
char particles are of sufficient fineness to pass a 10 mesh screen and the majority
of the particles are in the 100 to 200 mesh size. The mesh sizes refer to the Tyler
Standard Screens. The char 24 is continuously conveyed to the beneficiation means
26.
[0032] The beneficiation means 26 can be any device known in the art utilized to extract
pollutants and other undesirable inorganics such as sulfur and ash from a particulate
char material. This can be done for example, by washing, jigging, extraction, flotation,
chemical reaction, and/or electrobeam techniques. The exact method employed will depend
largely on the coal constituent utilized in forming the char, the sizes of the char
particles and the conditions of pyrolysis.
[0033] The beneficiated char 28 is sized in particulate sizing means 30 which can be any
apparatus known in the art for separating particles of a size in the order of 100
microns. Economically, screens or sieves are utilized, however cyclone separators
of the like can also be employed. In sizing selections made so as to assure combustion,
a second and/or third particle size is chosen to effect so-called "modal" packing.
The spheriod shape of the primary particle provides spacing or voids between adjacent
particles which can be filled by a distribution of second or third finer particle
sizes to provide bi-modal or tri-modal packing. This packing concept allows the compaction
of substantially more fuel in a given volume of fuel mixture while still retaining
good fluidity.
[0034] The resultant char mix 32 is conveyed by means of for example an air conduit to the
mixing means 42 where it is combined in appropriate proportion with the lower boiling
organic fraction 40.
[0035] Simultaneously, with the preparation of the char, the organic fraction 34 entering
the separation means 36 is continuously fractionally distilled or otherwise separated
to provide the lower boiling pollutant free organic fraction 40. The exact amount
of this fraction utilized will depend upon the properties of the combustible char
containing admixture which are desired. Normally, fractions having boiling points
up to about 200°F (94°C) have been found useful in carrying out the instant invention.
Any remaining pollutant fraction could be separated by other means as, for example,
steam stripping.
[0036] The higher boiling fractions 38 of the liquid organic fraction 34 advantageously
contain certain sulfur and nitrogen compounds. This fraction is removed and can be
used directly as a feedstock for chemical synthesis.
[0037] Within the mixing means 42 the particulate char and the lower boiling pollutant-free
organic fraction 40 are admixed in the desired proportions and sent to storage 46.
In the mixing means, an admixture is formed of char and the liquid constituent. The
ratio of char to liquid that can be utilized will depend upon the properties of the
fuel desired. For most applications the char constituent should comprise not less
than about 45% by weight of the composition and preferably from about 45% to about
75% by weight. The mixing means 42 can be any well known mixing apparatus in which
an organic constituent and a coal char can be mixed together in specific proportions
and pumped continuously to a storage tank such as 46.
[0038] Certain well known surfactant stabilizers may be added depending on the viscosity
and non-settling characteristics desired. Within the storage tank 46 it is generally
not required to agitate the fuel admixture of the instant invention unless such storage
is to be for an extended period. From the storage tank the fuel of the instant invention
is preferably continuously conveyed by means of pipelines well known in the art to
distant fixed source heat and electric generators.
[0039] It will be realized that the liquid organic fraction 34 derived from the pyrolytic
destructive distillation of coal can be utilized directly as a feedstock for chemical
synthesis, transportation fuels or the like rather than as the liquid phase of the
instant fuel admixture.
[0040] In accordance with another embodiment of the instant invention coal and water are
utilized to produce first CO and H2and then methanol and other lower alcohols which
are utilized as the liquid phase for the combustible fuel admixture of the instant
invention. Water released from the coal during preheating can be used as part of the
water required in the synthesis, thus further preserving precious resources.
[0041] As used herein the term alcohol is employed to mean alcohols which contain from 1
to about 4 carbon atoms. These include for example, methanol, ethanol, propanol, butanol
and the like. The alcohol may range from substantially pure methanol to various mixtures
of alcohols as are produced by the catalyzed reaction of synthesis gas or natural
gas. Advantageously, the alcohol constituent can be produced on site at the mine in
conjunction with the pyrolytic destructive distillation. The process can be fired
by coal, thereby negating the necessity to transport fuels long distances.
[0042] In accordance with the process for making these alcohols directly from coal and steam,
carbon monoxide and hydrogen are initially formed in accordance with equation I:

A portion of the gas is subjected to the shift reaction with steam to produce hydrogen
for hydrogen enrichment in accordance with equation II:

[0043] The C0
2 is scrubbed from the gaseous product leaving only hydrogen. The hydrogen is admixed
with gaseous products of equation I to produce a "syn gas" having desired ratio of
hydrogen to carbon monoxide from which methanol and similar products are synthesized
catalytically.
[0044] In the methanol synthesis plant the respective constituents such as carbon monoxide
and hydrogen are combined to produce methanol. The synthesis of methanol is described
in page 370-398 of vol. 13 of the above referenced KIRK-OTHMER ENCYCLOPEDIA. The carbon
monoxide and hydrogen are controlled in a ratio and temperature pressure combination
to obtain maximum yields of the methanol fuel product. Other methods for methanol
synthesis at lower temperatures and pressures are also known, as for example, the
ICI low pressure process as described in "Here's how ICI Synthesizes Methanol at Low
Pressure" Oil and Gas Journal, vol. 66, pp. 106-9, February 12, 1968. In accordance
with this aspect of the instant invention, the methanol is used as the liquid phase
to slurry the char 32 in mixing means 42.
[0045] It will be realized that in accordance with the instant invention surfactants, suspenders,
organic constituents and the like may be added depending on the particular application.
As hereinbefore mentioned, advantageously the admixture of the instant invention demonstrates
high fluidity. Thus high BTU per unit volume are obtained with lower viscosities and
higher fluidities.
[0046] It will be realized that the lower boiling organic fraction and/or the synthesized
methanol will not dissolve or otherwise solubilize impurities since the coal has been
charred and the char has been beneficiated. Thus the liquid phase of the composition
can be readily extracted at the fuel mixture destination for use as a chemical synthesis
feedstock. Additionally the fuel composition of the instant invention can be mobilized
or transported by all conventional means used for crude oil transportation, permitting
the efficacious foreign export of coal derived fuels which has not heretofore been
readily and easily accomplished. For example the existing pipelines to docks and tanking
facilities can readily be utilized. Oil tankers can empty their crude oil load in
this country, and be refilled with the char containing composition of the instant
invention which can be exported to other nations, thus improving the balance of payments
of this country.
[0047] The liquid solid admixture, upon reaching its ultimate destination, may be employed
directly as a fuel for heating; for utilities such as power plants; or for process
converters such as in the preparation of synthetic materials. On the other hand it
may be separated into its constituents, char and the lower boiling organic fractions
and/or methanol. The char portion is employed as fuel, while the organic fraction
and/or methanol can be employed as a feedstock or as a transportation fuel such as
a gasoline additive or as an extender.
[0048] While the invention has been explained in relation to its preferred embodiment it
is understood that various modifications thereof will become apparent to those skilled
in the art upon reading the specification and it is intended to cover such modifications
as fall within the scope of the appended claims.
1. A fuel composition comprising a liquid-solid admixture characterized in that it
includes a portion of a particulate coal char material dispersed in an amount of a
liquid organic material effective to produce a fluidic, combustible, transportable
composition.
2. The fuel composition of claim 1, characterized in that the coal char is produced
by the pyrolytic destructive distillation of a carbonaceous material in the absence
of oxygen and in that the liquid organic fraction is derived at least partially from
the pyrolytic destructive distillation.
3. The fuel composition of claim 1 or claim 2, characterized in that the ratio of
particulate material to liquid is not less than about 45% by weight.
4. The fuel composition of anyone of claims 1 to 3, characterized in that the char
is beneficiated, and in that the liquid organic fraction is substantially free of
sulfur and nitrogen pollutants.
5. The fuel composition of claim 1, characterized in that the liquid organic material
comprises a lower chain alcohol of from 1 to about 4 carbon atoms.
6. The fuel composition of claim 5, characterized in that the lower chain alcohol
is an alcohol produced by the catalyzed reaction of synthesis gas or natural gas.
7. A method of producing a fuel composition characterized in that it comprises the
steps of admixing. a coal char with an amount of a liquid organic material effective
to produce a fluidic transportable, combustible composition.
8. The method of claim 7, characterized in that the coal char is produced'by pyrolytic
distillation of carbonaceous material in the absence of oxygen, and in that the liquid
organic material is derived in substantial part from the pyrolytic destructive distillation.
9. The method of claim 7, characterized in that the liquid organic material is a lower
chain alcohol having from 1 to about 4 carbon atoms.
10. A method according to claim 7, characterized in that it comprises the the steps
of:
(a) subjecting a carbonaceous material to pyrolytic destructive thermal distillation
in the absence of oxygen to produce a coal char, and an organic liquid fraction;
(b) reducing the char to a particulate;
(c) beneficiating the particulate to produce a substantially pollutant free beneficiated
particulate char;
(d) separating the organic liquid fraction into an upper boiling pyrolysis fraction
which contains sulfur and nitrogen compounds and a lower boiling pyrolysis fraction
which is substantially free from such sulfur and nitrogen compounds; and
(e) admixing the beneficiated particulate char and an organic liquid selected from
the group consisting of the lower boiling pyrolysis fraction, lower chain alcohols
and mixtures thereof in proportions such that the particulate char is no less than
about 45% by weight.