U.S. patent application number 12/968318 was filed with the patent office on 2011-04-14 for cooling system with integral thermal energy storage.
Invention is credited to Ival O. Salyer.
Application Number | 20110083827 12/968318 |
Document ID | / |
Family ID | 43853896 |
Filed Date | 2011-04-14 |
United States Patent
Application |
20110083827 |
Kind Code |
A1 |
Salyer; Ival O. |
April 14, 2011 |
COOLING SYSTEM WITH INTEGRAL THERMAL ENERGY STORAGE
Abstract
A cooling system is provided which includes a primary heat
exchanger including heat exchange pipes filled with a phase change
material comprising water. The heat exchange pipes are in heat
transfer relation with a coolant fluid, which, upon cooling, is
transferred to a separate liquid to air heat exchanger for
conversion into cool air, for example, for use in air conditioning
or refrigeration.
Inventors: |
Salyer; Ival O.; (Flowery
Branch, GA) |
Family ID: |
43853896 |
Appl. No.: |
12/968318 |
Filed: |
December 15, 2010 |
Current U.S.
Class: |
165/104.14 ;
165/165 |
Current CPC
Class: |
F28D 2020/0021 20130101;
F28D 20/02 20130101; Y02E 60/147 20130101; Y02E 60/142 20130101;
F28D 20/0034 20130101; Y02E 60/14 20130101; F28D 15/00 20130101;
F24F 5/0021 20130101; Y02E 60/145 20130101 |
Class at
Publication: |
165/104.14 ;
165/165 |
International
Class: |
F28D 15/00 20060101
F28D015/00; F28D 7/00 20060101 F28D007/00 |
Claims
1. A residential and commercial cooling system comprising: 1) a
primary heat exchanger comprising: an outer shell; a plurality of
heat exchange pipes positioned in said shell, said pipes containing
a phase change material therein; at least one cooling element in
said shell; a coolant fluid in contact with said heat exchange
pipes; an inlet and an outlet for the transfer of said coolant
fluid to and from said primary heat exchanger; 2) a liquid to air
heat exchanger comprising: an inlet and outlet for the transfer of
said coolant fluid; and an inlet and outlet for the transfer of
air.
2. The cooling system of claim 1 including first and second cooling
elements positioned at the top and bottom of said primary heat
exchanger.
3. The cooling system of claim 1 wherein said phase change material
comprises water.
4. The cooling system of claim 3 wherein said phase change material
further comprises from about 1 to about 5% by weight polyvinyl
alcohol.
5. The cooling system of claim 1 wherein said phase change material
further comprises a water/urea phase change material comprising
from about 60 to 80% water and from about 20 to 40% by weight
urea.
6. The cooling system of claim 1 wherein said coolant fluid is
selected from the group consisting of ethylene glycol, propylene
glycol, and glycerine.
7. The cooling system of claim 1 further including insulation on
the exterior surface of said outer shell.
8. The cooling system of claim 7 wherein said insulation is vacuum
panel insulation having an R value of about 50 to 60 per inch of
thickness.
9. The cooling system of claim 1 wherein said heat exchange pipes
comprise a metal selected from copper, stainless steel, and
glass-coated steel.
10. The cooling system of claim 1 wherein said heat exchange pipes
have an outer diameter of from about 0.5 to about 2.5 inches.
11. The cooling system of claim 1 wherein each of said heat
exchange pipes include a cap at each end such that said phase
change material is sealed therein.
12. The cooling system of claim 1 having a rectangular
configuration.
13. The cooling system of claim 1 having a cubic configuration.
Description
BACKGROUND OF THE INVENTION
[0001] The present invention relates to a cooling system, and more
particularly, to a cooling system which utilizes phase change
materials for the storage and release of thermal energy.
[0002] It is known that a large amount of electric power is
consumed by the cooling of residual and commercial buildings,
especially during daylight hours. Overall, a large imbalance in
electric power usage exists during daylight hours, due primarily to
the amounts of power consumed by industry, businesses, and public
transportation. To compensate for the extensive day time use of
electric power, utility companies provide generating capacity
sufficient to supply day time usage, leaving unused capacity
available for the night hours.
[0003] A need has arisen in the art for a cooling system which can
provide more efficient cooling and which can make effective use of
energy during off-peak hours. Cooling units are known which utilize
phase change materials to provide more effective cooling. A cooling
unit utilizing a phase change material is described in my U.S. Pat.
No. 5,765,389. The cooling unit includes heat exchange conduits
including a coolant fluid therein which are positioned in heat
transfer relationship with a phase change material such as a melt
mix polymer or linear crystalline alkyl hydrocarbons.
[0004] However, there is a need for an improved cooling system
which can reduce commercial and residential energy costs through
the use of more effective phase change materials.
SUMMARY OF THE INVENTION
[0005] Embodiments of the invention meet that need by providing a
residential and commercial cooling system such as an air
conditioning unit which provides cooling by using a phase change
material contained in a plurality of heat exchange pipes which are
in heat transfer relation with a coolant fluid.
[0006] According to one aspect, a residential and commercial
cooling system is provided which comprises a primary heat exchanger
comprising an outer shell, and a plurality of heat exchange pipes
positioned in the shell, where the pipes contain a phase change
material therein. The system further includes at least one cooling
element in the shell. Preferably, the cooling system includes first
and second cooling elements positioned at the top and bottom of the
primary heat exchanger.
[0007] The cooling system further includes a coolant fluid in
contact with the heat exchange pipes, and an inlet and an outlet
for the transfer of the coolant fluid to and from the heat
exchanger.
[0008] The system further includes a separate liquid to air heat
exchanger including an inlet and outlet for the transfer of coolant
fluid to and from the liquid to air heat exchanger; and an inlet
and outlet for the transfer of air to and from the liquid to air
heat exchanger.
[0009] In one embodiment, the phase change material comprises
water/ice. The phase change material may further comprise from
about 1 to about 5% by weight polyvinyl alcohol.
[0010] In an alternative embodiment, the phase change material
comprises a water/urea phase change material comprising from about
60 to 80% by weight water and from about 20 to 40% by weight
urea.
[0011] The coolant fluid for use in the system is selected from the
group consisting of ethylene glycol, propylene glycol, and
glycerine. The coolant fluid is contained in the cavity of the
shell such that it comes into contact with the heat exchange pipes
filled with phase change material.
[0012] The heat exchange pipes comprise a metal selected from
copper, stainless steel, and glass-coated steel. The heat exchange
pipes have an outer diameter of from about 0.5 to about 2.5 inches,
and include a closure such as a cap at each end such that the phase
change material is sealed therein.
[0013] The cooling system preferably has a three-dimensional
rectangular or cubic configuration with generally flat sides. A
layer of insulation may be included on the exterior surface of the
shell. The insulation is preferably vacuum panel insulation having
an R value of about 50 to 60 per inch of thickness.
[0014] The coolant fluid is cooled by the cooling element(s) which
may be filled with a refrigerant such as freon. The cooling system
is preferably operated so that the coolant fluid (and the phase
change material) is cooled from the bottom up. As the coolant is
cooled, cooling of the phase change material is accomplished via
direct contact of the coolant fluid with the metal heat exchange
pipes containing the phase change material contained therein. When
the cooling system is not in use, energy stored in the phase change
material is transferred back to the coolant fluid such that the
temperature of the fluid lowers and may be transferred out from the
heat exchanger to the separate liquid to air heat exchanger
positioned externally from the primary heat exchanger, where the
coolant fluid will be used to cool air, for example, for air
conditioning. Alternatively, the cooled coolant fluid could be used
in a refrigeration unit.
[0015] In one embodiment, the cooling system may include a solenoid
valve in conjunction with the inlet or outlet to provide pulsatile
flow of the coolant fluid and improve cold transfer.
[0016] Accordingly, it is a feature of the invention to provide a
cooling system which employs a primary heat exchanger comprising a
plurality of heat exchange pipes including a phase change material
therein. These, and other features and advantages of the invention,
will become apparent from the following drawings, detailed
description and claims.
BRIEF DESCRIPTION OF THE DRAWINGS
[0017] FIG. 1A is a partial cross-sectional view of one embodiment
of the cooling unit;
[0018] FIG. 1B is a top view of embodiment of the cooling unit
shown in FIG. 1A; and
[0019] FIG. 2 is a perspective view of a single heat exchange pipe
including a phase change material therein.
DETAILED DESCRIPTION OF THE INVENTION
[0020] Embodiments of the cooling system use water as a phase
change material where the water in liquid form provides sensible
heat and the water/ice combination provides a latent heat of about
80 calories per gram. Water provides advantages over the use of
other conventional phase change materials such as linear
crystalline alkyl hydrocarbons as it has a higher latent heat and
higher sensible heat, is much lower in cost, and is readily
available.
[0021] Referring now to FIGS. 1A and 1B, one embodiment of the
cooling system 10 is shown. As shown in FIG. 1A, the cooling system
10 comprises a shell 12 including a primary heat exchanger 14
therein which comprises a plurality of heat exchange pipes 16
including a phase change material 18 therein. The heat exchanger 14
is used in conjunction with a separate liquid to air heat exchanger
32 which is capable of supplying the cooling requirements of a
residential home.
[0022] The shell 12 is preferably rectangular or cubic in
configuration and should be of a sufficient height to be able to
accommodate up to about 75 gallons of coolant fluid. The shell 12
may be comprised of copper, stainless steel, or glass-coated steel.
It should be appreciated that the shell and the heat exchange pipes
should comprise the same material. For example, if the heat
exchange pipes comprise stainless steel, the shell should also be
comprised of stainless steel to provide optimum heat transfer and
to avoid creating a battery effect between the two metals in
solution.
[0023] As shown, the shell 12 has a flat exterior surface 20 which
is surrounded by an insulation material 22. The insulation material
22 preferably covers substantially the entire exposed exterior
surface 20 of shell 12. Preferably, the insulation material 22 has
an "R" value of at least about 50 to 60 per inch. Vacuum panel
insulation suitable for use includes vacuum panel insulation
available from AcuTemp under the designation ThermoCor.RTM.. The
coolant fluid is supplied to the shell during manufacture of the
heat exchanger and is filled close to the top of the shell as
indicated by fluid level 48 as shown in FIG. 1A. As the shell is a
closed unit, there is no need to add additional coolant fluid.
[0024] Suitable coolant fluids for use in the cooling unit include
ethylene glycol, propylene glycol, and glycerine, which are
preferably mixed with water. A preferred coolant fluid is a mixture
of ethylene glycol and water in approximately equal amounts.
[0025] An outlet line 26 allows cooled fluid to flow from the heat
exchanger 14 to a separate heat exchanger 32 for conversion to
cooled air as will be explained in further detail below. If
desired, the outlet line 26 may include a programmable solenoid
valve 50 as shown. The solenoid valve may be partially closed at
regular intervals to provide pulsatile flow of coolant fluid to
improve cold transfer. The solenoid valve can be programmed to vary
both the amplitude and frequency in which the valve is partially
closed to provide the desired pressure drop. Variations of
frequency from 5 to 60 cycles per minute, and more preferably, from
about 15 to 30 cycles per minute are desirable. The valve closure
is preferably regulated so as to create a pressure drop of at least
5 psi, and preferably up to about 50% of the available fluid
pressure.
[0026] The cooling unit 10 further includes cooling elements
comprising coils 28 and 30 positioned at the top and bottom
portions of the shell. The cooling coils 28, 30 preferably contain
a refrigerant therein such as freon or fluorocarbon gas. These
materials are preferably selected to have a boiling point which is
desirable to initiate freezing of the phase change material. In
operation, evaporation and cooling of the refrigerant material
takes place in the cooling coils similar to a freon type
refrigeration or air conditioning system. The cooling unit further
includes a compressor 34 positioned externally from the heat
exchanger 14 which includes a condenser for returning the freon to
liquid form for reuse as in a conventional refrigeration unit. The
freon or other refrigerant is pumped through the cooling coils. As
the refrigerant evaporates, it cools the coil, which then cools the
coolant fluid in the primary heat exchanger. The evaporated coolant
gas is then returned to the compressor, where the gas is converted
to a liquid which is directed to the coils in the primary heat
exchanger 14.
[0027] The cooling unit 10 may also include a timer (not shown)
connected to a power supply (not shown) to control the power usage
of the heat exchanger during designated time periods, e.g. turning
off the power supply during peak power usage hours, thus reducing
energy costs. Suitable power sources include photovoltaic or wind
chargers.
[0028] The heat exchanger 14 further includes a plurality of heat
exchange pipes 16 including the phase change material 18 therein.
As shown, the heat exchange pipes 16 are positioned vertically in
the heat exchanger. The heat exchange pipes are preferably
configured in the shell as shown in the top view of the water
heater depicted in FIG. 1B and are preferably held in position by a
perforated metal screen (not shown) with holes therein which fit
around the heat exchange pipes to hold them together as a unit.
[0029] Prior to being filled with the phase change material, the
pipes are hollow and are comprised of a heat conducting material.
The heat exchange pipes include a cap at each end for sealing the
phase change material, which will be described in more detail
below. While the pipes and phase change material are shown in
cylindrical form, it should be appreciated that both the pipes and
phase change material may also vary in shape. For example, the
pipes and corresponding phase change material may be square or
rectangular in shape.
[0030] A preferred phase change material for use in embodiments of
the invention is water, which has a melting/freezing temperature of
0.degree. C. and a latent heat capacity of 80 calories/gram.
Preferred for use in the invention is pure water obtained by
distillation or reverse osmosis.
[0031] Another suitable phase change material is a water/urea
mixture having a melting/freezing temperature of about -12.degree.
C. and a latent heat capacity of about 70 calories/gram. Such a
water/urea mixture preferably comprises about 70% water and 30% by
weight urea. In this embodiment, a lower temperature refrigerant
would be required for use in the coolant coils to freeze the phase
change material. Suitable lower temperature refrigerant materials
include Freon materials having varied fluorine contents and
molecular weights, such as, for example, Freon.RTM. 22 commercially
available from Dupont.
[0032] Upon melting and freezing, the phase change material absorbs
and releases a large quantity of energy in the vicinity of its
melting/freezing point. The phase change materials may be
repeatedly converted between solid and liquid phases to utilize
their latent heats of fusion to absorb, store, and release heat
during the phase conversions at about 0.degree. C. for pure water
or about -12.degree. C. for water/urea mixtures.
[0033] The phase change material may further include from about 1
to 5% by weight of a polymeric thickening agent such as polyvinyl
alcohol which raises the viscosity of the water phase change
material, reducing the likelihood of leakage of water during the
multiple cycles of melting and freezing that take place during
operation of the cooling unit.
[0034] The phase change material may further include nucleating
agents such as silicon dioxide dry powders or silver iodide. Such
agents may be included in amounts of about 1 to 10% by weight
silicon dioxide or about 0.05 to 0.5% by weight silver iodide to
prevent super cooling in the system.
[0035] Referring now to FIG. 2, a single heat exchange pipe 16 for
containment of the phase change material 18 is shown which is
initially hollow in form and may be formed from metals including,
but not limited to, stainless steel, copper, and glass-coated
steel. The outer diameter of the pipes may range from about 0.5 to
2.5 inches, more preferably, about 1 to 2 inches, and most
preferably about 1.5 inches. The wall thickness of the pipe should
be sufficient to withstand normal pressures during operation and is
preferably from about 0.030 to 0.125 inches, and more preferably,
about 0.060 inches. The pipes 16 are preferably provided in lengths
of about 27 inches, while the phase change material 18, once placed
into the pipes, is about 24 inches in height, which allows at least
about 3 to 4 inches of empty space in the pipe for expansion of the
phase change material when it freezes.
[0036] Prior to providing the phase change material 18 in the pipe,
an end cap 40 is applied to one end of the pipe and adhered thereto
by a high temperature thermosetting adhesive, by providing mating
threads on the pipe and cap, or by soldering (where copper pipes
are used).
[0037] The open end of the empty pipe 16 is then filled with a
source of inert gas such as nitrogen or argon such that most of the
oxygen in the pipe is purged. The phase change material is then
poured into the pipe sealed at the bottom with cap 40 such that the
water level is about 4 inches below the top of the pipe. A second
end cap 42 is then placed over the open end of the pipe 16 and
secured thereto in a conventional manner as described above. The
second end cap 42 includes a hole 44 which has been drilled in the
center of the cap which allows residual gas inside the heat
exchange pipe to be vented as the phase change material freezes and
expands for the first time. This avoids the buildup of high
pressure from the expansion of the phase change material which
could potentially cause swelling and/or rupture of the pipes.
[0038] The initial freezing and expansion of the phase change
material should take place prior to final assembly of the cooling
system, i.e., prior to placing the heat exchanger inside the shell.
After the venting process, the cap 42 is then permanently sealed.
The cap may be sealed with a threaded metal screw comprised of the
same metal as the pipe, by the use of a high temperature
thermosetting adhesive or by soldering (where copper pipes are
used).
[0039] The filled heat exchange pipes are then assembled in a
compact configuration consisting of approximately 24 rows with
about 24 heat exchange pipes in each row (arranged in a rectangular
or square configuration). A perforated metal screen 36 having
openings to accommodate the pipes may be used at the top and bottom
of the pipes to maintain them in proper position. A thin metal
strip may also be attached to the bundle of pipes to keep the pipes
in place. The bundle of pipes including the phase change material
therein is then inserted into the shell of the cooling unit.
[0040] The coolant fluid contained in the cavity of the heat
exchanger provides a fluid transfer medium which comes into contact
with the water-filled heat exchange pipes for cooling. The water
phase change material is in direct heat transfer contact with the
inner surfaces of heat exchange pipes 16 so that, during operation,
as the coolant fluid surrounds the heat exchange pipes, heat can be
transferred from the phase change material 18 to the coolant fluid
and vice versa.
[0041] The thermal energy supplied from the cooling system is
delivered on a plateau of nearly constant temperature until the
latent heat capacity is exhausted and electric power is supplied.
If desired, lower cost off-peak electricity or a green source of
energy such as solar photovoltaic or wind driven devices can be
used to supply the energy required to "charge" the phase change
material, resulting in significant cost savings for consumers.
[0042] Referring again to FIG. 1A, the cooling system 10 operates
in the following manner. The cooling coils 28 and 30 positioned at
the top and bottom portions of the shell include a refrigerant
material therein such as freon which is supplied from compressor
34. The temperature of the refrigerant material is controlled by a
thermostatic valve (not shown) which controls the rate of coolant
flowing through the top and bottom coils such that a desired
temperature differential is maintained between the two coils and to
allow freezing of the phase change material from the bottom up. By
freezing the phase change material from the bottom up, the phase
change material can expand into the empty space at the top of the
heat exchange pipe without a build-up of pressure.
[0043] As the coolant fluid in the cooling system 10 is cooled by
the cooling coils (via evaporation of refrigerants in the coils),
energy from the coolant fluid is transferred from the metal heat
exchange pipes 16 to the water phase change material 18 contained
therein, which begins to freeze. Once the water reaches the
freezing point (0.degree. C.), the ice continues to cool the system
until heat is added to the system at which point the coolant fluid
becomes warmer than the (ice) phase change material and a melt
cycle begins.
[0044] Thus, when the cooling unit 10 is not in operation, e.g.,
during peak times of power usage, the phase change material in the
heat exchanger 14 cools the coolant fluid, i.e., heat energy from
the coolant fluid is transferred to the phase change material which
lowers the temperature of the coolant fluid.
[0045] The cooled coolant fluid is then transferred from the
primary heat exchanger 14 to the liquid to air heat exchanger 32
via outlet line 26. The heat exchanger 32 is a conventional liquid
to air heat exchanger and includes a return line 66 for the return
of coolant fluid to the heat exchanger. The liquid to air heat
exchanger 32 further includes a warm air inlet 68 and cold air
outlet 70. As cooled coolant fluid enters the liquid to air heat
exchanger 32, air entering the heat exchanger 32 is cooled by
transport over the cooled pipes of the heat exchanger 32 such that
the temperature of the air is reduced. The rate of heat transfer
depends on the rate of air flow, the surface area of the pipe, and
temperature differentials. The cool air then exits through air
outlet 70.
[0046] While certain representative embodiments and details have
been shown for purposes of illustrating the invention, it will be
apparent to those skilled in the art that various changes in the
compositions and apparatus disclosed herein may be made without
departing from the scope of the invention, which is defined in the
appended claims.
* * * * *