CA1172851A - Fuel composition and method of manufacture - Google Patents

Abstract

ABSTRACT

FUEL COMPOSITION AND METHOD OF MANUFACTURE

Coal char is produced by the pyrolytic destructive thermal distillation of coal in the absence of oxygen in distillation means. The char so produced is ground in grinding means to provide a ground char. The ground char is beneficiated in beneficiation means, and is then sized in sizing means to produce a char mix. The char mix is then admixed in suitable proportions with a liquid organic fraction to form a combustible, liquid-solid mixture which is a stable, transportable, fuel composition. Preferably, the liquid organic fraction is obtained from the low boiling fractions derived from the pyrolysis of coal.

Description

MEYC:002 FUEL COMPOSITION AND METHOD OF MANUFACTURE

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.

Over 200 billion tons of economically recoverable coal exists in the United States o~ America. This represents enough to lask the United States Eor at least three centu-ries at the current consumption rate. It has been esti-mated 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 sup-plies less than 20% of the energy production. A number offactors have combined to create this disparity. Even with ~he abundance of coal energy it has not heretofore been competitive with, nor as'easily utilized asr hydrocarbon containing fuels such as oil, natural gas and the like.
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~2--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. Sta-- 5 tionary power conversion facilities can operate using coal leaving the liquid and gaseous hydrocarbon fuels to trans-portation and certain residential/commercial uses. Use of coal in stationary power facilities requires either trans-portation of the solid fuel to the power facility or utili-zation of the solid fuel at the mine site. Utilization atthe mine site to produce electricity is not always effi-cient due to transmission and/or conversion losses. Pro-duction 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.
A further attendant problem with the use oE solid fuels yenerally, and coal specifically, is that not all solid ~uels contain the same mixture of constituents. For example weste~n U.S. coal, while being low in sulfur, is also low in BTU per unit weight and has a high water con-tent. 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.

Additionally, coal from whatever source contains various pollutants which heretofore have been difEicult or impossible to remove. The nature and amount of these depends upon the geographical area from which the coal ~ 1728~.1.

is mined. Ash, sulfur, and nitrogen comprise the most objectionable of these pollutants.

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.

In addition to being useful as transportation ~uels, 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 sta-tionary energy neéds while utilizing the liquid crude supply and synfuels for transportation as well as feed-stock purposes.

In order to move coal over long distances, methodshave been proposed for creating so-called "coal slurries"
which comprise a pulverized, comminuted or ground coal admixed with water, and which may contain var~ous addi-tives to, for example, increase the wetability of the coal. This slurry, while capable of being transmitted by pipeline, requires special pipelines and pumping e~uipment. ~queous coal slurries have additional draw-backs. First the water which is necessary to slurry thecoal 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 f urnace or boiler.

8,~ 1 Non-aqueous or hydrocarbon containing liquid can also be used as the transmission medium to form a slurry o~
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 solutionsl 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.

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 effec-tively conveyed in conventional pipeline systems. Coke, being an agglomerated product, tends to settle out. Coke particles, because of their surface and yeometric char-acteristics, and because of their agglomerated structure,do not roll over each other and do not pack effectively.

Thus it would be highly advantageous to have a fuel mixture easily prepared from coal which would be trans-portable using existing pipeline systems; which would beburnable in substantially all existing boiler systems .~ ~

7 2 ~ ~3 1 with little or no modificatioll regardless of the region from which the solid fuel was obtained; which would be high in BTU content per unit volumei and which would be low in ash, sulfur and nitrogen pollutants.

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 derived from coal dispersed in an amount of a liquid organic material effective to produce a fluidic, combustible/ transportable composition.

The invention further extends to a method of producing a fuel composition, which comprises admixing a particulate coal char derived from coal with an amount of a liquid organic material effective to produce a fluidic, transportable, combustible composition.

In one embodiment of the invention the coal char may be produced by the pyrolytic distillation of coal in the absence of oxygen, and the liquid organic material may be derived entirely or at least partially from the pyrolytic clestructive distillation~

In an alternative embodiment of the invention, the liquid organic material may be a ~ower chain alcohol o~ from 1 to about 4 carbon atoms.

The invention also encompasses the novel method of pro-ducing a combustible fuel composition which comprises the steps of subjec~ting coal to pyrolytic destructive thermal distillation in the absence of oxygen to produce a particulate coal char, and an organic liquid fractioni reducing the char to a sized particulate to effect bimodal or trimodal packing; beneficiating ~ .

:1 L ~ 2 ~ t ~5a-the particulate to produce a substantially pollutant free beneficiated particulate char; 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 admixing the beneficiated particulate cbar and an organic liquid selected from *he group consisting of the lower boiling pyrolysis frac~ion, lower chain alcohols and mixtures thereof in proportions such that the particulate char is no less than about 45% by weight.

It has been discovered that such an admixture of a particulate coal char and a liquid organic fraction ~i~lds a transportable fuel composition which has high BTU per unit volume, is low in pollutants, and can be a generally - lS universal fuel for most boilers with little or no modifi-cation.
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The composition o this invention is formed to create a composition which has fluidic characteristics such that it can be transported by certain existing pipeline facilities.
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 sepa-rated from the liquid-solid mixture prior to the ignition o the char. The separated liquid is then available for use as a feedstock for synthesis of chemical compounds.

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.

In accordance with one aspect of the invention the combustible liquid-solid mixture is produced by firs~ sub-jecting 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 partic-ulate matter. The particulate matter is then beneficiated to produce a substantially pollutant-free char material.
The lower boiling organic fraction obtained from the pyroly-sis of coal is admixed with the particulate beneficiatedchar 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.

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In accordance with another embodiment, the benefi-ciated particulate char is admixed with a lower chain alcohol which is produced by well known synthetic methods utilizing coal and water or natural gas.

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 IQ single BTU of fuel energy is significantly reduced, In a further advantageous embodiment the ground, beneficiated char is sized to yield a particulate distri-bution 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.

A preferred embodiment of the invention is now described by way of example with re~erence to the accom-panying drawing. The drawing is a flow diagram of oneembodiment of the process of the instant invention.

The drawing shows a schematic of process step~ for producing a coal derived f~el 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" 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 3 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 ox~gen to produce a char portion 20 and a liquid organic ~ :1 7 ~

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 ~round char product 24 which is inherently spherical in - 5 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 consti-tuents 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.
The liquid organic fraction 34 is conveyed from the pyrolytic destructive distillation means 18 to a separa-tion means 36 where the higher boiling fraction 38 contain-ing 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 oxidesl and like pollutants. The lower boiling pollutant Eree fraction 40 is continuously conveyed to the mixing means 42. Within the mixing rneans 42 the char mixture 32 and the li~uid 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.

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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.

The rnining 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.

The raw coal material 12 is preferably subjected to preliminary crushing to reduce the particle size.
Particle sizes of from 1/2" to about 1/4" in lateral dimension (diameter) are found useful, with particles of about 3/8" being preferred. The need for size reduction and the siz~ of the reduced material will depend upon the pyrolykic conditions utilized as well as the composition of the coal material. The crushiny and/or grinding is preferably accomplished with impact mills such as counter-rotating cage mills, hammer mills of the like. This is done to impart an impact type shock to the coal to sepa-rate 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 -- i17~

coal particles are passed continously through a preheater within pyrolytic destructive distillation means 18 which is operated at 150 to 220F in order to remove gases and moisture. This is a well known process and is of value in - 5 that the BTU content of the resultant coal per unit weight is increased. This preheating also removes certain en-trained gases which may have further ~alue as fuel for the pyrolysis step.

The pyrolytic destructive distillation means 18 can ~e 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 pyri~ine, pipera-zine and the like.

The char 20 is continually conveyed to the grindiny means 22. The grinding means 22 reduces the char to a suitable fineness to facilitate beneficiation and subse-quent sizing for use in the fuel admixture. Any conven-tional crushing and grinding means, wet or dry, may be employed. This would include ball grinders, roll grind-ers, 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 ;~ ~ 7Z~

Tyler Standard Screens. The char 24 is continuously con-veyed to the beneficiation means 26.

The beneficiation means 26 can be any device known in the art utilized to extract pollutants and other unde-sirable inorganics such as sulfur and ash from a particu-late 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.

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 parti-cles which can be filled by a distribution of second or third finer particle sizes to provide bi-modal or tri~modal packing. Thi~ packing concept allows the compaction oE
substantially more fuel in a given volume of fuel mixture while still retaining good fluidity.

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.

Simultaneously, with the preparation of the char, the organic fraction 34 entering the separation means 36 is continuously fractionally distilled or otherwise " ~ 1 7~8.~ :~

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 combusti-ble char containing admixture which are desired. Nor-mally, fractions having boiling points up to about 200Fhave been found useful in carrying out the instant inven~
tion~ Any remaining pollutant fraction could be separated by other means as, for example, steam stripping.

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.

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 ~5% hy weight of the composition and preferably from about 45% to about 75~ hy 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.

Certain well known surfactant stabilizers may be added depending on the viscosity and non-settling charac-teristics 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

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means of pipelines well known in the art to distant fixed source heat and electric generators.

It will be realized that the liquid organic fraction ; - 534 derived from the pyrolytic destructive distillation of coal can be utilized directly as a feedsto~k for chemical synthesis, transportation fuels or the like rather than as the liquid phase of the instant fuel admixture.

10In accordance with another embodiment of the instant invention coal and water are utilized to produce first CO
and H2 and then methanol and other lower alcohols which are utilized as the liquid phase for the combustible fuel admixture of the instant invention. Water released ~rom the coal during preheating can be used as part of the water required in the synthesis, thus further preserving precious resources.

As used herein the term alcohol is employed to mean ~0 alcohols which contain from 1 to about ~ carbon atoms.
These include for example, methanol, ethanol, propanol, butanol and the like. The alcohol may range Erom substan-tially 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.
In accordance with the process for making these alco-hols directly from coal and steam, carbon monoxide and hydrogen are initially formed in accordance with equation I:
I. HOH (steam) ~ C(coal~ CO+H2 ~ 1 7 ~

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

- 5 II. CO + HOH (steam) CO2+H2.

The CO2 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.

In the methanol synthesis plant the respective consti-tuents such as carbon monoxide and hydrogen are combined to produce methanol. The synthesis of methanol is described in page 370-39~ of vol. 13 of the above referenced KIRK-OTHMER ENCYCLOPEDIA. The car~on mono~ide 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 low~r temperatures and pressures are also known, as for e~ample, the ICI low pressure process as described in "Here's how I~I Synthesizes Methanol at Low Pressure" Oil and Gas Journal, vol. 66, pp. 10~-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.

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 applica-tion. As hereinbefore mentioned, advantageously the admix-ture of the instant invention demonstrates high fluidity.
Thus high ~TU per unit volume are obtained with lower vis-cosities and higher fluidities.

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It will be realized that the lower boiling organic fraction and/or the synt~esized 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 syn-thesis ~eedstock. 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 tank-ers 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.

The liquid solid admixture, upon reaching its ulti-mate destination, may be employed directly as a fuel forheating; for utilities such as power plants; or or 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 gaso-line additive or as an extender.

While the invention has been explained in relation to its preferred embodiment it is understood that various modi-fications thereof will become apparent to those skilled in the art upon reading the specification and it is in~ended to cover such modifications as fall within the scope of the appended claims.

Claims (15)

The embodiments of the invention in which an exclusive property or privilege is claimed are defined as follows:

1. A fuel composition comprising a liquid-solid admixture including a portion of a particulate coal char material derived from coal dispersed in an amount of a liquid organic material effective to produce a fluidic, combustible, transportable composition.

2. The fuel composition of Claim 1, wherein the coal char is produced by the pyrolytic destructive distillation of coal in the absence of oxygen.

3. The fuel composition of Claim 2, wherein the liquid organic fraction is at least partially derived from the pyrolytic destructive distillation.

4. The fuel composition of Claims 1, 2 or 3, wherein the ratio of particulate material to liquid is not less than about 45% by weight.

5. The fuel composition of Claim 1, 2 or 3, wherein the char is beneficiated and the liquid organic fraction is substantially free of sulfur and nitrogen pollutants.

6. The fuel composition of Claim 1, wherein the liquid organic material comprises a lower chain alcohol of from 1 to about 4 carbon atoms.

7. The fuel composition of Claim 6 wherein the lower chain alcohol is an alcohol produced by the catalyzed reaction of synthesis gas or natural gas.

8. A method of producing a fuel composition comprising the steps of admixing a particulate coal char derived from coal with an amount of a liquid organic material effective to produce a fluidic, transportable, combustible composition.

9. The method of Claim 8, wherein the coal char is produced by pyrolytic distillation of coal in the absence of oxygen, and wherein the liquid organic material is derived in substantial part from the pyrolytic destructive distillation.

10. The method of Claim 8, wherein the liquid organic material is a lower chain alcohol having from 1 to about 4 carbon atoms.

11. A process for producing a fuel composition comprising the steps of slurrying an effective amount of a particulate coal char with a liquid organic material to produce a fluidic, transportable, combustible composition wherein the particulate coal char is derived from the pyrolytic destructive distillation of coal in the absence of oxygen and the liquid organic fraction is at least partially derived from said pyrolytic distillation.

12. A method of producing a combustible fuel composition comprising the steps of:
(a) subjecting coal to pyrolytic destructive thermal distillation in the absence of oxygen to produce a particulate coal char, and an organic liquid fraction;
(b) reducing the char to a sized particulate to effect bimodal or trimodal packing;
(c) beneficiating the particulate to produce a sub-stantially 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.

13. A fuel composition comprising a liquid solid admixture including a portion of a particulate coal char material derived from coal dispersed in an amount of a liquid organic material effective to produce a fluidic, combustible, transportable composition wherein said particulate coal char is produced by the pyrolytic destructive distillation of coal in the absence of oxygen and wherein said liquid organic material is at least partially derived from said pyrolytic destructive distillation.

14. The fuel composition of Claim 13 wherein said parti-culate material is of the order of 100 microns in size, being substantially spherical in shape.

15. The composition of Claim 13 or Claim 14 wherein the ratio of particulate material to the liquid is not less than about 45% by weight.