U.S. patent application number 15/183929 was filed with the patent office on 2016-10-06 for pelletized fuel products, methods, and apparatuses.
The applicant listed for this patent is Novus Technology, Incorporated. Invention is credited to James Grady Coble, III, William J. Lawrence.
Application Number | 20160289583 15/183929 |
Document ID | / |
Family ID | 49714180 |
Filed Date | 2016-10-06 |
United States Patent
Application |
20160289583 |
Kind Code |
A1 |
Lawrence; William J. ; et
al. |
October 6, 2016 |
PELLETIZED FUEL PRODUCTS, METHODS, AND APPARATUSES
Abstract
Pelletized fuel products, methods, and apparatuses are provided.
The method includes pelletizing at least partially carbonized
biomass in an inert atmosphere. The apparatus includes a feeder of
at least partially carbonized biomass, a pelletizer configured to
receive and pelletize the at least partially carbonized biomass,
and an inert gas source configured to provide inert gas to the
pelletizer.
Inventors: |
Lawrence; William J.;
(Meridian, MS) ; Coble, III; James Grady;
(Fernandina Beach, FL) |
|
Applicant: |
Name |
City |
State |
Country |
Type |
Novus Technology, Incorporated |
Northport |
AL |
US |
|
|
Family ID: |
49714180 |
Appl. No.: |
15/183929 |
Filed: |
June 16, 2016 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
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13915401 |
Jun 11, 2013 |
9394498 |
|
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15183929 |
|
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61658396 |
Jun 11, 2012 |
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Current U.S.
Class: |
1/1 |
Current CPC
Class: |
C10L 9/086 20130101;
Y02E 50/30 20130101; Y02E 50/15 20130101; C10L 5/363 20130101; Y02E
50/10 20130101; C10L 9/083 20130101; C10L 5/447 20130101 |
International
Class: |
C10L 5/44 20060101
C10L005/44; C10L 9/08 20060101 C10L009/08; C10L 5/36 20060101
C10L005/36 |
Claims
1. An apparatus for producing a pelletized fuel product,
comprising: a feeder of at least partially carbonized biomass; a
pelletizer configured to receive and pelletize the at least
partially carbonized biomass; and an inert gas source configured to
provide inert gas to the pelletizer.
2. The apparatus of claim 1, wherein the at least partially
carbonized biomass comprises torrefied wood or hydrothermally
carbonized wood.
3. The apparatus of claim 1, wherein the inert gas comprises
nitrogen, carbon dioxide, or steam.
4. The apparatus of claim 1, further comprising: a water source
configured to moisten the at least partially carbonized biomass to
a moisture content of from about 2 percent to about 40 percent by
weight of the at least partially carbonized biomass prior to
pelletization.
5. The apparatus of claim 4, wherein the at least partially
carbonized biomass is pelletized in an inert atmosphere, and
wherein a portion of the inert atmosphere comprises steam and at
least a portion of the steam is produced during pelletization.
6. An apparatus for producing a pelletized carbonized fuel product,
comprising: a feeder of raw biomass; a reactor configured to
receive and at least partially carbonize the raw biomass; a
pelletizer configured to receive and pelletize the at least
partially carbonized biomass; and an inert gas source configured to
provide inert gas to the pelletizer.
7. The apparatus of claim 6, wherein the raw biomass comprises
wood.
8. The apparatus of claim 6, wherein the reactor is a torrefaction
reactor or a hydrothermal carbonization reactor.
9. The apparatus of claim 6, wherein the inert gas comprises
nitrogen, carbon dioxide, or steam.
10. The apparatus of claim 6, further comprising: a water source
configured to moisten the at least partially carbonized biomass to
a moisture content of from about 2 percent to about 40 percent by
weight of the at least partially carbonized biomass prior to
pelletization.
11. The apparatus of claim 10, wherein the at least partially
carbonized biomass is pelletized in an inert atmosphere, and
wherein a portion of the inert atmosphere comprises steam and at
least a portion of the steam is produced during pelletization.
Description
CROSS-REFERENCE TO RELATED APPLICATIONS
[0001] This application is a divisional of U.S. patent application
Ser. No. 13/915,401, filed Jun. 11, 2013, which claims the benefit
of U.S. Provisional Application No. 61/658,396, filed Jun. 11,
2012, each of which is incorporated herein by reference in its
entirety.
TECHNICAL FIELD
[0002] The present invention relates generally to the field of fuel
products, and more particularly to pelletized biomass-based fuel
products and methods and apparatuses for producing the same.
BACKGROUND
[0003] Biomass-based fuel products are desirable because they
provide a renewable energy source and an eco-friendly alternative
to coal and other fossil fuels. Processes such as torrefaction are
known to produce at least partially carbonized biomass-based fuel
products offering increased energy value and improved combustion
properties over the raw biomass.
[0004] Densification and pelletization processes are known to
transform the at least partially carbonized biomass into more
useful forms for storage, shipping, and handling. Densification and
pelletization processes, however, experience handling problems. It
would therefore be desirable to provide improved methods and
apparatuses for producing pelletized, torrefied biomass-based fuel
products.
SUMMARY
[0005] In one aspect, a method for producing a pelletized fuel
product is provided. The method includes pelletizing at least
partially carbonized biomass in an inert atmosphere. In one
embodiment, the at least partially carbonized biomass includes
torrefied wood or hydrothermally carbonized wood. In one
embodiment, the inert atmosphere includes an inert gas selected
from the group consisting of nitrogen, carbon dioxide, and
steam.
[0006] In another aspect, an apparatus for producing a pelletized
fuel product is provided. The apparatus includes a feeder of at
least partially carbonized biomass, a pelletizer configured to
receive and pelletize the at least partially carbonized biomass,
and an inert gas source configured to provide inert gas to the
pelletizer. In one embodiment, the apparatus further includes a
water source configured to moisten the at least partially
carbonized biomass to a moisture content of between about 2 percent
and about 40 percent by weight of the at least partially carbonized
biomass prior to pelletization.
[0007] In yet another aspect, a method for producing a pelletized
carbonized fuel product is provided. The method includes at least
partially carbonizing a biomass feed to produce at least partially
carbonized biomass, and thereafter pelletizing the at least
partially carbonized biomass in an inert atmosphere to produce a
pelletized carbonized fuel product. In one embodiment, the step of
at least partially carbonizing a biomass feed comprises torrefying
the biomass feed or hydrothermally carbonizing the biomass
feed.
[0008] In another aspect, an apparatus for producing a pelletized
carbonized fuel product is provided. The apparatus includes a
feeder of raw biomass, a reactor configured to receive and at least
partially carbonize the raw biomass, a pelletizer configured to
receive and pelletize the at least partially carbonized biomass,
and an inert gas source configured to provide inert gas to the
pelletizer. In one embodiment, the reactor is a torrefaction
reactor or a hydrothermal carbonization reactor.
BRIEF DESCRIPTION OF THE DRAWINGS
[0009] FIG. 1 is a schematic diagram illustrating one embodiment of
an apparatus for producing a pelletized fuel product.
[0010] FIG. 2 is a schematic diagram illustrating one embodiment of
an apparatus for producing a pelletized carbonized fuel
product.
DETAILED DESCRIPTION
[0011] The present application will now be described more fully
hereinafter with reference to the accompanying drawings, in which
several embodiments of the application are shown. Like numbers
refer to like elements throughout the drawings.
[0012] In the following description, numerous specific details are
given to provide a thorough understanding of embodiments. The
embodiments can be practiced without one or more specific details,
or with other methods, components, materials, and the like. In
other instances, well known structures, materials, or operations
are not shown or described in detail to avoid obscuring aspects of
the embodiments.
[0013] Reference throughout the specification to "one embodiment,"
"an embodiment," or "embodiments" means that a particular feature,
structure, or characteristic described in connection with the
embodiment is included in at least one embodiment. Thus, the
appearances of the phases "in one embodiment" or "in an embodiment"
in various places throughout the specification are not necessarily
referring to the same embodiment. Furthermore, the particular
features, structures, or characteristics may be combined in any
suitable manner in one or more embodiments.
[0014] Carbonization processes are known that convert organic
substances into carbon or carbon-containing residue. As used
herein, the terms "carbonize" and "carbonized" refer to these
processes and their products. For example, processes such as
torrefaction and hydrothermal carbonization convert raw biomass to
at least partially carbonized products having increased mass energy
density.
[0015] As used herein, the term "biomass" refers to renewable
organic materials such as biological materials comprising
lignocellulose including hardwood and softwood from trees, wood
chips, slash or hog fuel from softwood tree processing, forest
residue, straw, chaff, grain, grasses, corn, corn husk, weeds,
aquatic plants, and hay, and lignocellulose containing material of
biological origin, such as some municipal waste or household waste.
Woody biomass is mainly composed of hemicellulose, cellulose,
lignin, and small amounts of ash. The structure is a complex
arrangement of microfibrils, or bundles of cellulose covered with
hemicellulose. Lignin fills the voids between the microfibrils and
is sometimes embedded within the amorphous portions of the
microfibrils. Each component of the woody biomass displays a unique
thermal stability, with hemicellulose decomposing between 225 and
325.degree. C., cellulose decomposing between 305 and 375.degree.
C., and lignin decomposing between 250 and 500.degree. C.
[0016] Torrefaction refers to the heating of biomass to produce a
product having increased mass energy density that can be used as a
fuel. Generally, torrefaction may be performed on biomass at
temperatures between about 200.degree. C. and about 300.degree. C.
After a residence time, the biomass partially decomposes, giving
off volatiles such as syngas. Accordingly, torrefaction is commonly
performed in the absence of oxygen to prevent ignition of the
biomass during torrefaction. The process produces a final product
known as "torrefied biomass" or "torrefied wood" when produced from
woody biomass. Torrefaction offers a promising biomass upgrading
option, as the physical properties of the torrefied solids are
similar to those of coal.
[0017] During torrefaction, the hemicellulose is the removed to a
greater extent than the other components of the biomass. The
hemicellulose displays an initial rapid decomposition rate followed
by a more lengthy secondary charring with increased holding time.
Portions of lignin have been observed to decompose or transform
during torrefaction, while cellulose maintains its crystalline
structure. The removal of hemicellulose results in a physiochemical
transformation of the solid woody biomass material. Elemental
analysis of torrefied wood has shown that the fractional makeup of
carbon is increased by up to 15-20% while oxygen is reduced by up
to 50%. As a result, the atomic ratios of H/C and O/C are reduced
from approximately 1.64 to 1.11 and from 0.82 to 0.49,
respectively.
[0018] The resulting torrefied wood solids offer great promise in
renewable combustion opportunities and syngas production due to
their increased energy value, friability, and hydrophobic nature.
Densification and pelletization of the torrefied solids are
desirable to improve ease of handling and storage of the fuel
product, i.e., by transforming the product into uniform,
high-density pellets; however, these processes experience many
problems.
[0019] Conventional wisdom suggests that because much of the
original hemicellulose is liberated during the torrefaction
process, there remains a higher proportion of lignin on a per unit
basis of total solid mass than before the reaction occurred.
Therefore, adequate amounts of lignin remain to sufficiently bind
the solids during pelletization or densification. However, at the
reaction temperatures necessary to complete torrefaction, the glass
transition temperature of the lignin is altered. In other words,
the temperature required to initiate re-bonding of the lignin is
increased. The absence of water, considered to be a positive
attribute in the torrefaction process, is also believed to play a
role in altering the glass transition temperature of the remaining
lignin.
[0020] In an effort to reach higher temperatures to achieve
reactions with the residual lignin to bind the solids, conventional
pellet presses would have to be operated at temperatures beyond
current technological limits. While several technologies offer
promising results for making high temperature pellets, these
technologies are tedious, expensive, and presently unavailable for
commercialization.
[0021] High-temperature operation introduces another serious
drawback to pelletization, namely syngas production. As higher
temperatures are reached in an effort to initiate lignin
reactivity, the previously reacted materials liberate significant
amounts of syngas composed of a mixture of carbon monoxide,
hydrogen, carbon dioxide, methane, nitrogen, and small amounts of
hydrocarbons. This thermo-chemical conversion is further encouraged
by the altered friability of the remaining solids, which is now
much greater, and by a solids particle size that is quickly reduced
to micron size as the solid is introduced to the feed rollers,
pellet rams or pellet dies. The resulting product is an ultra-fine
particle with a greater surface area than that of the original
torrefied solids and consequently is highly pyrophoric. While
desirable for the end use of the product, the pyrophoric nature of
the product creates a hazard to personnel and equipment during the
densification and pelletization process and remains problematic for
the successful formation of torrefied pellets.
[0022] To avoid the drawbacks associated with high-temperature
pelletization, Applicants have developed a novel process that
allows for the densification and pelletization of torrefied
biomass, hydrothermal carbonized biomass, and other chars without
the use of temperatures exceeding the technological limits of
conventional pellet presses. Applicants discovered that
low-temperature pelletization utilizing a binder as a substitute
for the lignin also involved many challenges and drawbacks.
Specifically, Applicants discovered that once a pelletization unit
reaches temperatures adequate for pellet formation, explosions and
hollow core pellets occur, despite operating temperatures well
below the flashpoint of torrefied wood. Without intending to be
bound by a particular theory, Applicants believe that fine
particles of torrefied wood in the pelletizer emit hydrogen gas and
carbon monoxide even at very low temperatures, resulting in highly
pyrophoric properties. While considerable teaching exists in the
literature regarding the liberation of torrefaction gases, this
discovery was surprising.
[0023] Applicants discovered that lower pelletization temperatures
combined with an inert environment yields less spontaneous and
unintentional combustion reactions during pelletization and results
in an improvement in machine uptime and yield. Applicants believe
this limits the amount of syngas produced during the pelletization
process and offers the user an opportunity to operate an array of
pelletization equipment in the absence of increased syngas
hazards.
[0024] To maintain margins of safety with the finished pelletized
product, the formation of robust pellets is necessary to reduce the
pyrophoric nature of the product. Applicants found that properly
formed pellets or briquettes will significantly reduce the fire
hazard by removing the small particle sizes prone to spontaneous
combustion. The robustness of the pellet is necessary to maintain
this density during storage and transportation. If particle size is
allowed degrade to a small fraction in an oxygen rich environment,
the risk of unintentional combustion will likely increase due to
continued liberation of syngas.
[0025] In one aspect, a method is provided for producing a
pelletized fuel product, which includes pelletizing at least
partially carbonized biomass in an inert atmosphere. In certain
embodiments, the at least partially carbonized biomass comprises
torrefied wood or hydrothermally carbonized wood. The at least
partially carbonized biomass may also include coal and/or char. In
one embodiment, the method includes applying a binder to the at
least partially carbonized biomass prior to the step of
pelletization. The binder may be a starch-based binder or a
waterproof binder. For example, the binder may include defatted or
full-fatted soybeans. In one embodiment, the binder may be as
described in pending U.S. patent application Ser. No. 13/367,138,
filed on Feb. 2, 2012 and entitled "Methods For Producing Binders
and Combustible Composite Materials and Compositions Produced
Therefrom," the disclosure of which is incorporated herein by
reference in its entirety.
[0026] In one embodiment, the inert atmosphere includes an inert
gas selected from the group consisting of nitrogen, carbon dioxide,
and steam. Other inert gasses may also be used. The inert
atmosphere may be substantially free of excess oxygen. In one
embodiment, the inert atmosphere includes an oxygen displacing
fluid. For example, the inert atmosphere may include an oxygen
displacing foam or other material that renders the pelletizer
substantially oxygen-free. In one embodiment, the inert atmosphere
includes a glycerin foam, alone or in combination with an inert
gas. Other foams may also be used. For example, an inert gas may be
used to foam a foaming material. The foam may aid in capturing the
inert gas and maintaining the inert gas with the at least partially
carbonized biomass during subsequent processing.
[0027] In one embodiment, the method includes applying water to the
at least partially carbonized biomass prior to the step of
pelletization. In one embodiment, the at least partially carbonized
biomass has a moisture content of from about 2 percent to about 40
percent, from about 2 percent to about 30 percent, from about 5
percent to about 30 percent, or from about 10 percent to about 30
percent by weight of the at least partially carbonized biomass. For
example, water may be applied to the at least partially carbonized
biomass such that it obtains a moisture content of about 10 percent
by weight of the at least partially carbonized biomass or from
about 2 percent to about 40 percent by weight of the at least
partially carbonized biomass. In certain embodiments, where the at
least partially carbonized biomass contains moisture, the step of
pelletizing may produce steam from the biomass that acts as at
least a portion of the inert gas of the inert atmosphere.
[0028] In another aspect, a method for producing a pelletized
carbonized fuel product is provided. The method includes at least
partially carbonizing a biomass feed to produce at least partially
carbonized biomass, and thereafter pelletizing the at least
partially carbonized biomass in an inert atmosphere to produce a
pelletized at least partially carbonized biomass fuel product. In
one embodiment, the step of at least partially carbonizing a
biomass feed includes torrefying the biomass feed or hydrothermally
carbonizing the biomass feed. For example, the biomass feed may
include wood. In one embodiment, the method includes applying a
binder to the at least partially carbonized biomass prior to the
step of pelletization. In one embodiment, the method includes
applying water to the at least partially carbonized biomass prior
to the step of pelletization such that the at least partially
carbonized biomass has a moisture content of at least about ten
percent or from about 2 percent to about 40 percent by weight of
the at least partially carbonized biomass.
[0029] In another aspect, an apparatus for producing a pelletized
fuel product is provided. As shown in FIG. 1, the apparatus 10
includes a feeder 12 of at least partially carbonized biomass, a
pelletizer 14 configured to receive and pelletize the at least
partially carbonized biomass, and an inert gas source 16 configured
to provide inert gas to the pelletizer 14. In certain embodiments,
the at least partially carbonized biomass includes torrefied wood
or hydrothermally carbonized wood. In one embodiment, the inert gas
includes nitrogen, carbon dioxide, or steam.
[0030] In certain embodiments, the pelletizer 14 includes one or
more of the following components: a pelletizing chamber 22, a
pelletizing discharge 24, a conveyance to cooling chamber 26, and a
cooling chamber 28. In a preferred embodiment, the pelletizer
includes pelletizing chamber 22. Inert gas source 16 may be
configured to provide inert gas to any or all components of
pelletizer 14. Separate inert gas sources may also provide inert
gas to the individual components of the pelletizer.
[0031] In one embodiment as shown in FIG. 1, the apparatus 10
includes a water source 20 configured to moisten the at least
partially carbonized biomass to a moisture content of at least
about ten percent prior to pelletization. The apparatus 10 also may
include a binder source 18 configured to introduce a binder to the
at least partially carbonized biomass prior to pelletization. For
example, the binder may be introduced to the at least partially
carbonized biomass such that the biomass contains binder in an
amount from about 0.5 percent to about 15 percent, from about 1
percent to about 10 percent, or from about 2 percent to about 5
percent by weight of the at least partially carbonized biomass. In
one embodiment, the biomass may contain binder in an amount of
about 2.5 percent by weight of the at least partially carbonized
biomass.
[0032] In another aspect, an apparatus for producing a pelletized
fuel product is provided. As shown in FIG. 2, the apparatus 50
includes a feeder 52 of raw biomass, a reactor 54 configured to
receive and at least partially carbonize the raw biomass, a
pelletizer 56 configured to receive and pelletize the at least
partially carbonized biomass, and an inert gas source 58 configured
to provide inert gas to the pelletizer. In one embodiment, the raw
biomass includes wood. In certain embodiments, the reactor is a
torrefaction reactor or a hydrothermal carbonization reactor.
[0033] In certain embodiments, the pelletizer 56 includes one or
more of the following components: a pelletizing chamber 64, a
pelletizing discharge 66, a conveyance to cooling chamber 68, and a
cooling chamber 70. In a preferred embodiment, the pelletizer
includes pelletizing chamber 64. Inert gas source 58 may be
configured to provide inert gas to any or all components of
pelletizer 56. Separate inert gas sources may also provide inert
gas to the individual components of the pelletizer.
[0034] In one embodiment as shown in FIG. 2, the apparatus 50
includes a water source 60 configured to moisten the at least
partially carbonized biomass to a moisture content of at least
about ten percent prior to pelletization. The apparatus 50 may also
include a binder source 62 configured to introduce a binder to the
at least partially carbonized biomass prior to pelletization.
[0035] The pelletizing chamber may include any known
pellet-producing mechanism. For example, the pelletizing chamber
may be a small ring die pellet mill, a commercial scale ring die
pellet mill, a punch-and-die pellet machine, or a pellet press or
the like. For example, the die may be an 8 mm die.
[0036] Publications cited herein and the materials for which they
are cited are specifically incorporated by reference herein.
Modifications and variations of the methods and compositions
described herein will be obvious to those skilled in the art from
the foregoing detailed description. Such modifications and
variations are intended to come within the scope of the appended
claims.
* * * * *