U.S. patent application number 12/342252 was filed with the patent office on 2009-07-02 for energy control system.
This patent application is currently assigned to JOHNSON CONTROLS TECHNOLOGY COMPANY. Invention is credited to Gregory Ralph HARROD, Jeffrey Norris NICHOLS.
Application Number | 20090171862 12/342252 |
Document ID | / |
Family ID | 40799709 |
Filed Date | 2009-07-02 |
United States Patent
Application |
20090171862 |
Kind Code |
A1 |
HARROD; Gregory Ralph ; et
al. |
July 2, 2009 |
ENERGY CONTROL SYSTEM
Abstract
A method for adjusting an economic balance point in a dual fuel
HVAC system includes a furnace, a heat pump and a control system.
The method comprises providing a control device having a
preprogrammed algorithm for controlling the HVAC system, providing
a communication path between the control device and at least one
component of the HVAC system, and accessing current fuel cost data;
determining an economic balance point temperature based on the
current fuel cost data; and updating the economic balance point
temperature in the preprogrammed algorithm to adjust an actual
balance point of the HVAC system.
Inventors: |
HARROD; Gregory Ralph;
(Wichita, KS) ; NICHOLS; Jeffrey Norris; (Wichita,
KS) |
Correspondence
Address: |
MCNEES WALLACE & NURICK LLC
100 PINE STREET, P.O. BOX 1166
HARRISBURG
PA
17108-1166
US
|
Assignee: |
JOHNSON CONTROLS TECHNOLOGY
COMPANY
Holland
MI
|
Family ID: |
40799709 |
Appl. No.: |
12/342252 |
Filed: |
December 23, 2008 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
|
|
61017383 |
Dec 28, 2007 |
|
|
|
Current U.S.
Class: |
705/412 ;
700/278; 700/300; 707/999.01 |
Current CPC
Class: |
F24F 11/30 20180101;
F24F 2110/12 20180101; F24F 11/47 20180101; A01C 5/062 20130101;
G06Q 50/06 20130101; A01C 5/066 20130101; F24F 2221/34
20130101 |
Class at
Publication: |
705/412 ;
700/278; 700/300; 707/10 |
International
Class: |
G06Q 10/00 20060101
G06Q010/00; G05D 23/19 20060101 G05D023/19; G06F 17/30 20060101
G06F017/30 |
Claims
1. A method for adjusting a balance point temperature in a dual
fuel HVAC system having a furnace, a heat pump and a control
system, by monitoring operating costs for the furnace and the heat
pump, the method comprising: accessing fuel cost data; determining
a balance point temperature based on the fuel cost data; and
updating the balance point temperature in a preprogrammed algorithm
to adjust a balance setpoint of the HVAC system, the balance
setpoint being the exterior temperature below which the HVAC system
switches from the heat pump to the furnace as a heat source.
2. The method of claim 1, also comprising: sensing an exterior
temperature; and controlling an interior temperature by operating
the furnace when the exterior temperature is less than the balance
setpoint, and by operating the heat pump when the exterior
temperature is greater than or equal to the balance setpoint.
3. The method of claim 1, also including the steps of: determining
at least one predetermined parameter of the heat pump at a
plurality of exterior temperatures.
4. The method of claim 3, further comprising: continually
determining the at least one predetermined parameter and
incorporating the at least one predetermined parameter into an
algorithm to calculate an application balance point temperature,
below which the heat pump heating capacity is less than the rate of
heat loss of structure, in response to a change in the at least one
predetermined parameter.
5. The method of claim 4, wherein the at least one predetermined
parameter includes heating capacity, energy consumption, or
efficiency.
6. The method of claim 1, wherein the control system comprises a
microprocessor-based electronic controller configured to implement
the algorithm, receive input values and generate output
signals.
7. The method of claim 1, wherein the HVAC system comprises a
plurality of system components, the system components comprising a
heat pump controller, a furnace controller, a room thermostat, an
independent control panel, and a personal computer; the system
components in data communication with one another through a
network.
8. The method of claim 7, wherein the algorithm may be
preprogrammed into at least one of the system components.
9. The method of claim 1, wherein system components are connected
through thermostat wires, and one of the system components receives
the data to process the algorithm.
10. The method of claim 1, wherein the control system is connected
to a network having an Internet connection.
11. The method of claim 1, wherein the HVAC system is in electronic
communication with a network that may be connected through a
network coupling device.
12. An HVAC system comprising: a furnace, a heat pump, a
controller, and a communication path between the controller and at
least one component of the HVAC system; wherein the controller is
configured to access a remote database including a current fuel
cost data and retrieve the current fuel cost data, determine a
balance point temperature based on the current fuel cost data, and
update a balance point temperature in a preprogrammed algorithm to
adjust a balance setpoint of the HVAC system.
13. The HVAC system of claim 12, wherein the controller is
configured to determine at least one predetermined parameter of the
heat pump at a plurality of exterior temperatures.
14. The HVAC system of claim 13, wherein the preprogrammed
algorithm is configured to periodically determine at predetermined
intervals the at least one predetermined parameter and calculate an
application balance point exterior temperature, below which
exterior temperature the heat pump heating capacity is less than
the rate of heat loss of structure, in response to a change in the
at least one predetermined parameter.
15. A method for controlling energy use in a structure, the
structure including a dual fuel HVAC system having a furnace, a
heat pump and a control system, comprising: selecting an indoor
temperature setpoint, a heat loss for the structure, and a heating
capacity of the system determining an application balance point
exterior temperature below which the heat pump heating capacity is
less than the rate of heat loss of the structure, based on one or
more of the selected indoor temperature, the heat loss for the
structure, and the heating capacity of the system; determining an
operating cost of the furnace; determining an operating cost for
the heat pump; determining a balance point temperature based on a
point of intersection of the heat pump operating costs and the
furnace operating cost; comparing the application balance point
temperature to a balance point temperature and generating a balance
setpoint, the balance setpoint being selected as the greater value
of the application balance point temperature and the balance point
temperature; and monitoring system parameters periodically to
determine whether a change in the balance setpoint has occurred as
a result of changes in system parameters.
16. The method of claim 15, wherein the step of determining the
operating cost for the heat pump comprises: determining the
electric power consumption of the heat pump, determining the cost
of electricity, calculating heat pump energy cost for the heat
pump;
17. The method of claim 15, further comprising: controlling the
system to operate the heat pump based on the exterior temperature
equaling or exceeding the balance setpoint, and to operate the
furnace based on the exterior temperature being less than the
balance setpoint.
18. The method of claim 15, further comprising: determining that a
current balance setpoint value differs from a preceding balance
setpoint and replacing the balance setpoint with the current
balance setpoint.
19. The method of claim 15, further comprising: determining the
heat loss based on a design heat loss of a structure at a
predetermined outdoor temperature
20. The method of claim 15, wherein the heating capacity of the
heat pump is determined by plotting a curve of the heating capacity
of the heat pump for a range of exterior temperatures.
21. The method of claim 20, wherein the balance point temperature
is determined by an intersection of a heat pump electrical
consumption cost curve and a furnace heating cost curve.
22. The method of claim 21, wherein the application balance point
is defined as an intersection of a heat loss curve of the structure
and a heating capacity curve of the heat pump.
Description
CROSS-REFERENCE TO RELATED APPLICATIONS
[0001] This application claims priority from and the benefit of
U.S. Provisional Application No. 61/017,383 entitled METHOD AND
APPARATUS FOR DYNAMIC BALANCE POINT SELECTION, filed Dec. 28, 2007,
which is hereby incorporated by reference.
BACKGROUND
[0002] The application generally relates to control systems for
heating ventilation and air conditioning (HVAC) systems. The
application relates more specifically to a method and apparatus to
dynamically determine a balance point of an HVAC system having a
heat pump and a fossil fuel furnace.
[0003] The balance point of an HVAC system determines whether the
heat pump or fossil fuel furnace is to be used for heating. Static
balance point settings can be primarily based on exterior
temperature readings, and on the existing utility rates at the time
of the HVAC system installation.
[0004] Heat pumps may be installed with indoor air handlers having
electric resistance heating elements as the auxiliary or
supplemental heating source. However, the rising cost of
electricity is causing more HVAC systems to be installed with a
heat pump as the primary heating source and a fossil fuel furnace
as the auxiliary heating source.
[0005] In existing air handler/electric heater installations, the
evaporator coil is located in the airflow path before the electric
resistance heating elements. However, in a fossil fuel furnace
installation, the evaporator coil is located in the airflow path
after the furnace heating section. Therefore, the furnace is not
permitted to produce heat while the heat pump is also providing
heat, because the heat produced by the furnace heating section
would be transferred into the refrigerant through the indoor coil,
causing the refrigerant pressure to increase. Adding more heat to
the refrigerant may cause the refrigerant pressure to exceed a
high-pressure limit of the system.
[0006] Current methods employ a balance point setting that is
static. By static, what is meant is that once the balance point is
calculated by the installer and applied to the system, the balance
point is not updated during the life of the HVAC system, or the
balance point is updated infrequently such as during service or
maintenance calls. However, the cost of fossil fuel and electricity
changes continuously. Therefore, the balance point setting does not
necessarily reflect an optimized balance between fuel sources.
Previous heat pump/fossil fuel HVAC systems include some means for
setting the balance point for the system. This setting can be made
with an accessory kit or fossil fuel kit, which includes an
exterior thermostat. The control system electromechanical devices
or electronic control board of the heat pump may also include
means, such as a shunt jumper or DIP switch, for setting the
balance point. Indoor room thermostats are now available with a
balance point setting. In all of these methods for setting the
balance point, a control device determines the exterior ambient
temperature, compares the exterior ambient temperature with the
balance point setting, and determines whether to operate the heat
pump or the furnace. Other methods use room thermostats to control
the switching between heat pump and furnace without monitoring
exterior temperature.
SUMMARY
[0007] One embodiment relates to a method for adjusting a balance
point temperature in a dual fuel HVAC system having a furnace, a
heat pump and a control system, by monitoring operating costs for
the furnace and the heat pump. The method includes accessing fuel
cost data; determining a balance point temperature based on the
fuel cost data; and updating the balance point temperature in a
preprogrammed algorithm to adjust a balance setpoint of the HVAC
system, the balance setpoint being the exterior temperature below
which the HVAC system switches from the heat pump to the furnace as
a heat source.
[0008] Another embodiment relates to an HVAC system comprising a
furnace, a heat pump, a controller, and a communication path
between the controller and at least one of the furnace and the heat
pump. The controller is configured to access a remote database
including a current fuel cost data and retrieve the current fuel
cost data, determine a balance point temperature based on the
current fuel cost data, and update a balance point temperature in a
preprogrammed algorithm to adjust a balance setpoint of the HVAC
system.
[0009] Another embodiment relates to a method for controlling
energy use in a structure, the structure including a dual fuel HVAC
system having a furnace, a heat pump and a control system. The
method includes selecting an indoor temperature setpoint, a heat
loss for the structure, and a heating capacity of the system;
determining an application balance point exterior temperature below
which the heat pump heating capacity is less than the rate of heat
loss of structure, based on one or more of the selected indoor
temperature, the heat loss for the structure, and the heating
capacity of the system; determining an operating cost of the
furnace; determining an operating cost for the heat pump;
determining a balance point temperature based on a point of
intersection of the heat pump operating costs and the furnace
operating cost; comparing the application balance point temperature
to a balance point temperature and generating a balance setpoint,
the balance setpoint being selected as the greater value of the
application balance point temperature and the balance point
temperature; and monitoring system parameters periodically to
determine whether a change in the balance setpoint has occurred as
a result of changes in system parameters.
[0010] Embodiments disclosed herein provide an ability to determine
a balance point that is based on current utility rates and to
determine an optimal balance point based on a user preferred input
and multiple sensor data, and to control a source of heat from one
of a fossil fuel furnace and a heat pump.
BRIEF DESCRIPTION OF THE FIGURES
[0011] FIG. 1 illustrates an exemplary embodiment of an HVAC system
for a typical residential structure.
[0012] FIG. 2 illustrates schematically an exemplary embodiment of
a vapor compression system.
[0013] FIG. 3 illustrates schematically another exemplary
embodiment of a vapor compression system.
[0014] FIG. 4 is a graph illustrating design heat loss of an
exemplary structure as a function of outdoor temperature.
[0015] FIG. 5 is a flow chart of an exemplary process for
determining an application balance point for an exemplary
structure.
[0016] FIG. 6 is a graph illustrating an exemplary heat pump
electrical consumption curve and an exemplary furnace heating cost
curve.
[0017] FIG. 7 is a graph illustrating a shift in the economic
balance point shown in FIG. 6 due to changing characteristics of
the furnace or heat pump.
[0018] FIG. 8 shows an alternate embodiment of a heating capacity
curve representing a heating capacity of and HVAC system operating
the heat pump at less than maximum capacity
[0019] FIG. 9 discloses an exemplary embodiment of a logic process
to continually or periodically monitor system parameters
DETAILED DESCRIPTION OF THE EXEMPLARY EMBODIMENTS
[0020] Referring to FIG. 1, an exemplary environment for an HVAC
system 10 for a residential setting is shown. HVAC system 10 may
include an exterior unit 38 located outside of a structure 44 and
an interior unit 50 located inside structure 44. Outdoor unit 38
may include a fan 40 that circulates air across coils 42 to
exchange heat with refrigerant in coils 42 before the refrigerant
enters structure 44 through lines 46. A compressor 48 may also be
located in outdoor or exterior unit 38. Indoor unit 50 may include
a heat exchanger 52 to provide cooling or heating to structure 44
depending on the operation of HVAC system 10. Indoor unit 50 may be
located in a basement 54 of structure 44 or interior unit 50 may be
disposed in any other suitable location such as in a first floor
closet or in an attic (not shown) of structure 44. HVAC system 10
may include a blower 56 and air ducts 58 to distribute the
conditioned air (either heated or cooled) through structure 44. A
thermostat (not shown) or other control may be used to control and
operate HVAC system 10.
[0021] Referring next to FIGS. 2 and 3, a vapor compression system
20 includes a compressor 62, a condenser 64, and an evaporator 66
(FIG. 2) or a compressor 62, a reversing valve 150, an indoor unit
50 and an exterior unit 38 (FIG. 3). System 20 can be operated as
an air conditioning only system, where the evaporator 66 is located
indoors, that is, as interior unit 50, to provide cooling to the
interior air and condenser 64 is located exteriors, that is, as
exterior unit 38, to discharge heat to the exterior air. System 20
can be operated as a heat pump with the inclusion of the reversing
valve 150 to control and direct the flow of refrigerant from
compressor 62. When system 20 is operated as a heat pump in an air
conditioning mode, the reversing valve 150 is controlled for
refrigerant flow as described with respect to FIG. 2. However, when
system 20 is operated as a heat pump in heating mode, the flow of
refrigerant is in the opposite direction from the air conditioning
mode and condenser 64 is located indoors, that is, in interior unit
50, to provide heating of the indoor air and the evaporator 66 is
preferably located outdoors, that is, as exterior unit 38, to
absorb heat from the exterior air.
[0022] Compressor 62 compresses a refrigerant vapor and delivers
the refrigerant vapor to condenser 64 through a discharge line 60,
and the reversing valve 150 if operated as a heat pump. Compressor
62 can be a rotary compressor, screw compressor, reciprocating
compressor, centrifugal compressor, swing link compressor, scroll
compressor, turbine compressor, or any other suitable type of
compressor. Refrigerant vapor is delivered by compressor 62 to
condenser 64 and enters into a heat exchange relationship with a
fluid, for example, air or water, and undergoes a phase change to a
refrigerant liquid as a result of the heat exchange relationship
with the fluid. Condensed liquid refrigerant from condenser 64
flows through an expansion device 65 to evaporator 66.
[0023] Condensed liquid refrigerant delivered to evaporator 66
enters into a heat exchange relationship with a fluid, for example,
air or water, and undergoes a phase change to a refrigerant vapor
as a result of the heat exchange relationship with the fluid. Vapor
refrigerant exits evaporator 66 and returns to compressor 62 by a
suction line to complete the cycle, and reversing valve 150 if
operated as a heat pump.
[0024] Compressor 62 of system 20, whether operated as a heat pump
or as an air conditioner, is driven by a motor 70. Motor 70 can be
powered by a variable speed drive (VSD) or can be powered directly
from an AC or DC power source. A VSD, if used, receives AC power
having a particular fixed line voltage and fixed line frequency
from AC power source and provides power to the motor 70. The motor
70 used in system 20 can be any suitable type of motor that can be
powered by a VSD or directly from an AC or DC power source, for
example, a switched reluctance (SR) motor, an induction motor, an
electronically commutated permanent magnet motor (ECM).
[0025] For an HVAC system incorporating a heat pump and a fossil
fuel furnace a determination is first made regarding the conditions
that can cause the heat pump to operate, and the conditions that
can cause the furnace to operate. The determination is made through
a predetermined balance point setting. The balance point is defined
by an exterior air temperature below which only the fossil fuel
furnace can operate, and above which only the heat pump can
operate. To determine the applicable balance point, a heat loss
calculation is made of the residence or structure 44.
[0026] The application balance point as defined herein refers to
the exterior temperature below which the heat pump heating capacity
is less than the rate of heat loss of structure 44. When the
exterior temperature is below the application balance point,
structure 44 loses heat faster than system 10 can generate heat in
heat pump mode, and the interior air temperature of structure 44
will decrease even when system 10 is operating at its full
capacity. Traditionally, the heat loss of structure 44 is assumed
to be linear and inversely proportional to the exterior
temperature. A graphic representation of the heat loss (see FIG. 4)
is a line created by connecting a point at a selected exterior
temperature and a predetermined interior comfort temperature, for
example, 70.degree. F. The exterior design temperature depends on
multiple factors, for example, residence structure type and
location. At the predetermined interior comfort temperature, the
exterior temperature and the interior temperature are identical.
Therefore, there is no heat transfer between structure 44 and the
exteriors. Thus, when the exterior temperature and the interior
temperature equal the interior comfort temperature, HVAC system 10
does not require heating or cooling of the structure. Each
structure or structure 44 has an associated heat loss curve that is
determined as a part of the installation process.
[0027] System 20 heating capacity and energy consumption at various
exterior temperatures may be determined during testing and
development of a particular heat pump model or system. System 20
heating capacity decreases as the ambient temperature decreases.
The system heating capacity curve is presumed to be linear and is
determined based on the heating capacity of system 20 at two
standard testing temperatures, 17.degree. F. and 47.degree. F. (see
FIG. 4). The linear extrapolation for determining system 20 heating
capacity for exterior temperatures other than the standard testing
temperatures is adequate for calculating the balance point in most
situations. However, the actual heating capacity curve of a heat
pump may be nonlinear and thus may be represented by other methods,
for example, by determining data at additional temperature points.
Alternately, the actual heating capacity curve of heat pump or
system 20 may be determined by representing the heating capacity of
the heat pump system 20 using a mathematical model or equation.
Each mathematical model of heat pump system 20 may be characterized
by a heating capacity curve that is determined and documented
during the development of the heat pump system.
[0028] At exterior temperatures above the application balance
point, system 20 can produce more heat than is needed to maintain
the interior temperature of structure 44. At exterior temperatures
below the application balance point, system 20 cannot produce
sufficient heat to maintain the temperature of structure 44 at a
desired temperature setpoint, and the temperature within structure
44 will fall or be maintained below the desired setpoint, even
though system 20 is operating at or near full capacity.
[0029] Referring to FIG. 4, a design heat loss for an exemplary
structure 44 is depicted by a line 101. The exterior design
temperature in this example is a point 105 which shows an exterior
design temperature of minus 10.degree. F. (degrees Fahrenheit), at
which structure 44 exhibits a heat loss of 40 million British
Thermal Units per hour (MBTUH). The interior comfort temperature is
represented by a point 106 which exhibits a heat loss of 0 MBTUH at
70.degree. F. System 20 heating capacity is represented by line
102. In FIG. 4, line 102 is a straight line defined by connecting
of test data points 103 and 104. Point 104 represents the heating
capacity of system 20 when the exterior temperature is at or about
17.degree. F. and point 103 represents the heating capacity of
system 20 when the exterior temperature is at or about 47.degree.
F. An intersection point 100 depicts an application balance point
of 22.degree. F. for this exemplary system.
[0030] Referring next to FIG. 5, a flow diagram describes an
exemplary process for determining an application balance point.
First, at step 120, the design heat loss is determined. For
example, in FIG. 4, the design heat loss is indicated by point 105,
as being approximately 40 MBTUH at minus 10.degree. F. At step 122,
interior comfort setpoint 106 (FIG. 4) is determined, for example,
0 British Thermal Units per hour (BTUH) at 70.degree. F. Next at
step 124, heat loss is determined for structure 44, by line 101
connecting interior comfort setpoint 106 and design heat loss 105.
At step 126, heating capacity of system 10 is determined and
plotted as a curve 102 (FIG. 4). At step 128, the application
balance point 100 is determined by the intersection of line 102 and
line 101.
[0031] An economic balance point 201 (FIG. 6) is separately
determined in FIG. 5, beginning at step 132, by determining an
Annual Fuel Utilization Efficiency (AFUE) for the furnace. The
system 10 proceeds to step 134 and step 136 to determine fuel cost,
and optionally, any unit conversions that may be required, for
example, Therm to MBTUH. At step 138, the furnace energy or
operating cost is plotted in dollars as a function of AFUE, fuel
cost and any required unit conversions.
[0032] At step 142, system 10 determines the electric power
consumption of the heat pump, for example, by a map or profile of
the heat pump. At step 144, system 10 determines the cost of
electricity, and at step 146 calculates the heat output per unit of
electricity, for example, MBTUH per KW. Next, at step 148, the
system calculates heat pump energy cost, or operating cost, for the
particular heat pump used, at multiple exterior temperatures.
[0033] Next, at step 140 system 10 determines economic balance
point 201 as the intersection of heat pump operating costs plotted
in step 148 and furnace operating cost plotted in step 138.
[0034] At step 130, system 10 compares application balance point
100, determined in step 128, with economic balance point 201,
determined in step 140, and generates a balance setpoint, or actual
balance point 100, which is the higher value of application balance
point 100 and application balance point 100, at step 152
[0035] Economic balance point 201 (see FIG. 6) is defined as the
exterior temperature below which it is more economical to operate
the fossil fuel furnace than it is to operate the heat pump.
Economic balance point 201 is derived from the cost of electricity
and the cost of fossil fuel, as well as system 10 energy
consumption. System 10, when operated as a heat pump, is powered by
electricity. The energy consumption of system 10 decreases as the
exterior ambient temperature decreases, and the heating capacity of
system 20 also decreases. Therefore, calculations for economic
balance point 201 must be based on the amount of energy generated
per dollar, for example, millions of BTUs per dollar. The energy
consumption of a particular model of heat pump used in system 20 is
determined during product development and testing. Energy
consumption is measured at various, standard testing conditions and
documented. The energy consumption curve is depicted as linear, but
can be represented more accurately using additional data points or
an equation for the curve. With a more accurate representation of
the energy consumption curve and heating capacity curve, the
economic balance point 201 may be more accurately calculated.
[0036] A fossil-fuel furnace burns gas to produce heat. This gas
(natural gas or liquid propane) must be purchased by structure
owner at some cost. To determine economic balance point 201, the
amount of energy that the furnace can deliver (MBTUH) per dollar
spent for the gas must be calculated. Furnace efficiencies may be
based only on their efficiencies in combustion. Electrical energy
consumption of the furnace to power the blower to distribute the
air is not taken into account. However, it will be appreciated by
those skilled in the art that electrical energy consumption of the
furnace may be incorporated in the algorithms described in FIGS. 5
and 9, to further refine the economic and actual balance points. A
furnace's heating capacity is considered to not vary with the
exterior temperature. The heating capacity of the furnace is
determined at the time of installation based on the exterior
temperature design point. The heating capacity of the furnace must
be sufficient to produce enough heat to maintain the interior
temperature of structure 44 at the lowest expected exterior
temperature without any heating assistance from the heat pump.
[0037] Referring to FIG. 6, curve 200 represents the electrical
energy per dollar of a heat pump. Curve 200 is linear and has been
created by connecting two standard points of test data, the energy
consumption per dollar at 17.degree. F. and at 47.degree. F.
[0038] Curve 202 represents the energy produced per dollar for a
95% efficient furnace given a gas cost of $1.086281/Therm. One
Therm is equal to 100 MBTU. FIG. 6 depicts the process of
determining the amount of energy produced per dollar using
exemplary values.
[0039] Returning to FIG. 6, point 201, the economic balance point
for this exemplary system, represents the intersection of heat pump
electrical consumption curve 200 and furnace heating cost curve
202. For the given gas costs, electricity costs, heat pump heating
performance, and furnace efficiency, economic balance point 201 is
-20.degree. F. In this system, it is most economical to operate the
heat pump until the exterior temperature falls to -20.degree. F.
Because the heat pump cannot generate enough heat to maintain the
desired interior temperature of structure 44 (FIG. 4), economic
balance point 201 cannot be used as the actual balance point in
this system. The higher of application balance point 100 and
economic balance point 201 should be selected as described in FIG.
5. In this example, the actual balance point should be 22.degree.
F., the application balance point. Referring again to FIG. 4, the
economic balance point 201 is shown along with application balance
point 100. The actual balance point is the higher of the two
temperature values, application balance point 100.
[0040] The actual balance point setting is typically the higher of
the application balance point and the economic balance point. This
embodiment allows either the heat pump or the furnace to
independently maintain the desired temperature of structure 44.
However, in another embodiment, the economic balance point may be
lower than the application balance point and the actual balance
point may be selected to be the economic balance point. In the
latter embodiment, that is, where the application balance point is
selected to be the economic balance point, when the exterior
temperature is above the economic balance point but below the
application balance point, the heat pump will try to heat structure
44 but will be unable to offset the heat loss of structure 44. A
two-stage room thermostat will then call for auxiliary heating to
be energized. Through control logic built into the software or
hardware of system 20, which software or hardware may include a
room thermostat, a heat pump controller, a fossil fuel kit, etc.
the heat pump is de-energized and the furnace energized. The
furnace then operates exclusively, until the demand for auxiliary
heat from the room thermostat is satisfied. Once the room
thermostat is satisfied, the control system will return to heating
the room using the heat pump. This cycle will control the
temperature at the desired setpoint as long as the exterior
temperature remains between the application balance point and the
economic balance point, that is, the scenario in which the actual
balance point is lower than the application balance point.
Structure 44 will remain comfortable, but the HVAC heating system
will not cycle off.
[0041] The factors that may be taken into account in selecting the
application balance point include heat loss of the structure,
exterior design temperature, interior comfort condition, and
heating capacity of system 20 when operated in heat pump mode. The
heat loss of the structure varies with exterior temperature and
physical characteristics of the structure, and heating capacity of
system 20 varies with exterior temperature and equipment
operational mode. Factors that may be taken into account in
selecting the economic balance point include fossil fuel cost,
electrical energy cost, and energy consumption of system 20 when
operated in heat pump mode. The electrical energy consumption of
system 20 in heat pump mode varies with exterior temperature and
equipment operational mode.
[0042] Referring to FIG. 7, if the efficiency of the furnace in
system 20 decreased, and/or if the cost of gas increased, the
furnace would be less economical to operate. Curve 202 would shift
and economic balance point 403 would occur at a lower temperature
due to a new intersection point with curve 200. In the exemplary
embodiment shown in FIG. 7, a new economic balance point 402 occurs
at -28.degree. F. The change in economic balance point 403 to
economic balance point 402 would not result in a change of the
actual balance point.
[0043] In another example, should the heating efficiency of system
20 heat pump decrease or the cost of electricity increase, curve
200 would move down the temperature scale, since system 20 would
require more energy and cost in heat pump mode in order to generate
approximately the same quantity of heat. If the furnace conditions
remained the same, the economic balance point 402 would increase.
Economic balance point 403, located at 30.degree. F., occurs at a
higher temperature than application balance point 100, which occurs
at 22.degree. F. Therefore, new actual balance point 403 would
occur at 30.degree. F.
[0044] If the heat pump heating capacity changes through the use of
a multi-stage or fully variable capacity system, the application
balance point also changes. In a typical two-stage heat pump system
the heating capacity of system 20 can be reduced to 67% or 50% when
operating in single stage compressor mode compared to full capacity
compressor mode. A heat pump with a fully variable speed compressor
can vary the heating capacity with a high degree of resolution
between the minimum and maximum heating capacity. Although not
represented in a figure, the electrical power consumption of the
heat pump varies along with the heating capacity and the economic
balance point calculation is also affected.
[0045] FIG. 8 shows an additional heating capacity curve 500 that
represents the heating capacity of the system 20 operating as a
heat pump at less than maximum capacity. The lower heating capacity
causes the intersection of heating capacity curve 500 with
structure heat loss curve 101 to change from point 100 to point
501. Thus, the application balance point has also changed or
shifted to 36.degree. F., as indicated by point 501.
[0046] Similarly, heat loss curve 101 may also change. For example,
if the user selects an interior comfort setpoint change that is
lower than 70.degree. F., for example, 65.degree. F., the structure
heat loss curve will change. Or, if the construction or physical
characteristics of the structure change, heat loss curve 101 may
change. If heat loss curve 101 changes, application balance point
100 will change accordingly.
[0047] FIG. 8 shows that the interior comfort setpoint has changed
from 70.degree. F. to 60.degree. F. As a result structure heat loss
curve 101 has changed to a new heat loss curve represented by curve
502 and application balance point 100 has changed from 22.degree.
F. to 18.degree. F. as indicated by a second application balance
point 503. Varying the interior comfort setpoint may in some
situations change application balance point 100, 503, and change
the actual balance point depending on the current economic balance
point.
[0048] An exemplary embodiment relates to a method of specifying a
balance point by continuously monitoring the operating costs and
determining the current economic balance point for the system based
on the monitored operating costs. The method also includes
continuously monitoring capacity and performance to determine the
current application balance point. The method further includes
continually comparing the economic and application balance points
to determine the optimum actual balance point and then apply the
optimum actual balance point to system 20 operation.
[0049] HVAC system 10 includes a control device with a
preprogrammed algorithm (See, for example, FIGS. 5 & 9), which
incorporates various system data and controls the components of the
system 20. The control device can be a microprocessor-based
electronic controller to implement the algorithm, receive input
values and generate output signals. In one embodiment, the
disclosure includes a networked HVAC system 20. The network may be
configured as a wired or wireless network, or a combination
thereof. A heat pump controller, furnace controller, room
thermostat, an independent control panel, a personal computer (PC),
and other components of the HVAC system are in communication with
one another through the network. Since data and control commands
are transmitted freely throughout the network, the control
algorithm may be programmed into any of the HVAC system components.
In an alternate embodiment standard, non-networked HVAC controls
are connected through thermostat wires with only one of the devices
receiving the data to process the algorithm.
[0050] The present application contemplates methods, systems and
program products on any machine-readable media for accomplishing
its operations. The embodiments of the present application may be
implemented using an existing computer processors, or by a special
purpose computer processor for an appropriate system, incorporated
for this or another purpose or by a hardwired system.
[0051] As noted above, embodiments within the scope of the present
application include program products comprising machine-readable
media for carrying or having machine-executable instructions or
data structures stored thereon. Such machine-readable media can be
any available media which can be accessed by a general purpose or
special purpose computer or other machine with a processor. By way
of example, such machine-readable media can comprise RAM, ROM,
EPROM, EEPROM, CD-ROM or other optical disk storage, magnetic disk
storage or other magnetic storage devices, or any other medium
which can be used to carry or store desired program code in the
form of machine-executable instructions or data structures and
which can be accessed by a general purpose or special purpose
computer or other machine with a processor. When information is
transferred or provided over a network or another communications
connection (either hardwired, wireless, or a combination of
hardwired or wireless) to a machine, the machine properly views the
connection as a machine-readable medium. Thus, any such connection
is properly termed a machine-readable medium. Combinations of the
above are also included within the scope of machine-readable media.
Machine-executable instructions comprise, for example, instructions
and data which cause a general purpose computer, special purpose
computer, or special purpose processing machines to perform a
certain function or group of functions.
[0052] In many structures 44, Internet access is available through
a local personal computer (PC). A wired or wireless network (not
shown) may also be available. HVAC system 10 network described
above may be incorporated as a part of structure 44 network.
Preferably, however, HVAC system 10 will be part of a separate
network that may be connected to a second network in structure 44
through a gateway or network coupling device (not shown).
[0053] FIG. 9 discloses an exemplary embodiment of a control or
logic process 80 for system 10 to continually or periodically
monitor system 10 parameters. System parameters may change over
time and cause actual balance point 100 to change. System 10 may
monitor the parameters described above, either continually or
periodically at predetermined intervals. Using the methods
described above (see FIG. 5), at step 81 system 10 determines
economic balance point 201 and application balance point 100 based
on the current conditions present in system 10. System 10
determines actual balance point 100 based on economic balance point
201 and application balance point 100. Once the initial balance
points are determined in step 81, system 10 proceeds to step 82,
and obtains current electricity cost, and in step 83, current
natural gas cost. Any other relevant fuel source or utility may be
obtained as well. At step 84, system 10 determines a current energy
consumption and cost and at step 85, computes economic balance
point 201. System 10 proceeds to step 86 to determine current heat
pump capacity. At step 87, system 10 obtains exterior design
temperature, and at step 88, obtains an interior comfort setpoint.
At step 89, system 10 computes application balance point 100, and
at step 90 calculates actual balance point 100. At step 91, system
10 compares a newly calculated actual balance point 100 to previous
actual balance point 100 and determines if actual balance point 100
has changed. If actual balance point 100 has changed, system 10
applies the new actual balance point 100 to operate system 10, at
step 92, and returns to step 82. Otherwise, system 10 returns
directly to step 82.
[0054] System 10 may apply methods which are well known, to
transition to the new actual balance point setting. Such transition
methods include waiting until system 10 is not operating, that is,
there is no thermostat call for heating or cooling, to make the
change; forcing system 10 to "Off" mode to make the change and
re-starting system 10; and applying predetermined rules specified
by the manufacturer, installer, or structure owner.
[0055] System 20 heating capacity in heat pump mode, and energy
consumption of system 20 at various exterior temperatures, are
determined during testing and development of a specific heat pump.
In one embodiment one or more heat pump algorithms for continually
determining actual heat pump performance and efficiency, which are
known in the art, may be applied or incorporated into the
algorithms set forth in steps 84 and 86, to dynamically calculate
the application balance point.
[0056] In another embodiment, performance data for the heat pump
may be stored in the memory of the heat pump controller during
production of the heat pump. The stored performance data is used by
the heat pump controller in steps 84 and 86 if the dynamic balance
point algorithm is implemented in the heat pump control.
Alternately, if the algorithm is implemented by another controller
device on the network, the heat pump controller is configured to
transmit or transfer the performance data to that other control
device when the performance data is installed on the HVAC network
during installation of the HVAC system.
[0057] The respective electrical and gas or fuel oil utility
companies determine electricity rates and fossil fuel rates.
Current energy cost information may be transferred in a variety of
ways to a control device that implements the algorithm. In one
embodiment, an HVAC network is in communication with or is a node
on structure 44 network having access to the Internet. Therefore,
the control device can access the rate information provided by the
applicable utility company via the utility company websites.
Utility companies currently provide a variety of communication
channels to communicate with HVAC devices, for example, thermostats
and temperature controls, for purposes such as load shedding and
load monitoring. These communication channels can also be used for
acquiring the utility rate information. Methods will vary with each
utility provider and geographical area, as will be readily
appreciated by persons skilled in the art.
[0058] For installations in which real time utility rate
information is unavailable--for example, because there is no
Internet connection associated with the network to which the
control device is connected, or the utility companies do not make
the rate information available, another embodiment is disclosed. In
this embodiment, a user may enter utility rate information
manually. Users may obtain rate information through various means,
for example, a monthly utility bill, an Internet source, a utility
company hotline, etc. User may enter the rate information at
predetermined intervals, for example, monthly, or on an ad hoc
basis as needed. For example, the user may update the information
only when rates change or monthly when they receive their utility
bill. The interface with the HVAC network could be any of a variety
of methods including through PC software, room thermostat menus,
cell phone/PDA software, etc. Network interfaces may include
features that prompt the user to input the information at a
predetermined or specified interval. Manually entering the utility
rate information is less precise compared with automatically
updating the rate information from the Internet, the manual entry
of rate information provides more accurate information than
traditional HVAC installations. Additionally, some users may prefer
manual entry of rate information so that they have control over how
the system is functioning.
[0059] Heat loss curve 101 for the structure 44 is entered into the
control device when the system is first installed, and updated as
needed, for example, when significant changes are made to structure
44 such as major remodeling, or more efficient windows or doors are
installed. Heat loss information may be entered into the HVAC
system controller in a variety of ways, for example, thermostat
menus, service tools, control panel interface, cell phone, and PC
software. Since the standard method assumes a straight line
representing the heat loss of the structure (see, for example, FIG.
4), only two points are required. However, more accurate techniques
could include the use of an algorithm in the control device that
determines the actual heat loss of the structure over the
temperature range.
[0060] System 10 provides a dynamic interior comfort temperature.
Instead of using a heat loss curve calculated only at the time of
installation using one interior comfort temperature, system 10 can
recalculate heat loss curve 101 as the interior comfort temperature
changes. System 10 applies the available information based on the
input of the user by continuously recalculating linear heat loss
curve 101 as a function of the current interior temperature
setpoint.
[0061] Initially the user enters one interior comfort temperature
to establish an initial linear heat loss curve. For instance, the
interior comfort temperature might initially be set at 70.degree.
F. Generally, however, the interior comfort temperature is not
constant in actual operation. The interior comfort temperature is
the temperature setpoint of the room thermostat. Therefore, the
interior comfort temperature changes based on, for example, a
programmable thermostat that changes automatically with the time of
day, or if the structure 44 is occupied or unoccupied, or that is
manually overridden based on the preference of the user. In one
embodiment, the invention provides the ability to automatically
recalculate heat loss curve 101 based on changes in the interior
comfort temperature. The system also recalculates actual balance
point 100, since actual balance point selection is based on heat
loss curve 101.
[0062] Other, more elaborate methods may be incorporated into the
system algorithm to dynamically determine the actual heat loss of
the structure by applying data acquired through additional sensors
or information derived from the analysis of room temperature, time,
or similar parameters.
[0063] Additionally, because heat loss curve of structure 44 is, in
reality, non-linear, in another embodiment a non-linear curve may
be calculated which more accurately represents the actual heat loss
of structure 44.
[0064] The greater value of the application balance point or
economic balance point is typically selected as the controlling
parameter of the system. However, in another exemplary embodiment,
a balance point may be selected that is below the application
balance point or above both the economic and application balance
points. When an actual balance point is selected that is below the
application balance point, the heat pump and furnace operate
alternately while the exterior temperature remains above the
selected balance point and below the application balance point. One
advantage of selecting a balance point that is below the
application balance point is that the long run times maintain the
interior temperature more constant, as opposed to the situation
where a the application balance point is below the balance point,
which causes the interior temperature to drop when the system cuts
off, and to spike when the system is turned on again. In some
installations users may prefer to operate the furnace at
temperatures above the application or economic balance point. Their
decision may be based on perceived comfort as described below or
simply a matter of personal preference.
[0065] The control device may optionally include selection elements
to allow the user to specify which method of operation is desired,
or to set a specific static setpoint and override the control
algorithm.
[0066] Additionally, the control device may provide the ability for
the user to specify conditional operational parameters. For
instance, some individuals do not like feel of cooler air
temperatures at the duct registers in a heat pump system. Discharge
air temperature of a fossil fuel furnace is typically higher than
that of a heat pump. Both types of heat are capable of heating the
structure, but the cooler discharge air may be perceived by some
users as uncomfortably cold. However, when heat pump heating is
cheaper than fossil fuel heating, many users select financial
savings over comfort. Given these alternate user preferences,
system 20 allows the user to select or program the operating
parameters in financial terms. For instance, the user might select
heat pump operation below 20.degree. F. only when it will result in
a predetermined level of cost saving.
[0067] System 10 may optionally permit the user to specify a
minimum duct register air temperature, by incorporating in the
control system an additional sensor or algorithm that senses or
calculates the air temperature of the duct register. The user
interface would permit the user to display the economic impact so
they could decide the level of comfort versus cost savings they are
willing to trade. The user interface and controller are
configurable to display the economic impact data based on time
intervals of monthly, bi-monthly, seasonally, or annually.
[0068] The heat loss of structure 44 and the heat pump heating
capacity also change over time. Such changes are gradual when
compared with the fluctuations in fuel costs and the other time
variable factors. In an alternate embodiment, structural heat loss
and the heating capacity of the heat pump are factors that are
monitored by the control system through appropriate sensing
devices, and are incorporated into the control system/control
algorithm to further adjust the application balance point.
[0069] While only certain features and embodiments of the invention
have been shown and described, many modifications and changes may
occur to those skilled in the art (e.g., variations in sizes,
dimensions, structures, shapes and proportions of the various
elements, values of parameters (for example, temperatures,
pressures, etc.), mounting arrangements, use of materials, colors,
orientations, etc.) without materially departing from the novel
teachings and advantages of the subject matter recited in the
claims. The order or sequence of any process or method steps may be
varied or re-sequenced according to alternative embodiments. It is,
therefore, to be understood that the appended claims are intended
to cover all such modifications and changes as fall within the true
spirit of the invention. Furthermore, in an effort to provide a
concise description of the exemplary embodiments, all features of
an actual implementation may not have been described (that is,
those unrelated to the presently contemplated best mode of carrying
out the invention, or those unrelated to enabling the claimed
invention). It should be appreciated that in the development of any
such actual implementation, as in any engineering or design
project, numerous implementation specific decisions may be made.
Such a development effort might be complex and time consuming, but
would nevertheless be a routine undertaking of design, fabrication,
and manufacture for those of ordinary skill having the benefit of
this disclosure, without undue experimentation.
* * * * *