U.S. patent application number 16/005593 was filed with the patent office on 2019-05-09 for systems and methods for temperature control and heat extraction from waste landfills.
The applicant listed for this patent is James L. Hanson, Nazli Yesiller. Invention is credited to James L. Hanson, Nazli Yesiller.
Application Number | 20190137144 16/005593 |
Document ID | / |
Family ID | 53172102 |
Filed Date | 2019-05-09 |
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United States Patent
Application |
20190137144 |
Kind Code |
A1 |
Yesiller; Nazli ; et
al. |
May 9, 2019 |
SYSTEMS AND METHODS FOR TEMPERATURE CONTROL AND HEAT EXTRACTION
FROM WASTE LANDFILLS
Abstract
The field of the invention relates to systems and methods for
exchanging heat from the degradation, decomposition, and
chemical/biochemical transformation of municipal, industrial, and
other types of waste. In one embodiment, a heat extraction system
may include a closed-loop fluid circulation piping channeled
throughout at least one heat extraction well oriented throughout a
waste mass. The piping is fluidly coupled to a heat exchanger. A
first circulation fluid is circulated through the closed-loop
circulation piping into various depths of the waste mass to
transfer thermal energy between said mass and said heat exchanger.
In one embodiment, the transfer of thermal energy between the waste
mass and the heat exchanger is used as alternative energy method
and to control at least one of shear strength, compressibility, and
hydraulic conductivity of the waste mass.
Inventors: |
Yesiller; Nazli; (San Luis
Obispo, CA) ; Hanson; James L.; (San Luis Obispo,
CA) |
|
Applicant: |
Name |
City |
State |
Country |
Type |
Yesiller; Nazli
Hanson; James L. |
San Luis Obispo
San Luis Obispo |
CA
CA |
US
US |
|
|
Family ID: |
53172102 |
Appl. No.: |
16/005593 |
Filed: |
June 11, 2018 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
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15232754 |
Aug 9, 2016 |
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16005593 |
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14522503 |
Oct 23, 2014 |
9435569 |
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15232754 |
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14162448 |
Jan 23, 2014 |
9255727 |
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14522503 |
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13190313 |
Jul 25, 2011 |
8672586 |
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14162448 |
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Current U.S.
Class: |
1/1 |
Current CPC
Class: |
Y02A 30/274 20180101;
F25B 27/02 20130101; B09B 1/006 20130101; F24T 2010/56 20180501;
Y02E 10/10 20130101; Y02E 10/125 20130101; F24T 10/17 20180501 |
International
Class: |
F24T 10/17 20180101
F24T010/17; F25B 27/02 20060101 F25B027/02; B09B 1/00 20060101
B09B001/00 |
Claims
1. A temperature control and heat exchange system comprising: a
closed-loop fluid circulation pipe; at least one heat transfer well
providing a thermal encasement for the closed-loop fluid
circulation pipe, the heat transfer well filled at intervals with a
highly conductive granular backfill; wherein the at least one heat
transfer well is installed in a waste mass; a heat exchanger having
an inlet and outlet for a first circulation fluid and an inlet and
outlet for a second circulation fluid; a circulation pump
operatively coupled to the closed-loop circulation pipe to provide
fluid flow for the first circulation fluid; and wherein the heat
exchanger is fluidly coupled to the closed-loop fluid circulation
pipe at the inlet and outlet for the first circulation fluid such
that the first circulation fluid, when circulated through the
closed-loop fluid circulation pipe via the circulation pump into
the at least one heat transfer well distributed in the waste mass,
transfers thermal energy between the waste mass and the second
circulation fluid through the heat exchanger.
2. The temperature control and heat exchange system of claim 1,
further comprising: a microprocessor computer coupled to both the
heat exchanger and the circulation pump, wherein the microprocessor
computer is operable to control, via control signals, fluid flow of
the first circulation fluid using the circulation pump and thermal
energy transfer of the first circulation fluid using the heat
exchanger.
3. The temperature control and heat exchange system of claim 2,
further comprising: a network of sensors integrated into the
closed-loop fluid circulation pipe and the waste mass and
electronically coupled to the computer providing control signals to
the computer, wherein the network of sensors is operable to detect
at least one of temperature, position, time, and flow-rate.
4. The temperature control and heat exchange system of claim 1,
wherein the at least one heat transfer well encasing the
closed-loop fluid circulation pipe is installed in the waste mass
either vertically, horizontally, or at an incline.
5. The temperature control and heat exchange system of claim 1,
further comprising: a thermostat-controlled trace heater operable
to prevent freezing of the first circulation fluid.
6. The temperature control and heat exchange system of claim 1,
wherein the heat exchanger is a plate and frame heat exchanger.
7. The temperature control and heat exchange system of claim 1,
wherein the highly conductive granular backfill is dense gravel,
soil, or industrial byproduct.
8. The temperature control and heat exchange system of claim 1,
wherein the closed-loop fluid circulation pipe is plastic, metal,
or composite material.
9. The temperature control and heat exchange system of claim 1,
wherein the first circulation fluid is water, propylene glycol, or
a water-glycol mixture.
10. The temperature control and heat exchange system of claim 1,
wherein the at least one heat transfer well is covered by an
insulating seal at a ground surface.
11. A process of controlling the temperature in a waste mass when
the waste mass has at least a first, second, third, and fourth life
cycle stage of biochemical processes using a heat exchanger,
comprising: using the heat exchanger which is fluidly coupled with
a first circulation fluid and a second circulation fluid to
transfer a first level of thermal energy from the second
circulation fluid to the first circulation fluid during the first
life cycle stage of biochemical processes of the waste mass, using
the heat exchanger to transfer a second level of thermal energy
from the first circulation fluid to the second circulation fluid
during the second life cycle stage of biochemical processes of the
waste mass, using the heat exchanger to transfer a third level of
thermal energy from the second circulation fluid to the first
circulation fluid during the third life cycle stage of biochemical
processes of the waste mass, and using the heat exchanger to
transfer a fourth level of thermal energy from the first
circulation fluid to the second circulation fluid during the fourth
life cycle stage of biochemical processes of the waste mass, where
the first circulation fluid circulates in a closed-loop fluid
circulation pipe due to operation of a circulation pump coupled to
the closed-loop circulation pipe and the closed-loop circulation
pipe is encased in at least one heat transfer well which is filled
at intervals with a highly conductive granular backfill.
12. The process of controlling the temperature in a waste mass when
the waste mass has at least a first, second, third, and fourth life
cycle stage of biochemical processes using a heat exchanger of
claim 11, wherein the transfer of the first level of thermal energy
from the second circulation fluid to the first circulation fluid
during the first life cycle stage of biochemical processes of the
waste mass cools the waste mass.
13. The process of controlling the temperature in a waste mass when
the waste mass has at least a first, second, third, and fourth life
cycle stage of biochemical processes using a heat exchanger of
claim 11, wherein the transfer of the first level of thermal energy
from the second circulation fluid to the first circulation fluid at
the first life cycle stage of biochemical processes of the waste
mass heats to the waste mass.
14. A method of temperature control and heat exchange in a waste
mass comprising: routing at least one heat transfer well in the
waste mass; channeling a closed-loop fluid circulation pipe into
the at least one heat transfer well such that the at least one heat
transfer well provides a thermal encasement for the closed-loop
fluid circulation pipe, the at least one heat transfer well filled
at intervals with a highly conductive granular backfill;
circulating a first circulation fluid in the closed-loop fluid
circulation pipe using a circulation pump operatively coupled to
the closed-loop circulation pipe; and exchanging heat between the
first circulation fluid and a second circulation fluid using a heat
exchanger, the heat exchanger having an inlet and outlet for the
first circulation fluid and being hydraulically coupled to provide
fluid circulation to the closed-loop circulation pipe at the inlet
and outlet for the first circulation fluid and having an inlet and
outlet for the second circulation fluid.
15. The method of temperature control and heat exchange in a waste
mass of claim 14, wherein the heat exchanger and the circulation
pump are coupled to a microprocessor computer operable to control,
via control signals, fluid flow of the first circulation fluid
using the circulation pump and thermal energy transfer of the first
circulation fluid using the heat exchanger.
16. The method of temperature control and heat exchange in a waste
mass of claim 14, wherein exchanging heat between the first
circulation fluid and the second circulation fluid influences at
least one of shear strength, compressibility, and hydraulic
conductivity of the waste mass.
17. The method of temperature control and heat exchange in a waste
mass of claim 14, wherein the first circulation fluid is water,
propylene glycol, or a water-glycol mixture.
18. The method of temperature control and heat exchange in a waste
mass of claim 14, comprising: monitoring at least one of
temperature, position, time, and flow-rate of the first circulation
fluid using a network of sensors integrated into the closed-loop
fluid circulation pipe and the waste mass, the network of sensors
electronically coupled to the computer providing control signals to
the computer.
Description
CROSS-REFERENCE TO RELATED APPLICATIONS
[0001] The present application is a continuation of U.S.
application Ser. No. 15/232,754, filed Aug. 9, 2016, which is a
continuation of U.S. application Ser. No. 14/522,503, filed Oct.
23, 2014, and issued as U.S. Pat. No. 9,435,569, which is a
continuation-in-part of U.S. application Ser. No. 14/162,448, filed
Jan. 23, 2014, and issued as U.S. Pat. No. 9,255,727, which is a
continuation of and claims the benefit of U.S. application Ser. No.
13/190,313, filed Jul. 25, 2011 and issued as U.S. Pat. No.
8,672,586, all of which are hereby incorporated in their entireties
by reference.
FIELD OF THE INVENTION
[0002] The field of the invention relates to systems and methods
for temperature control and heat extraction, and more particularly
to systems and methods for controlling and manipulating temperature
and extracting heat from the degradation, decomposition, and
chemical/biochemical transformation of municipal, industrial, and
other types of waste.
BACKGROUND OF THE INVENTION
[0003] Continued increases in generation of industrial and
municipal solid waste (MSW) has resulted in increased use of
landfill sites worldwide. The U.S. Environmental Protection Agency
estimates that the MSW generation in the U.S. is approximately 240
million tons (U.S. E.P.A. 2009). A significant portion of the waste
is disposed of in landfills. As MSW landfills undergo normal
operation, the primary byproducts of the landfill processes are
heat, gas, and leachate (i.e., contaminated liquid generated due to
passage of liquid through the waste mass). Significant amounts of
other types of wastes such as industrial waste, agricultural waste,
mining waste, and other types of wastes also are generated in the
U.S. on an annual basis.
[0004] Turning to FIG. 1, an example of a typical waste landfill
100 is illustrated. Generally, a low permeability barrier 103 is
placed over ground surface 105. The waste mass 101 is deposited and
landfilled upon the barrier 103. Waste mass 101 may consist of, for
example, alternating layers of soil and trash. The landfilled waste
mass 101 is covered with a low permeability cover 102. The total
depth 104 of waste landfill 100 varies, for example, between tens
to hundreds of feet.
[0005] In the waste that is buried or landfilled, the organic
components decompose resulting in generation of heat and gas that
can be converted to usable energy. A considerable amount of energy
is produced in this manner. In fact, a mid-sized landfill--such as
the Riverview Landfill in Riverview, Mich.--can provide energy
equivalent to 10,000 residential homes. A number of recognized
techniques for effectively using landfill sites are based on, for
example, collecting the gas produced from decomposed waste and
converting to energy or maintaining conditions for recycling
leachate. Furthermore, these techniques attempt to minimize both
nearby contamination and atmospheric pollution.
[0006] For example, waste decomposition in a landfill produces an
effluent gas, which contains about fifty percent (50%) methane
(CH.sub.4). This landfill gas in the interior of the landfill is
often at a higher pressure than that of the surrounding atmosphere.
Consequently, this pressure differential creates a migration
pattern of the landfill gas towards both the surface (vertically)
and near the edges/perimeter (horizontally) of the landfill.
However, methane is an inflammable gas that not only can damage
plants in a nearby area but also lead to a danger of explosion.
Additionally, emission into the atmosphere of the landfill gas
contributes to the "greenhouse effect" as a direct factor to
abnormal climate phenomena. With respect to environmental
pollution, where the level of methane contained in the landfill gas
is in the amount of 50 to 60%, the influence on the "greenhouse
effect" is approximately 21 times or greater compared to that of
carbon dioxide (CO.sub.2). However, as methane also has a
beneficial combustion property, it is possible to collect the gas
from a landfill to provide an efficient energy resource.
[0007] A conventional technique of controlling the withdrawal of
gas from a landfill site is to drill deep vertical wells, such as
well 106 in FIG. 1, into the landfill. These vertical wells are
attached to a network of pipes and gas pumps (not shown) to
vacuum/extract gas from the wells. An example of such a system
implementing this technique is disclosed in U.S. Pat. No.
7,448,828, to Augenstein et al., filed Feb. 23, 2007 for a
"Landfill design and method for improved landfill gas capture,"
which is hereby incorporated by reference in its entirety. This
system contemplates an improved method for collecting landfill gas
by minimizing the collection of atmospheric air with the gas.
[0008] Another example of effective landfill use controls gas
generation rates of the landfill through leachate regulation. This
technique involves regulating both temperature and pH levels of
leachate to be recycled and continuously injected into a deposit of
wastes. For example, see U.S. Pat. No. 6,334,737, to Lee, filed
Dec. 17, 1999 for a "Method and apparatus of controlling landfill
gas generation within a landfill," which is hereby incorporated by
reference in its entirety. Monitoring and controlling a variety of
conditions for recycling leachate provides the advantage of
maintaining, as consistently as possible, the level of gas
production during the landfill process.
[0009] Significant amount of research and development has been
reported for gas and leachate. However, less information is
available on heat generation in landfills. Elevated temperatures
can affect the ongoing biochemical processes (e.g., decomposition)
and mechanical and hydraulic properties/behavior of the wastes.
Operational and climatic conditions have significant effects on
heat generation and transfer in landfills. For example, see
Yesiller et al., for "Heat Generation in Municipal Solid Waste
Landfills" (Yesiller, N., Hanson, J. L., and Liu, W.-L., Journal of
Geotechnical and Geoenvironmental Engineering, ASCE, Vol. 131, No.
11, p. 1330-44 (2005)) and Yesiller and Hanson, for "Analysis of
Temperatures at a Municipal Solid Waste Landfill" (Yesiller, N. and
Hanson, J. L. "Analysis of Temperatures at a Municipal Waste
Landfill," Sardinia 2003, Ninth International Waste Management and
Landfill Symposium, Christensen et al. Eds., CISA, Italy, p. 1-10
(2003)), which are hereby incorporated by reference in their
entirety. These effects may be short-term (e.g., reaction rates)
and/or long-term (e.g., microbial population balance within the
waste). In general, waste decomposition rates generally increase
with increased temperatures up to a point of killing microbial
populations (e.g., approximately 70.degree. C.).
[0010] Temperatures within landfills undergo seasonal fluctuations
near the surface and edges/perimeter of the landfill due, in part,
to conductive and convective heat transfer. Elevated temperatures
are correspondingly observed within the landfilled mass at central
locations. Accordingly, optimal decomposition and gas production
conditions are not uniform within a landfill mass.
[0011] Current systems for energy extraction from MSW landfills
focus on the generation and distribution of gas and leachate in
landfills. However, such systems do not take advantage of a
detailed analysis of spatial heat distribution or a long-term
thermal trend of landfills. In addition, systems are not available
for controlling and manipulating temperatures in landfills.
Furthermore, current systems do not provide a method for creating a
symbiotic energy source between the landfill and nearby facilities
to create optimal operating conditions.
[0012] Accordingly, a system and method for controlling and
manipulating temperatures and extracting heat from a landfill that
considers heat generation and temperature distribution within a
landfill is desired.
SUMMARY OF THE INVENTION
[0013] The field of the invention relates to systems and methods
for heat exchange, and more particularly to systems and methods for
controlling and manipulating temperature and extracting heat from
the degradation, decomposition, and chemical/biochemical
transformation of municipal, industrial, and other types of waste.
In one embodiment, a temperature control and heat extraction system
may include at least one heat exchange well providing a channel for
a closed-loop fluid circulation piping that contains a first
circulation fluid. The at least one closed-loop well extends
throughout a waste mass. The closed-loop fluid circulation piping
runs throughout the network of heat exchange wells and is fluidly
coupled to a heat exchanger. The heat exchanger has a first inlet
and outlet for the first circulation fluid and exchanges heat to a
second circulation fluid through a second inlet and outlet. The
system further includes a highly conductive granular backfill
intermittently dispersed within the at least one fluid circulation
well to provide a thermal encasing for said piping. The first
circulation fluid is circulated, via a circulation pump operatively
coupled to the piping, through the closed-loop circulation piping
into various depths of the waste mass to transfer thermal energy
from said mass to the heat exchanger.
[0014] In one embodiment, the waste mass has a first, second,
third, and fourth life cycle stage of biochemical reactions. The
transfer of thermal energy includes the steps of providing a first
level of heat to the heat exchanger at the first life cycle stage
of a waste mass, wherein the heat exchanger provides heat to said
mass through the at least one closed-loop fluid circulation well;
extracting heat from the at least one closed-loop fluid circulation
well through the heat exchanger at the second life cycle stage of
the waste mass; providing a second level of heat to the heat
exchanger at the third life cycle stage of the waste mass; and
maintaining a long-term heat exchange to or from the waste mass
through the heat exchanger at the fourth life cycle stage of the
waste mass.
[0015] Other systems, methods, features and advantages of the
invention will be or will become apparent to one with skill in the
art upon examination of the following figures and detailed
description. It is intended that all such additional systems,
methods, features and advantages be included within this
description, be within the scope of the invention, and be protected
by the accompanying claims.
BRIEF DESCRIPTION OF THE DRAWINGS
[0016] In order to better appreciate how the above-recited and
other advantages and objects of the inventions are obtained, a more
particular description of the embodiments briefly described above
will be rendered by reference to specific embodiments thereof,
which are illustrated in the accompanying drawings. It should be
noted that the components in the figures are not necessarily to
scale, emphasis instead being placed upon illustrating the
principles of the invention. Moreover, in the figures, like
reference numerals designate corresponding parts throughout the
different views. However, like parts do not always have like
reference numerals. Moreover, all illustrations are intended to
convey concepts, where relative sizes, shapes and other detailed
attributes may be illustrated schematically rather than literally
or precisely.
[0017] FIG. 1 is a diagram of a municipal waste landfill known in
the art.
[0018] FIG. 2a is a chart representing measurements of temperatures
at various depths within waste mass as a function of time;
[0019] FIG. 2b is a curve representing general earth temperature
trends as a function of depth.
[0020] FIG. 3 is a chart illustrating measured temperatures and
analytically calculated temperatures within waste mass as a
function of time.
[0021] FIG. 4a is a chart representing a series of measured heat
content within waste mass for various sites as a function of
depth;
[0022] FIG. 4b is another chart representing a series of measured
heat content within waste mass for various sites as a function of
normalized depth;
[0023] FIG. 4c is a curve representing heat content as a function
of initial temperature of a waste mass.
[0024] FIG. 5 is a diagram representing the trend of heat content
for various sites as a function of waste age.
[0025] FIG. 6a is a diagram of a heat exchange system in accordance
with a preferred embodiment of the present invention.
[0026] FIG. 6b is a diagram of a heat exchange system in accordance
with a preferred embodiment of the present invention.
[0027] FIG. 6c is a diagram of a heat exchange system in accordance
with a preferred embodiment of the present invention.
[0028] FIG. 7a is another diagram of a heat exchange system in
accordance with a preferred embodiment of the present
invention;
[0029] FIG. 7b is another diagram of a heat exchange system in
accordance with a preferred embodiment of the present invention;
and
[0030] FIG. 8 is a chart illustrating exemplary thermal exchange
stages in accordance with a preferred embodiment of the present
invention.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
[0031] As described above, heat is generated as a result of
biochemical processes and decomposition of organic components in
wastes as well as chemical/biochemical transformation of various
components in wastes. Field measurements of temperatures within
landfills reveal spatial variations of temperature as a function of
depth.
[0032] FIG. 2a illustrates an example of temporal variations in
temperature with location at a given depth of waste landfill 100.
Temperatures at relatively shallow depths of waste mass 101 (e.g.,
at the surface as well as near the edges/perimeter of the waste
mass) undergo seasonal fluctuation similar to variability in earth
temperature, which is shown in FIG. 2b. Turning to FIG. 2b, ground
surface 203 provides range T of temperatures from low temperatures
201 (e.g., 0.degree. C.) to elevated temperatures 202 (e.g.,
40.degree. C.). Elevated temperatures approach temperature 204,
which is the mean annual earth temperature, as the measurement
depth increases. Range T of temperatures at ground surface 203
illustrates a similar trend in waste mass temperatures at shallow
depths in FIG. 2a.
[0033] Conversely, stable, elevated temperatures (e.g.,
50-60.degree. C.) can be seen near mid-depth of landfill 100 in
FIG. 2a (e.g., 13-9 meters). The seasonal variations of temperature
within waste mass 101 decrease significantly at locations away from
the edges of the landfill (e.g., 20 meters from air surface). These
steady elevated temperatures also may increase over time.
[0034] At intermediate depths between the edges and center of waste
mass 101, temperatures demonstrate phase lag as well as amplitude
decrement in relation to ground-surface temperatures shown in FIG.
2b. Phase lag can represent the delay in timing of peak seasonal
temperatures at a given depth relative to corresponding peaks at
the ground surface. Amplitude can represent the one-half the
maximum range of temperature measured in a single year.
[0035] Given a typical thermal gradient of waste mass 101 in FIG.
2a, heat gain in the waste compared to unheated (i.e., ambient)
baseline conditions can be determined. This difference between
measured waste temperature, as shown in FIG. 2a, and unheated
baseline waste temperature at equivalent depths is known as the
Heat Content (HC) of the waste mass. Specifically, HC represents
the average temperature differential of the waste mass as compared
to unheated conditions. In order to determine the HC, the baseline
waste temperatures can be determined using equation (1), which is
an analytical formulation for ground temperature at any depth on
any calendar day.
T ( x , t ) = T m - A s e - x .PI. 365 .alpha. cos 2 .PI. 365 ( t -
t 0 - x 2 365 .PI..alpha. ) ( 1 ) ##EQU00001##
where:
[0036] T.sub.(x,t)=temperature (.degree. C.) at depth, x and at
time, t
[0037] T.sub.m=mean annual earth temperature (.degree. C.)
[0038] A.sub.s=amplitude of surface temperature wave (.degree.
C.)
[0039] x=depth below surface (m)
[0040] .alpha.=thermal diffusivity (m.sup.2/day)
[0041] t=time of year, days (where 0=midnight December 31)
[0042] t.sub.0=phase constant (34.6 days)
[0043] Analytical and numerical approaches have been developed for
modeling temperatures in municipal solid waste landfills with heat
generation in wastes due to decomposition, underlying native soil
conditions, and overlying seasonal air temperature fluctuations. A
typical example of thermal modeling for various landfill sites is
contained in a study from Hanson et al for an "Analytical and
Numerical Methodology for Modeling Temperatures in Landfills"
(Hanson, J. L., Liu, W.-L, and Yesiller, N., Proceedings of
Selected Sessions of GeoCongress 08: Geotechnics of Waste
Management and Remediation, ASCE GSP No. 177, Khire et al., eds.,
ASCE, Reston, Va., p. 24-31 (2008)), which is hereby incorporated
by reference in its entirety. In determining a baseline ground
temperature profile in a landfill application, thermal diffusivity
(a) values between approximately 3.times.10.sup.-7 m.sup.2/sec to
7.times.10.sup.-7 m.sup.2/sec can be used for an equivalent waste
mass that is not undergoing seasonal temperature variations and not
gaining heat due to biochemical decomposition.
[0044] With reference to FIG. 3, the HC of a landfill site can be
determined by calculating the area between the time-temperature
curves of the measured waste temperatures and the analytical
baseline unheated waste temperatures governed by equation (1). FIG.
3 illustrates a typical temperature change within waste over time.
Temperature curve 302 represents a measured temperature within
waste mass 101, using sensor arrays or other suitable measurement
tools, at a given depth. For example, Type K thermocouples deployed
in custom-fabricated flexible sensor arrays ranging from a length
between 1 and 60 m for vertical installations and between 150 and
200 m for horizontal installations may be used. These sensors
provide high resistance to chemical environments and are well
suited for landfill applications. Additional information regarding
sensor arrays can be found in an article for "Spatial and Temporal
Temperature Distributions in Municipal Solid Waste Landfills"
(Hanson, J. L., Yesiller, N., and Oettle, N., Journal of
Environmental Engineering ASCE, Vol. 136, No. 8, p. 804-814
(2010)), which is hereby incorporated by reference.
[0045] Temperature curve 303 provides equivalent ambient waste
temperatures at the specified depth, calculated using the
analytical solution (1) discussed above. As can be seen in FIG. 3,
shaded area 304 represents the area between temperature curves 302
and 303, which provides the total heat gain due to biological and
chemical activity of waste mass 101 in units of degree-days.
Furthermore, shaded area 304 can be divided by the duration of the
analysis period to normalize HC with respect to time. The resulting
calculation provides HC as a time weighted average of the change in
temperature from unheated conditions in units of degrees-centigrade
day per day (.degree. C. day/day). Accordingly, this calculation
provides heat gain in waste mass 101 due to, for example,
decomposition, rather than the effects of seasonal/climatic
variation of temperature occurring at the given depth.
[0046] The analysis of HC for various locations reveals that higher
HC can be found in the central core of waste mass rather than near
the edges, top surfaces, and bases of waste mass 101, as
illustrated in FIG. 4a. FIG. 4a provides typical examples of the
variation of HC as a function of the depth of the sensors in the
waste mass 101. The curves in FIG. 4a demonstrate elevated heat
content near central depths of waste mass. In each of these
measurements of HC, the HC is linearly related to the initial waste
temperature and waste placement rate (m/year). FIG. 4c shows the
general relationship between measured HC values as a function of
the initial waste temperature.
[0047] FIG. 4b represents the measurements of HC as a function of
the respective normalized depth--the ratio of the depth of the
measurement over the total depth to linear 104. The curves of FIG.
4b verify that the peak HC occurs at normalized depths near the
mass-center (i.e., normalized depth near 0.5).
[0048] Using common exponential growth and decay functions, it is
then possible to model the relationship between HC and the life
cycle of a landfill (i.e., time representing the age of waste).
Specifically, equation (2) was developed in the form of the
Streeter-Phelps approach (presented in Vesilind, P. A., 1997,
Introduction to Environmental Engineering) for modeling HC as a
function of time for waste.
HC = a .psi. ( b - a ) ( e - at w - e - bt w ) ( 2 )
##EQU00002##
where:
[0049] HC=heat content (.degree. C.-day/day)
[0050] a=heat generation constant (day.sup.-1)
[0051] b=heat utilization constant (day.sup.-1)
[0052] .psi.=heat production potential (.degree. C.-day/day)
[0053] t.sub.w=waste age (year)
[0054] Examples of the model curve generated by equation (2) for
sites measured in FIG. 4a are illustrated in FIG. 5. FIG. 5 shows
the variation of the maximum HC with waste age for various sensors.
In general, HC can be seen to increase in a first life cycle of
waste degradation (e.g., 2 to 4 years for a landfill in a humid
continental temperate climate) followed by a period of decrease at
a slower rate to a stable low value of HC.
[0055] HC also may be used to determine heat generation of the
waste mass. Heat generation is defined as the energy required to
raise the temperature of the waste mass and can be determined using
the heat capacity of the waste, the magnitude of temperature
increase of the waste, the evaporation of water into the landfill
gas phase, the temperature of the biochemical reactions, and the
heat loss to the surrounding environment. This energy production
can be calculated using equation (3).
E = i = 1 n .DELTA. T i cM ( T ) i ( 3 ) ##EQU00003##
where:
[0056] E=energy production (heat generation, MJ/m.sup.3)
[0057] .DELTA.T.sub.i=increment of temperature rise for waste
(K)
[0058] c=heat capacity of waste (MJ/m.sup.3K)
[0059] M(T).sub.i=fraction of energy released that is used for
heating a landfill
In order to determine heat generation for various representations
of HC, for example, those curves represented in FIG. 4, the peak HC
for a given location can be used as the magnitude of temperature
increase of the waste. In this example, with references to FIG. 4
and equation (3), the energy produced E for HC measurements in FIG.
4 range from 23 and 77 MJ/m.sup.3 for the various sites. Similar to
the results illustrated in FIG. 5, variations in energy produced E
occurs as a function of waste age. Additionally, energy E peaks and
heat content HC peaks are also similar in timing.
[0060] Despite low permeability cover 102 used in most landfill
sites and the relatively high insulating quality of MSW, heat loss
to the surrounding environment should be considered in a
determination of heat generation. For example, from a central core
of waste mass (i.e., the location of the highest HC) to an average
annual air temperature location (e.g., landfill cover 102) and
subgrade 10 m below the barrier at mean annual earth temperature,
the magnitude of conductive thermal losses to the surrounding
environment can range between 42 and 139 MJ/m.sup.3-year for losses
towards the cover and atmosphere (upward losses) and between 6 and
152 MJ/m.sup.3-year for losses towards the barrier and subgrade
(downward losses). Similarly, convective losses, for example,
through leachate records, may range between 0 and 11
MJ/m.sup.3-year. As discussed above, biochemical processes of waste
decomposition varies as a function of temperature. Current systems
attempt to extract energy from landfills through the control of the
gas production in landfill sites. Temperature conditions may affect
the rate at which these systems produce usable gas; however, as
decomposition produces heat, alternative uses for the heat energy
are typically not utilized. One approach that benefits from the
elevated temperature conditions discussed above is shown in FIG.
6a, which shows system 600 for heat exchange in accordance with an
embodiment of the present invention. The system 600 preferably
includes at least one heat exchange well 601 extending throughout
waste mass 606. Heat exchange well 601 provides a channel for
closed-loop fluid circulation piping 603, which is routed below
ground surface 602 through heat exchange well 601. In one
embodiment of the present invention, the portion of piping 603
submerged below ground surface 602 may be of cross-linked
polyethylene (PEX), high density polyethylene, copper, or other
metal, plastic, or composite materials. Composite materials can
include metal and plastic combinations or fiber composites such as
glass fiber or carbon fiber. In some embodiments, carbon fiber
reinforced polymer and glass fiber reinforced polymer can be used.
Such piping provides durability in a chemically aggressive
environment, resistance to heat, and flexibility for both
differential movements within waste mass 606 and seismic
deformations in waste mass 606. However, it is also appreciated by
one of ordinary skill that the piping 603 may also be of any
material suitable for heat exchange.
[0061] Additionally, the annular space surrounding piping 603
within heat extraction well 601 may be filled with a highly
conductive granular backfill 604 (e.g., dense gravel, soil, or
industrial byproduct such as foundry sand, cement kiln dust,
recycled concrete aggregate, steel slag, fly ash, blast furnace
slag, metal processing wastes, industrial sludges, mining wastes,
waste rock, and heavy construction/demolition debris, etc.) to
provide a material with high thermal conductivity for efficient
heat transfer between the fluid circulated in said piping 603 (not
shown) and waste mass 606. An insulating seal 607 is applied at the
surface 602 of well 601 to prevent convective thermal losses. The
piping 603 extends beyond ground surface 602 and is fluidly coupled
to circulation pump 608 and heat exchanger 605. In one embodiment,
the portion of piping 603 above ground surface 602 may be metal to
provide UV resistance. Circulation pump 608 provides fluid flow
through the system 600 such that circulated fluid through piping
603 conductively transports heat from within waste mass 606 to heat
exchanger 605. FIG. 6b shows an example embodiment where the
annular space surrounding piping 603 within heat exchange well 601
may be filled at intervals with highly conductive backfill 604 to
provide a material with high thermal conductivity for efficient
heat transfer between the fluid circulated in said piping 603 (not
shown) and waste mass 606. Also included at intervals can be a
highly insulative fill 610. Examples of highly insulative fill 610
can include byproducts such as shredded tires, processed mattresses
and furniture, textiles, lightweight construction or demolition
debris, auto shredder fluff, packaging materials (e.g., packing
peanuts, bubble wrap, corrugate), shredded paper, organic
agricultural wastes, green wastes, and agricultural plastics.
Intervals of conductive and insulative materials are provided to
localize effects of thermal transfer. The configuration of backfill
(conductive versus insulative) can be varied over time to create
desired thermal transfer conditions. For instance conductive and
insulative fill can be added, removed and shifted to suit
conditions as appropriate depending on weather, time (seasonally,
monthly, weekly, diurnally or otherwise), age of the waste mass,
desired treatment of the waste mass and others. References to
intermittent elsewhere in this document should be understood to
mean at intervals as described in this paragraph. In some
embodiments intervals of highly conductive and highly insulative
backfill can be similarly sized or uniform. In some embodiments
intervals can be non-uniform. In some embodiments a single type of
highly conductive or highly insulative backfill can be used
exclusively in a heat exchange well 601 while in other embodiments
multiple types of highly conductive or insulative backfill can be
used as appropriate to achieve the desired heat exchange
characteristics. In some embodiments multiple types of highly
conductive backfill can be combined in a single interval while in
other embodiments a single type of highly conductive backfill can
be used in a single interval. In some embodiments multiple types of
highly insulative backfill can be combined in a single interval
while in other embodiments a single type of highly insulative
backfill can be used in a single interval.
[0062] FIG. 6c shows an example embodiment where the annular space
surrounding piping 603 within heat exchange well 601 may be filled
with highly insulative backfill 610. In some circumstances it can
be desirable to slow the heat transfer process. In some
circumstances it can be desirable to fill the annular space
surrounding piping 603 when the heat exchange process is no longer
beneficial.
[0063] At ground surface 602, heat can be provided to heat
exchanger 605 as an alternative source of energy. In one embodiment
of the present invention, a typical heat exchanger 605 may be a
plate and frame heat exchanger that includes a plurality of heat
transfer surfaces (not shown) for exposing the heated processed
fluid to a second fluid (circulating outside waste mass 606). The
heat exchanger 605 further includes a housing having a process
fluid inlet and a process fluid outlet for piping 603.
[0064] In operation, the piping 603 conductively transports heat in
a closed-loop system. Processing fluid (not shown) passes through
piping 603 downwardly into waste mass 606 to conductively transfer
elevated heat upwardly from central depths to the ground surface
602. It is also appreciated by one of ordinary skill that the
process fluid could also flow laterally or at an angle, depending
on the orientation of heat extraction well 601 and heat exchanger
605.
[0065] A closed-loop system provides heat while reducing public and
regulatory concern. The fluid used for circulation in piping 603 as
well as other fluids used in the system are self-contained and
avoid exposure to contaminants throughout the process. In one
embodiment of the present invention, the circulation fluid may be
water, which provides a high heat capacity for efficient thermal
exchange, propylene glycol, which prevents the fluid from freezing
near surface temperatures in colder atmospheric climates, or a
water-glycol mixture. For systems using water as a circulation
fluid, thermostat-controlled trace heaters (not shown) may be used
to avoid freezing of the fluid in system components located above a
frost line.
[0066] A microprocessor computer 609 coupled to both the heat
exchanger 605 and circulation pump 608 may be used to monitor and
control pumping rates and thermal energy transfer in the system.
The computer 609 can receive and manipulate signals including, for
example, temperature, position, flow-rate, and time related to the
circulated fluid and waste mass via a network of sensors (not
shown) integrated into piping 603 and throughout waste mass 606
electronically coupled to computer 609. Conventional sensors with
means for measuring temperature, position, time and flow-rate can
be used to provide computer 609 with control signals relating to
the circulated fluid and waste mass 606. For example, as discussed
above, Type K thermocouples deployed in custom-fabricated flexible
sensor arrays may be installed and coupled to computer 609.
[0067] The present invention provides an alternative heat source
that may be used, for example, by a nearby industry, landfill
office, maintenance garage, scale house, or other industrial,
commercial, or residential facility. In an alternative embodiment
of the present invention, FIG. 7a illustrates system 700 that
provides another application for heat extraction. Similar to heat
extraction well 601 of system 600, system 700 uses a network of
heat extraction wells 701 each providing a channel for a
closed-loop circular piping system oriented throughout waste mass
706. In one embodiment, heat extraction wells 701 extend vertically
into waste mass 706; however, wells 701 may also extend
horizontally throughout waste mass 706, as shown in FIG. 7b, such
that circulated fluid flows laterally into waste mass 706.
Similarly, wells 701 may also be placed at an incline (not shown)
into waste mass 706. For wells that are installed horizontally or
at an angle, placement of wells 701 would occur in stages as waste
mass 706 is landfilled onto barrier 705. This allows waste mass 706
to cover wells after installation. For wells that extend vertically
into waste mass 706, installation may occur during waste placement
or even after landfilling of waste mass 706 is complete.
[0068] Each well of network 701 may be filled with a highly
conductive granular backfill and covered with an insulating seal as
described in system 600. A barrier 705 is shown to sit upon native
subgrade soils 708. Waste mass 706 is landfilled onto barrier 705
and covered by a low permeability cover 707. The network of heat
extraction pipes channeled through wells 701 are jointly and
fluidly coupled to an integrated surface piping system 702. The
surface piping 702, represented by dotted lines, provides a
communal channel for transporting processed fluid (not shown) to
heat exchanger 703, located above surface 708. It should be
appreciated by one of ordinary skill that surface piping 702 or
heat exchanger 703 are not limited to placement above ground
surface 708 and may be partially or fully located below ground
surface 708. Circulation pump 710 is coupled to piping 702 to
provide fluid flow throughout the closed loop system 700. In one
embodiment, pump 710 is interposed between the heat extraction
wells 707 and heat exchanger 703; however, circulation pump 710 may
also be placed along circulation piping routed into wells 707 to
provide fluid flow throughout the system 700.
[0069] A microprocessor computer 711 coupled to both the heat
exchanger 703 and circulation pump 710 may be used to monitor and
control pumping rates and thermal transfer rates in the system. The
computer 711 can receive and manipulate signals including, for
example, temperature, position, flow-rate, and time related to the
circulated fluid via a network of sensors (not shown) integrated
into piping 702, circulation piping routed into wells 707, and
waste mass 706.
[0070] The processing fluid circulated through piping 702 and
throughout wells 701 is self-contained. Thermal energy transferred
to heat exchanger 703 may provide heat to nearby facility 704
through a second fluid (not shown) passing through surface or
subsurface piping 709. As discussed above, facility 704 may be, but
is not limited to, the landfill office operating system 700, a
maintenance garage, or a nearby industrial, commercial, or
residential facility.
[0071] Heat extraction system 700 also provides the means for
creating a symbiotic relationship between facility 704 and waste
mass 706. While elevated heat may be transferred as an alternative
energy source from waste mass 706 to facility 704, heat conversely
may be transferred from facility 704 to waste mass 706. This
technique has the advantage of accelerating gas and heat production
in the landfill because waste decomposition rates generally
increase with increased temperatures. As discussed with reference
to FIG. 4c, HC is linearly related to initial waste placement
temperatures. Elevated HC values occur where the initial waste
temperatures are also increased. Therefore, in order to elevate the
initial waste temperature at a landfill, system 700 may also be
used to provide additional heat to waste mass 706.
[0072] Facility 704 may provide thermal energy to heat exchanger
703 through piping 709. The heat transferred to the integrated
surface piping 702 can be conductively distributed throughout heat
extraction wells 701 to waste mass 706. Effectively controlling the
HC of waste mass reduces lag time between waste placement and
optimal gas extraction. The result is such that waste mass could
approach optimal heat and gas production levels rapidly after waste
placement at varying temperatures of the initial waste. An example
is provided with reference to FIG. 8.
[0073] Turning to FIG. 8, a more generalized trend of heat content
as a function of waste age is shown. As discussed above with
reference to FIG. 5 and equation (2), HC increases in the first
stage of the landfill life cycle t1. During period t1, gas
production rates also begin to increase (not shown) until the HC
reaches an elevated peak value characterizing a second stage of the
landfill life cycle t2. Similarly, the heat generated and gas
production levels (not shown) also peaks during t2. Following this
period of optimal performance of the landfill, HC decreases during
a third stage t3 of the landfill life cycle until a stable lower
value of HC, which ultimately approaches ambient conditions, is
reached in the fourth stage t4.
[0074] Preferably, the optimal performance of a landfill is
described by the most efficient thermal conditions for heat and gas
production levels. For example, an optimal temperature for growth
of mesophilic bacteria is approximately 35-40.degree. C. The
optimal temperature range for growth of thermophilic bacteria is
approximately 50-60.degree. C. Similar to the optimum mesophilic
range, optimal conditions for landfill gas production most notably,
of methane occurs between 34-41.degree. C. These temperature ranges
provide targets for optimal performance of a landfill relative to
gas production capacity. A system, such as system 700, that
supports thermal heat exchange can obtain these conditions in waste
mass 706 at an accelerated rate. Once the landfill reaches a stable
stage of heat production, the system may return to providing heat
from waste mass 706 to facility 704, thereby creating a symbiotic
relationship benefiting both waste mass 706 and facility 704.
Preferably, the symbiotic process would operate as follows.
[0075] In FIG. 8, during the early stage t1 of a landfill life
cycle, both HC and gas production rates increase. In one embodiment
of controlling the temperature of waste mass 706, facility 704 can
provide additional heat to heat exchanger 703 through piping 709
during t1. Heat is exchanged to integrated surface piping 702 and
can be circulated through network 701 of heat exchange wells to
provide additional heat to waste mass 706. This additional heat can
accelerate heat generation (and therefore increase HC) and gas
production rates similar to providing an electrical "jumpstart" to
a battery of an internal combustion engine vehicle. Once peak
performance of the landfill begins in stage t2, a symbiotic
relationship may begin such that waste mass 706 can return heat to
facility 704 and provide a long-term source of thermal energy for
use in industrial heating. However, as discussed above, following
the peak performance of the landfill in stage t2, HC of the waste
mass 706 may begin to decrease during stage t3 until a stable lower
level is reached in t4. This decrease may benefit from additional
heat exchange from facility 704. Providing heat to waste mass 706
once again during stage t3 may reduce the rate at which heat
generation and gas production levels are decreasing, thereby
prolonging the optimal productive stage of the landfill prior to
reaching stage t4. When the landfill eventually approaches the
stable levels of stage t4, system 700 can provide a constant source
of heat to facility 704 from waste mass 706. For example, waste
mass 706, having a stable elevated temperature measured at
mid-depth, can heat a fluid circulating in the network of heat
exchange wells 701 to a constant temperature above ambient
temperature conditions. Depending on seasonal climate fluctuations,
this heated fluid can proceed through integrated surface piping 702
towards heat exchanger 703 to be used for heating or cooling of
facility 704. The production of a constant source of heat creates a
renewable energy source similar to a conventional ground heat
source pump.
[0076] In an alternative embodiment of controlling temperature,
during the early stage t1 of a landfill life cycle, facility 704
can instead provide cooler temperatures to heat exchanger 703
through piping 709. This cooler temperature is exchanged to
integrated surface piping 702 and can be circulated through network
701 of heat exchange wells to cool temperatures within waste mass
706. Unlike providing additional heat, as described above, this
cooling effect can delay heat generation (and therefore postpone
elevated HC) and gas production rates. This would provide an
opportunity to delay significant capital expenditure, for example,
associated with construction of a gas collection system during this
time. Once peak performance of the landfill begins in a delayed
stage t2, a symbiotic relationship may begin, similarly as
discussed above, such that waste mass 706 can return heat to
facility 704 and provide a long-term source of thermal energy for
use in industrial heating. Following the peak performance of the
landfill in stage t2, HC of the waste mass 706 may begin to
decrease during stage t3 until a stable lower level is reached in
t4. This decrease may benefit from additional heat exchange from
facility 704. Providing heat to waste mass 706 once again during
stage t3 may reduce the rate at which heat generation and gas
production levels are decreasing, thereby prolonging the optimal
productive stage of the landfill prior to reaching stage t4. When
the landfill eventually approaches the stable levels of stage t4,
system 700 can provide a constant source of heat to facility 704
from waste mass 706. Depending on seasonal climate fluctuations,
this heated fluid can proceed through integrated surface piping 702
towards heat exchanger 703 to be used for heating or cooling of
facility 704. The production of a constant source of heat creates a
renewable energy source similar to a conventional ground heat
source pump.
[0077] Although the previous embodiments are based on the waste
mass 706 having decomposition stages as shown in FIG. 8, the system
would be applicable in other types of waste landfills. In addition
to municipal solid waste landfills, elevated temperatures also have
been observed in other types of landfills. For example, in a case
study, Klein et al. (2001) reported that temperatures up to
87.degree. C. were observed at a municipal solid waste incineration
bottom ash landfill. These elevated temperatures were due to
exothermic reactions occurring in the waste mass with the highest
temperatures occurring in the central zones of the waste mass.
Additional information can be found in Klein, R., et al., for
"Temperature development in a modern municipal solid waste
incineration (MSWI) bottom ash landfill with regard to sustainable
waste management" (Klein, R., Baumann, T., Kahapka, E., Niessner,
R., Journal of Hazardous Materials, B83, p. 265-80 (2001)), which
is hereby incorporated by reference in its entirety. Although these
various waste types may not display similar biochemical reactions
as shown in FIG. 8, system 700 may still be used to exchange heat
and control temperature within these various waste types.
[0078] In addition to the preceding benefits, managing the
temperature of waste mass 706 can directly influence the
geomechanical behavior of the waste mass. The engineering
properties of soils vary as a function of temperature. For example,
see Mitchell, J. K. & Soga, K., Fundamentals of Soil Behavior,
John Wiley & Sons, Inc. Hoboken, N.J. (3rd ed. 2005), which is
hereby incorporated by reference in its entirety. The particulate
structure of geomaterials is affected by changes in temperature due
to particle contact characteristics. Stiffness and strength of
particle contacts have been described using the rate process
theory, and temperature-dependent prediction models using this
theory have been developed to predict soil settlement. Fox, P. J.,
"An Analysis of One-Dimensional Creep of Peat," Ph.D. Thesis,
University of Wisconsin, Department of Civil and Environmental
Engineering, Madison Wis. (1992), which is hereby incorporated by
reference in its entirety. Fluids within geomaterials--typically
water--are also affected by changes in temperature. Viscosity of
fluids change with temperature and excess pore water pressures are
developed due to differential thermal expansion of liquid and solid
phases of the composite materials. Campanella, R. G. &
Mitchell, J. K., "Influence of Temperature Variations on Soil
Behavior," Journal of Soil Mechanics and Foundation Engineering,
ASCE, Vol. 94, SM3, p. 709-734 (1968), which is hereby incorporated
by reference in its entirety. Analogies between engineering
behavior of wastes (i.e., shear strength, compressibility, and
hydraulic conductivity) and soils have been commonly reported.
Therefore, similar dependence of temperature on waste properties is
expected as temperature-dependent tests on the engineering
properties of wastes have been reported in, for example, Lamothe,
D. & Edgers, L., "The Effects of Environmental Parameters on
the Laboratory Compression of Refuse," Proceedings of the 17th
International Madison Waste Conference, University of Wisconsin,
Madison, Wis., p. 592-604 (1994), which is hereby incorporated by
reference in its entirety. Accordingly, similar to the heat
generating properties discussed above, manipulation of the thermal
energy of waste mass 706 can also regulate the engineering behavior
of the waste mass.
[0079] In the foregoing specification, the invention has been
described with reference to specific embodiments thereof. It will,
however, be evident that various modifications and changes may be
made thereto without departing from the broader spirit and scope of
the invention. For example, the reader is to understand that the
specific ordering and combination of process actions described
herein is merely illustrative, and the invention may appropriately
be performed using different or additional process actions, or a
different combination or ordering of process actions. For example,
this invention is particularly suited for municipal solid waste
landfills; however, the invention can be used for an ash landfill,
chemical or industrial waste landfill, mining wastes, or any
organic degradation system. Additionally, and obviously, features
may be added or subtracted as desired. Accordingly, the invention
is not to be restricted except in light of the attached claims and
their equivalents.
* * * * *