FIELD
[0001] The embodiments described herein pertain generally to systems and methods for heat
energy control of a heating, ventilation, air conditioning, and refrigeration (HVACR)
system. More specifically, the embodiments described herein pertain to maintaining
desired temperature in the intermediate loop of a cascade heating and/or cooling HVACR
system in different modes of system operation.
BACKGROUND
[0002] A heating, ventilation, air conditioning, and refrigeration (HVACR) system may include
one or more heat transfer circuits. A heat transfer circuit may include one or more
compressors, a condenser, an evaporator, fans, filters, dampers, and various other
equipment. The one or more compressors, the condenser, the expansion device, and the
evaporator are fluidly connected. The heat transfer circuit can be a heat pump, a
chiller, or the like.
SUMMARY
[0003] Features in the embodiments disclosed herein may enable and/or expand the application
of an HVACR system including cascade heat transfer circuits such as vapor-compression
chiller units and/or heat pump units. Features in the embodiments disclosed herein
may also allow for reliable and/or long-term system operation when the operating capacities
of the primary unit and the secondary unit of the cascade system are not synchronized.
Features in the embodiments disclosed herein may aid in different system operation
modes such as system start-up, stable operation, and intentional capacity mismatch
(e.g., cooling-dominant system operation).
[0004] Features in the embodiments disclosed herein may maintain a desired temperature in
the intermediate loop of a cascade heating and/or cooling system in different modes
of system operation. The modes include, but not limited to, system startup, unit(s)
startup, individual unit capacity changes (e.g., loading, unloading, or the like),
intentional cooling dominant operation, intentional heating dominant operation, unit(s)
shutdown, and/or system shutdown. Features in the embodiments disclosed herein may
prevent unacceptable temperature transients from occurring (during one or more of
the operation modes) which may negatively impact system operation (e.g., supply of
heating or cooling), causing unstable system and/unit(s) operation and impact unit(s)
reliability, short or long term.
[0005] In an example embodiment, a heating, ventilation, air conditioning, and refrigeration
(HVACR) system is provided. The system includes a first heat transfer circuit; a second
heat transfer circuit; a fluid loop between the first heat transfer circuit and the
second heat transfer circuit; a heat exchanger connecting to the fluid loop; and a
controller. The controller is configured to determine an operation parameter of the
system; and control the heat exchanger to remove heat from the fluid loop when the
operation parameter is above a first threshold.
[0006] In an example embodiment, a method of operating a heating, ventilation, air conditioning,
and refrigeration (HVACR) system is provided. The system includes a first heat transfer
circuit; a second heat transfer circuit; a fluid loop between the first heat transfer
circuit and the second heat transfer circuit; a heat exchanger connecting to the fluid
loop; and a controller. The method includes determining an operation parameter of
the system; and controlling the heat exchanger to remove heat from the fluid loop
when the operation parameter is above a first threshold.
BRIEF DESCRIPTION OF THE DRAWINGS
[0007] The accompanying drawings illustrate various embodiments of systems, methods, and
embodiments of various other aspects of the disclosure. Any person with ordinary skills
in the art will appreciate that the illustrated element boundaries (e.g. boxes, groups
of boxes, or other shapes) in the figures represent one example of the boundaries.
It may be that in some examples one element may be designed as multiple elements or
that multiple elements may be designed as one element. In some examples, an element
shown as an internal component of one element may be implemented as an external component
in another, and vice versa. Non-limiting and non-exhaustive descriptions are described
with reference to the following drawings. The components in the figures are not necessarily
to scale, emphasis instead being placed upon illustrating principles. In the detailed
description that follows, embodiments are described as illustrations only since various
changes and modifications may become apparent to those skilled in the art from the
following detailed description.
FIG. 1 illustrates a schematic diagram of a controller subsystem, arranged in accordance
with at least some embodiments described herein.
FIG. 2A illustrates a schematic diagram of a cascade HVACR system, arranged in accordance
with at least some embodiments described herein.
FIG. 2B illustrates a schematic diagram of a cascade HVACR system, arranged in accordance
with at least some embodiments described herein.
FIG. 2C illustrates a schematic diagram of a cascade HVACR system, arranged in accordance
with at least some embodiments described herein.
FIG. 3 is a flow chart illustrating an example processing flow for operating a cascade
HVACR system, arranged in accordance with at least some embodiments described herein.
DETAILED DESCRIPTION
[0008] In the following detailed description, particular embodiments of the present disclosure
are described herein with reference to the accompanying drawings, which form a part
of the description. In this description, as well as in the drawings, like-referenced
numbers represent elements that may perform the same, similar, or equivalent functions,
unless context dictates otherwise. Furthermore, unless otherwise noted, the description
of each successive drawing may reference features from one or more of the previous
drawings to provide clearer context and a more substantive explanation of the current
example embodiment. Still, the example embodiments described in the detailed description,
drawings, and claims are not intended to be limiting. Other embodiments may be utilized,
and other changes may be made, without departing from the spirit or scope of the subject
matter presented herein. It will be readily understood that the aspects of the present
disclosure, as generally described herein and illustrated in the drawings, may be
arranged, substituted, combined, separated, and designed in a wide variety of different
configurations, all of which are explicitly contemplated herein.
[0009] It is to be understood that the disclosed embodiments are merely examples of the
disclosure, which may be embodied in various forms. Well-known functions or constructions
are not described in detail to avoid obscuring the present disclosure in unnecessary
detail. Therefore, specific structural and functional details disclosed herein are
not to be interpreted as limiting, but merely as a basis for the claims and as a representative
basis for teaching one skilled in the art to variously employ the present disclosure
in virtually any appropriately detailed structure.
[0010] Additionally, the present disclosure may be described herein in terms of functional
block components and various processing steps. It should be appreciated that such
functional blocks may be realized by any number of hardware and/or software components
configured to perform the specified functions.
[0011] The scope of the disclosure should be determined by the appended claims and their
legal equivalents, rather than by the examples given herein. For example, the steps
recited in any method claims may be executed in any order and are not limited to the
order presented in the claims. Moreover, no element is essential to the practice of
the disclosure unless specifically described herein as "critical" or "essential".
[0012] As referenced herein, "directly" upstream or "directly" downstream may refer to that
no other components of a fluid circuit, other than fluid lines/connections/pipes for
conveying the fluid are provided between such directly related elements. As referenced
herein, "upstream" and "downstream" may refer to the direction of flow of the fluid
or a component thereof through the fluid circuit.
[0013] FIG. 1 illustrates a schematic diagram of a controller subsystem 100, arranged in
accordance with at least some embodiments described herein. In an example embodiment,
the controller subsystem 100 can be a part of the HVACR system and/or a part of the
unit (e.g., a vapor-compression unit).
[0014] It is to be understood that an HVACR system may include one or more heat transfer
circuits. Each heat transfer circuit can be a vapor-compression unit such as a heat
pump, a chiller, or the like. The vapor-compression units (i.e., the heat transfer
circuits) can form a cascade HVACR system including at least a primary unit and a
secondary unit. Each heat transfer circuit may include one or more compressors, a
condenser, an evaporator, fans, filters, dampers, and various other equipment. The
one or more compressors, the condenser, the expansion device, and the evaporator are
fluidly connected.
[0015] In an example embodiment, the HVACR system may include plants, chillers, air handlers,
furnaces, and/or boilers with multiple data sensors producing a continuous stream
of data, variable air volume (VAV) boxes and dampers, temperature or humidity sensors
monitoring a space, etc. In an embodiment, the HVACR system may include a panel, a
sensor, a controller, a microprocessor-controlled device, a converter, a thermostat,
a furnace, a heating system, a chiller, a cooling system, an air conditioner, an air
filter, an air purifier, a fire and life safety system, a security system, an alarm
system, an occupancy sensor, an electrical system monitor and controller, a lighting
system monitor and controller, a ventilation system monitor and controller, a temperature
sensor, a smoke sensor, a light sensor, a motion sensor, a humidity sensor, a pump,
an air handler, fluid and air moving and handling equipment, a terminal device, life
science and pharmacological control equipment and monitoring systems, a positive pressure
clean room, a negative pressure clean room, industrial automation and control equipment
and systems, a programmable logic controller, etc.
[0016] In an example embodiment, the controller subsystem 100 includes a controller 110.
The controller 110 can be the HVACR system controller and/or the unit (e.g., vapor-compression
unit) controller. The controller 110 can include a processor 112 in operative communication
with a memory 114, a user interface 116, and data storage 118. The memory 114 can
include random-access memory (RAM) which can be used, for example, for storage of
transient data, computed and intermediate results, input/output (I/O) buffering, graphical
user interface (GUI) buffering, program execution, and any other suitable purposes.
Data storage 118 can include non-volatile storage such as a flash drive, read-only
memory (ROM), electrically erasable programmable ROM (EEPROM), magnetic hard disk,
solid state disk (SSD), hybrid drives (combination hard disk/SSD) which can be used
for storage of data which persists through power cycling.
[0017] In an example embodiment, user interface 116 can include a number of elements which
may facilitate user input and the display of output to the user, and may include one
or more buttons, switches, light-emitting diode (LED) indicators, a character display
such as a liquid crystal display (LCD) or a vacuum fluorescent display (VFD), a graphic
display such as a thin film transistor (TFT) display, a touchscreen display, and the
like.
[0018] In an example embodiment, the controller 110 can also include a data network interface
115 for communicating data (wirelessly or in wired communication) to one or more user
devices and/or one or more components of the HVACR system over a data network 120,
such as a private LAN and/or the public Internet. User devices may include a mobile
telephone, smart phone, tablet device, smart watch, pager, server, notebook computer,
and/or a desktop computer, and the like. An optional server 130 can be communicatively
coupled to the controller 110 via the data network 120 and stores information for
a plurality of devices, including information relating to specific products, product
versions, firmware versions, and/or software versions.
[0019] FIGS. 2A, 2B, and 2C illustrate schematic diagrams of cascade HVACR systems (201,
202, 203), arranged in accordance with at least some embodiments described herein.
Each of the HVACR systems (201, 202, 203) can be a cascade (heating and/or cooling)
system including a first (or primary) heat transfer circuit 210 and a second (or secondary)
heat transfer circuit 220. Each heat transfer circuit can be a unit (e.g., a vapor-compression
unit) such as a heat pump, a chiller, or the like. It is to be understood that the
HVACR systems can include fluid lines/connections/pipes for conveying the fluid. The
HVACR systems can also include flow control device(s) such as a valve (e.g., a solenoid
valve, a ball valve, a three-way valve, a butterfly valve, a check-vale, or the like),
a damper, a pump, or the like, to allow, regulate, and/or modulate the fluid flow
(e.g., the flow rate, the amount of flow, or the like) flowing through the flow control
device, or to block the fluid flow from passing through the flow control device. The
primary unit 210 and/or the secondary unit 220 can be water source units.
[0020] In an example embodiment, each heat transfer circuit (unit) can include a compressor,
a condenser, an optional expander, an evaporator, and a controller (e.g., 110 of FG.
1) configured to control the operations of other components of the heat transfer circuit.
The heat transfer circuit can generally be applied in a variety of systems used to
control an environmental condition (e.g., temperature, humidity, air quality, or the
like) in a conditioned space. The conditioned space can be a space within an office
building, a commercial building, a factory, a laboratory, a data center, a residential
building, or the like. In an example embodiment, the heat transfer circuit can be
configured to be a cooling system (e.g., an air conditioning system) capable of operating
in a cooling mode. In another example embodiment, the heat transfer circuit can be
configured to be a heat pump that can operate in a heating/defrost mode. It is appreciated
that the heat transfer circuit can be configured to operate in a cooling mode and/or
a heating/defrosting mode. In an example embodiment, the heat transfer circuit can
heat or cool a process fluid (e.g., air, water and/or glycol, or the like). A working
fluid (e.g., one or more refrigerants) can flow through the heat transfer circuit
and be utilized to heat or cool the process fluid. In the heat transfer circuit, the
compressor, the condenser, the expander, and the evaporator can be fluidly connected.
An "expander" as described herein may also be referred to as an expansion device.
The expander can be an expansion valve, expansion plate, expansion vessel, orifice,
or the like, or other such types of expansion mechanisms. It should be appreciated
that the expander may be any suitable type of expander used in the field for expanding
a working fluid to cause the working fluid to decrease in pressure and temperature.
The heat transfer circuit can be configured to include more or less components, such
as, but not limited to, an economizer heat exchanger, one or more flow control devices
(e.g., a valve, a pump, etc.), a lubricant separator, a receiver tank, a dryer, a
suction-liquid heat exchanger, one or more sensors, or the like.
[0021] It is to be understood that the heat transfer circuit can operate according to generally
known principles. The heat transfer circuit can be configured to heat and/or cool
a liquid process fluid. The liquid process fluid can be a heat transfer fluid or medium
(e.g., a liquid such as, but not limited to, water or the like). The heat transfer
circuit may be generally representative of a liquid chiller system. The heat transfer
circuit can alternatively be configured to heat and/or cool a gaseous process fluid
(e.g., a heat transfer medium or fluid (e.g., a gas such as, but not limited to, air
or the like), in which case the heat transfer circuit may be generally representative
of an air conditioner and/or heat pump.
[0022] In an example embodiment, the heat transfer circuit can operate as a vapor-compression
circuit such that the compressor compresses a working fluid (e.g., a heat transfer
fluid such as, but not limited to, refrigerant or the like) from a relatively lower
pressure gas to a relatively higher-pressure gas. The relatively higher-pressure gas
is at a relatively higher temperature, being discharged from the compressor and flowing
through the condenser. In accordance with generally known principles, the working
fluid flows through the condenser and rejects heat to the process fluid (e.g., water,
air, etc.), thereby cooling the working fluid. The cooled working fluid, which is
now in a liquid form, flows to the expander that can reduce the pressure of the working
fluid. As a result, a portion of the working fluid is converted to a gaseous form.
The working fluid, which is now in a mixed liquid and gaseous form flows to the evaporator.
The working fluid flows through the evaporator and removes heat from the process fluid
(e.g., a heat transfer medium such as, but not limited to, water, a solution, air,
etc.), heating the working fluid, and converting it to a gaseous form. The gaseous
working fluid then returns to the compressor. The above-described process continues
while the heat transfer circuit is operating, for example, in a cooling mode (e.g.,
while the compressor is enabled).
[0023] As shown in FIG. 2A, the HVACR system 201 is a cascade system including the heat
transfer circuit (the primary unit) 210 and the heat transfer circuit (the secondary
unit) 220. An optional cooled loop can be a source of heat energy to the cascade system
201. In an example embodiment, the cooled loop can be a chilled water-cooling loop,
or some form of geothermal heat source such as surface water (ocean, lake, stream,
or the like) or geothermal well system (e.g., vertical bore, horizontal trench, or
the like).
[0024] In an example embodiment, in the cooled loop, a fluid flow (e.g., water) 242 having
a first temperature (e.g., at or about 50°F) can be mixed with a fluid flow 246 having
a second temperature (e.g., at or about 38°F, which is lower than the first temperature)
to form a fluid flow 244 having a third temperature (e.g., at or about 43°F, which
is between the first temperature and the second temperature). The fluid flow 244 can
flow, e.g., via a pump 240, into the primary unit 210 through its first inlet 211
at the cooled loop side. The primary unit 210 can remove heat energy from the fluid
flow 244 such that the fluid flow 244 becomes the fluid flow 247. The fluid flow 247
having the second temperature flows out of the primary unit 210 through its first
outlet 212 at the cooled loop side, e.g., via a flow control device (e.g., a valve)
215. The fluid flow 247 can pass through the flow control device (e.g., a valve) 205
as fluid flow 248. In an example embodiment, a portion of the fluid flow 247 can also
pass through the flow control device 205 as fluid flow 246, when the flow control
device 205 is controlled by e.g. a system controller (e.g., e.g., 110 of FG. 1).
[0025] In an example embodiment, the primary (low temperature) unit 210 can elevate a cooled
loop temperature to a higher temperature (in the intermediate loop) by removing heat
energy (e.g., in British thermal unit) from the cooled loop and/or adding heat energy
to the intermediate loop. The intermediate loop can be a fluid loop such as a hydronic
loop. The primary unit 210 may include, but not limited to, water-to-water heat pump(s)
and/or air-to-water heat pump(s). The primary unit 210 may use any suitable type of
compressor technology. The primary unit 210 at the cooled loop side may include an
evaporator to remove heat energy from the cooled loop, and the primary unit 210 at
the intermediate loop side may include a condenser to add heat energy to the intermediate
loop.
[0026] In an example embodiment, the secondary (high temperature) unit 220 can remove heat
energy from the intermediate loop and elevate the temperature of the intermediate
loop to a higher temperature in a heated loop by adding heat energy to the heated
loop. The secondary unit 220 can be, but not limited to, water-to-water heat pump(s).
The secondary unit 220 may use any suitable type of compressor technology. The secondary
unit 220 at the intermediate loop side may include an evaporator to remove heat energy
from the intermediate loop, and the primary unit 220 at the heated loop side may include
a condenser to add heat energy to the heated loop.
[0027] In an example embodiment, the intermediate loop can be a closed loop (between the
primary unit 210 and the secondary unit 220) that couples the primary unit 210 and
the secondary unit 220. In the intermediate loop, a fluid flow (e.g., water) 292 having
a fourth temperature (e.g., at or about 95°F) can flow out of the second outlet 214
of the primary unit 210, e.g., via a pump 250, into the secondary unit 220 via its
first inlet 221. The secondary unit 220 can remove heat energy from the fluid flow
292 such that the fluid flow 292 becomes the fluid flow 282. The fluid flow 282 having
the fifth temperature (e.g., at or about 85°F, which is lower than the fourth temperature)
flows out of the secondary unit 220 through its first outlet 222 at the intermediate
loop side, e.g., via a flow control device (e.g., a valve) 265.
[0028] In an example embodiment, when the primary unit 210 and the secondary unit 220 are
in balance (i.e., in sync), the fluid flow 282 can flow through a flow control device
(e.g., a valve) 235 and become fluid flow 284. The fluid flow 284 can flow into a
receiver (e.g., a buffer tank) 270 via its inlet 271, and flow out of the receiver
270 via its outlet 272. The fluid flow 284 can then flow, via a flow control device
225, into the primary unit 210 through its second inlet 213 at the intermediate loop
side. The primary unit 210 can add heat energy to the fluid flow 284 such that the
fluid flow 284 becomes fluid flow 292 flowing out of its second outlet 214 at the
intermediate loop side. It is to be understood that when the amount of cooling load
for the primary (low temperature) unit 210 and the amount of heating load for the
secondary (high temperature unit 220) are in balance, cascading units (the primary
unit 210 and the secondary unit 220) on the intermediate loop side (e.g., the hydronic
side) are configured to take the fluid leaving the condenser of the low temperature
unit 210 and push it into the evaporator of the high temperature unit 220 to further
boost the temperature.
[0029] In an example embodiment, in the heated loop, a fluid flow (e.g., water) 262 having
a sixth temperature (e.g., at or about 135°F) can flow, via a pump 260, into the secondary
unit 220 through its second inlet 223 at the heated loop side. The secondary unit
220 can add heat energy to the fluid flow 262 such that the fluid flow 262 becomes
fluid flow 264 (having a seventh temperature, e.g., at or about 155°F, which is greater
than the sixth temperature) flowing out of its second outlet 224 at the heated loop
side, e.g., via a flow control device (e.g., a valve) 255. It is to be understood
that the heated loop can be the main sink of heat energy from the cascade system.
The heated loop can be a building or process heating water loop.
[0030] It is to be understood that in typical cascade system operations, the capacity of
the cooled loop and the heated loop may not be in balance or in sync. That is, the
heat output of the primary unit 210's condenser may not naturally and dynamically
meet the heat input requirements of the secondary unit 220's evaporator. This deviation
(of 210's heat output and 220's heat input) may cause the temperature in the intermediate
loop to vary. It is to be understood that it may be possible to control the primary
unit 210's and the secondary unit 220's capacities to keep the intermediate loop's
temperature in an acceptable/desired range under some operating conditions. However,
it may be difficult or impossible to guarantee this (i.e., the intermediate loop's
temperature being in an acceptable/desired range) under various dynamic conditions
the cascade system is subject to such as preventing unacceptable temperature transients
from occurring (during one or more of the operation modes). Variation of the intermediate
loop temperature out of the acceptable/desired design range may result in malfunction
of the system and/or units.
[0031] In an example embodiment, when the primary unit 210 and the secondary unit 220 are
not in balance (i.e., not in sync), the fluid flow 282 can flow through the flow control
device 235 and become fluid flow 286. That is, instead of the fluid flow 282 flowing
through the flow control device 235 and becoming fluid flow 284, the flow control
device 235 is controlled (e.g., by a controller) to direct the fluid flow 282 (or
the fluid flow 292) into a heat exchanger 230 via its first inlet 233. The heat exchanger
230 is coupled to, connected to, or disposed in the intermediate loop (e.g., the heat
exchanger 230 connecting to either the fluid flow 282 or to the fluid flow 292). The
heat exchanger 230 can either remove heat energy from the fluid flow 286 of the intermediate
loop, or add heat energy to the fluid flow 286, based on an operation parameter so
that the fluid flow 286 may flow out of the heat exchanger 230 via its first outlet
234 and becomes fluid flow 288 and then becomes fluid flow 284 flowing into the receiver
270.
[0032] In an example embodiment, the operation parameter can be a temperature of the intermediate
loop (e.g., leaving and/or entering water temperature of the secondary unit 220, leaving
and/or entering water temperature of the primary unit 210, a combination thereof,
etc.). The operation parameter can be determined (e.g., by a controller) via sensed
measurements of sensor(s) (e.g., temperature sensor(s), etc.).
[0033] In an example embodiment, a fluid flow (away from the intermediate loop side) can
flow into the heat exchanger 230 via its second inlet (232 or 231), and the heat exchanger
230 can either remove heat energy from such fluid flow, or add heat energy to such
fluid flow, and the fluid flow can flow out of the heat exchanger 230 via its second
outlet (231 or 232). A flow control device 245 can be controlled (e.g., by a controller)
to adjust, regulate, modulate, or control the flow rate and/or the amount of flow
of the fluid flow (away from the intermediate loop side) based on the determined operation
parameter so that the operation parameter can be changed back to be in the acceptable/desired
range.
[0034] It is to be understood that the heat exchanger 230 can be e.g., an isolation heat
exchanger, applied in the intermediate loop of the cascade heating/cooling system,
to enable heat exchange between the intermediate loop and another heat sink and/or
heat source (not shown, at the side away from the intermediate loop side). Such heat
sink and/or heat source can be transient heat sink/source such as a cooling tower
circuit, a geothermal, a chilled water circuit, or the like. It is to be understood
that the secondary (high temperature) unit 220 may need to reject more heat energy
that is produced by the primary (low temperature) unit 210, due to heat produced via
the compression. It is to be understood that the primary unit 210 and the secondary
unit 220 may almost never be in balance so the intermediate loop temperature may vary.
By adding the heat exchanger 230 in the intermediate loop, heat energy can either
be added to or removed from the intermediate loop in order to ensure that the temperature
of the intermediate loop is within operational parameters.
[0035] In an example embodiment, the cooling capacity of the primary unit 210 can be at
or about 1000 tons. That is, the primary unit 210 can make at or about 1000 cooling
tons, and the energy rejected into its condenser loop can be at or about 1300 tons
due to the heat of compression. If the capacity of the secondary unit 220 is limited
to at or about 1000 tons (e.g., on its evaporator capacity), then the additional at
or about 300 tons may need to be rejected out of the intermediate loop via the heat
exchanger 230. That is, the capacity of the heat exchanger 230 can be at or about
300 tons. It is also to be understood that (the capacity of) the heat exchanger 230
and/or the heat sink and/or heat source can be sized based on the system requirements.
For example, they can be sized based on the minimum load of the primary unit 210 if
they are only needed for system start up and transient load modulation. If there is
a requirement for the primary unit 210 to be able to provide a full cooling capacity
under any (or no) heating load, then they can be sized based on the full cooling capacity
of the primary unit 210. The heat sink and/or heat source connected to the isolation
heat exchanger 230 can provide for the heat removal from and/or heat addition to the
intermediate loop via the operation of the heat exchanger 230. In an example embodiment,
types of heat sinks and/or heat sources include, but not limited to, evaporative cooling
towers dedicated to the intermediate loop operation and/or applied for dedicated unit
(210, 220) operation. It is further to be understood that dry coolers or evaporative
fluid coolers can be applied rather than separate isolation heat exchanger(s) 230
and evaporative cooling tower(s) as equivalent equipment. The cooling tower can be
configured to add heat energy to the atmosphere, by controlling e.g., fan speed or
water flow into the cooling tower.
[0036] In an example embodiment, the heat exchanger 230 can be a water-to-water heat exchanger
(i.e., a water-water heat exchanger), a water-to-air heat exchanger, or the like.
For water-water heat exchangers, the intermediate loop temperature can be controlled
(e.g., by a controller, via the flow control device 245) by controlling the flow (e.g.,
the amount of flow, the flow rate, etc.) flowing through the water-water heat exchanger.
For example, as the flow is controlled to be reduced, the capacity rejected (and/or
added) by the heat exchanger 230 may be reduced. Conversely, as the flow is controlled
to be increased, the capacity may be increased. The water-water heat exchanger can
be in series with a number of heat sources (and/or heat sinks) such as geo-thermal,
condenser loop, chilled water circuit, hot water circuit, wastewater, body of water,
and/or any viable fluid stream that has a temperature differential with the intermediate
loop.
[0037] In an example embodiment, the flow (of the heat exchanger 230) can be controlled
in different ways. For example, a variable speed pump can be utilized to regulate
the flow, a modulating valve (e.g., the flow control device 245) can be used to regulate
the flow, etc. The pump(s)/valve(s) can be on either side of the heat exchanger 230,
and they may be feedback controlled to a desired intermediate loop temperature.
[0038] In an example embodiment, the heat exchanger (e.g., 230A of FIG. 2C) can be an air-water
heat exchanger. In such configuration, the energy may be exchanged with the ambient
air, and the heat exchanger (e.g., 230A of FIG. 2C) can be a cooling tower, a dry
fluid cooler, or the like. It is to be understood that with these types of heat exchangers
(e.g., 230A of FIG. 2C), the capacity can be adjusted by either regulating the air
flow through the heat exchanger, or the fluid flow through the heat exchanger. For
regulating the airflow, variable speed fans can be utilized. In an example embodiment,
fan staging can be used for varying airflow as well. Louvers may also be used to restrict
airflow. It is to be understood that for the water flow (e.g., for the heat exchanger
230), variable speed pumps and/or modulating valves can be utilized. These arrangements
may also utilize the intermediate loop temperature for control.
[0039] It is to be understood that in FIG. 2B, the structure and function of the HVACR system
202 is the same as those of the HVACR system 201 of FIG. 2A except that in FIG. 2B,
(1) there are two primary units (210 and 210A) arranged in parallel, (2) there are
two secondary units (220 and 220A) arranged in parallel, and (3) in the heated loop,
the flow control devices are disposed upstream of the inlets of the secondary units
(220 and 220A) at the heated loop side (instead of downstream of the outlet of the
secondary unit 220 as shown in FIG. 2A).
[0040] It is to be understood that in FIG. 2C, the structure and function of the HVACR system
203 is the same as those of the HVACR systems 201 of FIG. 2A except that in FIG. 2C,
(1) there is no cooled loop, and the primary unit 210B can be an air-sourced unit,
(2) the heat exchanger 230A replaces the heat exchanger 230 (and another heat source/sink);
the heat exchanger 230A can be a fluid or dry cooler for heat rejection, (3) the receiver
(buffer tank) is disposed downstream of the outlet of the primary unit 210B and upstream
of the pump 250, and (4) a flow control device 275 is disposed downstream of the flow
control device 255 so that the fluid flow 264A can pass through the flow control device
275 as fluid flow 264, and/or a portion of the fluid flow 264A can pass through the
flow control device 275 as fluid flow 266, when the flow control device 275 is controlled
by e.g. a system controller (e.g., e.g., 110 of FG. 1). The fluid flow 262 can be
mixed with the fluid flow 266 to form a fluid flow 268 flowing to the secondary unit
220B via the pump 260.
[0041] In an example embodiment, the heat exchanger 230A can be a fluid cooler/dry cooler
heat exchanger in intermediate loop. The heat exchanger 230A may serve the same function
as the isolation heat exchanger 230 (plus a heat sink/source such as a cooling tower),
which may be preferable for users who do not want an evaporative cooling tower on
site.
[0042] It is to be understood that in FIGS. 2A, 2B, and 2C, the cascade systems (201, 202,
203) can have pump(s) 250 to manage fluid flow through units and/or heat exchangers,
to minimize flow transients. Valves and other hydronic specialties can be used to
enable hydronic system operation. The units (210, 210A, 210B, 220, 220A, 220B) can
control their respective compressor capacity based on e.g., their respective condenser
leaving (water) temperature. The intermediate loop heat exchanger (230, 230A) can
enable unit start and help protect against heating system load transients. The (capacity
of the) heat exchanger (230, 230A) can be sized based on minimum primary units' load
if a full cooling capacity is not required of primary units. The heat exchanger (230,
230A) can also be sized for full primary unit cooling capacity if cooling is required
at any heating load. Optional receivers such as buffer tanks 270 can be configured
to moderate temperature transients caused by units' load changes, and/or to provide
sufficient loop fluid volume to keep the control in a stable condition.
[0043] In an example embodiment, the controller (e.g., 110 of FIG. 1) can be configured
to regulate and optimize the temperature of the intermediate loop as required by the
vapor-compression units, external heating and cooling loads, and system mode of operation.
The controller can be also configured to control and coordinate the staging of vapor
compression units, heat exchanger(s), and heat sink and/or source operation. Features
in the embodiments disclosed herein may provide the intermediate loop heat exchanger
and heat sink/source and provide a method to control the temperatures in the intermediate
loop when the primary and secondary units' capacities are not matched (e.g., not in
balance, not in sync), either unintentionally or intentionally.
[0044] It is to be understood that "matching" of the primary and secondary unit's capacity
may consider the fact that the units' compressor, motor cooling, oil cooling, and/or
intermediate loop pump heat may be added to the heat energy in the system. As such,
the heat energy extracted from the cooled loop will not equal the heat energy added
to the heated loop. Rather, the heat energy added to the heated loop may be the sum
of the heat energy extracted from the cooled loop plus the sum of all the other heat
energy produced in the cascade system. Thus, the energy that must be extracted from
the cooled loop may be from at or about twenty to at or about sixty percent less than
that required by the heated loop.
[0045] It is further to be understood that the operation of the intermediate loop heat exchanger
(230, 230A) can be controlled (e.g., by a controller) in different operation modes
when the primary and secondary unit's capacities during operation are not in balance
(in sync), e.g., to add heat energy to the intermediate loop or remove heat energy
from the intermediate loop.
[0046] In an example embodiment, the operation of the intermediate loop heat exchanger (230,
230A) can be controlled during system heating mode startup process. It is to be understood
that starting the cascade system can be a dynamic process and maintaining the intermediate
loop temperature during the process can be challenging. Controlling the operation
of the heat exchanger (230, 230A) can simplify and stabilize the intermediate loop
temperature during system operation and/or start up. An example startup sequence using
the heat exchanger (230, 230A) can include: (1) enabling the intermediate loop, the
heat exchanger (230, 230A) and heat rejection (i.e. cooling tower) components, noting
that control sequence and setpoints may be required for proper system operation, (2)
enabling the cooled loop flow to the primary unit (210, 210A, 210B), (3) enabling
the primary unit controlling to its leaving condenser water temperature, if heating
is the system's main goal, or to its leaving evaporator water temperature if cooling
is the system's main goal, (4) allowing the primary unit's capacity and the intermediate
loop's temperature to stabilize, (5) enabling the heated loop flow to the secondary
unit (220, 220A, 220B), and (6) enabling the secondary unit controlling to its leaving
condenser water temperature, if heating is the system's main goal.
[0047] It is to be understood that as the secondary unit extracts heat from the intermediate
loop, the heat rejected via the heat exchanger 230 to the cooling tower can be decreased
by the system controls resulting in stable system operation. As long as the heat rejected
to the intermediate loop by the primary unit(s) is greater-than or equal-to the heat
energy required by the secondary unit(s) to meet the heating load, the system can
operate in balance.
[0048] It is to be understood that if the intermediate loop heat exchanger (230, 230A) is
connected to a system that can not only remove heat energy from but also add heat
energy to the intermediate loop, the intermediate loop temperature can be controlled
when the primary and secondary units' capacities are out of sync, within the limits
of the system heat sink/source.
[0049] In an example embodiment, the operation of the intermediate loop heat exchanger (230,
230A) can be controlled during cooling dominant operation. It is to be understood
that the controlling of both the cascade system leaving cooled water temperature and
the leaving heated water temperature may be a common requirement in cascade systems,
especially when the overall system is in a cool dominant load condition. Features
in the embodiments disclosed herein may provide support to the cooling dominant operation
to leverage primary unit(s) cooling capacity and to reduce the need for additional
cooling units and therefore reduce system cost. In the cooling dominant operation,
the control and/or the system operation is similar to the control and/or operation
of the system heating mode startup process. It is to be understood that since the
overall system loads are cooling dominant, the primary unit(s) operating capacity
may exceed that required to maintain the temperature in the intermediate loop. The
heat exchanger 230 and the heat rejection (i.e. the cooling tower) may extract excess
heat from the intermediate loop, maintaining the intermediate loop's temperature within
an acceptable temperature range.
[0050] In an example embodiment, the operation of the intermediate loop heat exchanger (230,
230A) can be controlled during the heating dominant operation (which is an inverse
of the cooling dominant operation), with control of both the cascade system leaving
cooled water temperature and the leaving heated water temperature being possible if
a heat sink and heat source system is connected to the intermediate loop heat exchanger.
The control and/or operation may enable injections of heat energy from that heat source,
in addition to that from the chilled water loop load.
[0051] In an example embodiment, the operation of the intermediate loop heat exchanger (230,
230A) can be controlled during the system shutdown. It is to be understood that getting
both the primary and secondary units to reduce capacity and shutdown simultaneously
and maintaining the intermediate loop temperature can be very difficult. Features
in the embodiments disclosed herein may eliminate the difficulty. The reverse of the
startup sequence can be implemented.
[0052] It is to be understood that a large buffer tank can be included in the system (instead
of the heat exchanger 230, 230A in the intermediate loop) the units' operation may
be synced up enough to get it to operate. Such an embodiment may not enable cooling
dominant operation.
[0053] FIG. 3 is a flow chart illustrating an example processing flow 300 for operating
a cascade HVACR system, arranged in accordance with at least some embodiments described
herein.
[0054] It is to be understood that the processing flow 300 disclosed herein can be conducted
by one or more controllers including e.g., the controller of the HVACR system (and/or
of the unit) of FIG. 1 and/or any other suitable controller, unless otherwise specified.
[0055] It is also to be understood that the processing flow 300 can include one or more
operations, actions, or functions as illustrated by one or more of blocks 310, 320,
330, 340, and 350. These various operations, functions, or actions may, for example,
correspond to software, program code, or program instructions executable by a processor
(e.g., a controller) that causes the functions to be performed. Although illustrated
as discrete blocks, obvious modifications may be made, e.g., two or more of the blocks
may be re-ordered; further blocks may be added; and various blocks may be divided
into additional blocks, combined into fewer blocks, or eliminated, depending on the
desired implementation. It is to be understood that before the processing flow 300,
operations including initializations or the like may be performed. For example, system
parameters may be initialized. It is to be understood that the processes, operations,
or actions described in FIGS. 1, 2A, 2B, and 2C may be implemented or performed by
the controller. Processing flow 300 may begin at block 310.
[0056] At block 310 (Operate cascade System), the controller may be configured to operate
the cascade system (e.g., 201, 202, 203 of FIGS. 2A, 2B, and 2C). It is to be understood
that the primary unit(s) and/or the secondary unit(s) can be operated and/or controlled
independently relative to each other. Processing may proceed from block 310 to block
320.
[0057] At block 320 (In Sync?), the controller may be configured to determine whether the
primary unit(s) and the secondary unit(s) are in balance (in sync). In an example
embodiment, the controller may be configured to determine whether the primary unit(s)
and the secondary unit(s) are in balance (in sync) by determining whether an operation
parameter is within a desired range. The operation parameter can be a temperature
of the intermediate loop (e.g., the leaving and/or entering water temperature of the
primary unit at the intermediate loop side, the leaving and/or entering water temperature
of the secondary unit at the intermediate loop side, a combination thereof, etc.).
If the operation parameter is within a desired range (e.g., at or below a first threshold
and at or above a second threshold, where the first threshold is greater than the
second threshold), the cascade system is in sync, processing may proceed from block
320 back to block 310.
[0058] If the operation parameter is not within the desired range (e.g., above the first
threshold or below the second threshold), the cascade system is not in sync, processing
may proceed from block 320 to block 330.
[0059] At block 330 (Excessive Heat?), the controller may be configured to determine whether
the intermediate loop or the system has excessive heat energy. In an example embodiment,
the controller may be configured to determine whether the intermediate loop or the
system has excessive heat energy by determining whether the operation parameter is
above the first threshold. If the operation parameter is above the first threshold,
the intermediate loop or the system has excessive heat energy, processing may proceed
from block 330 to block 350.
[0060] If the operation parameter is not above the first threshold (that is, the operation
parameter is instead below the second threshold), the intermediate loop or the system
needs extra heat energy, processing may proceed from block 330 to block 340.
[0061] At block 340 (Add heat to the intermediate loop), the controller may be configured
to control the heat exchanger (230, 230A of FIGS. 2A-2C) of the intermediate loop
and/or its associated heat sink/source and/or its associated flow control device(s),
to add heat energy to the intermediate loop, to keep/adjust the operation parameter
in/to the desired range (e.g., at or below the first threshold and at or above the
second threshold). Processing may proceed from block 340 back to block 310.
[0062] At block 350 (Remove heat from the intermediate loop), the controller may be configured
to control the heat exchanger (230, 230A of FIGS. 2A-2C) of the intermediate loop
and/or its associated heat sink/source and/or its associated flow control device(s),
to remove/reject/subtract heat energy from the intermediate loop, to keep/adjust the
operation parameter in/to the desired range (e.g., at or below the first threshold
and at or above the second threshold). Processing may proceed from block 350 back
to block 310.
[0063] It is to be understood that features in the embodiments disclosed herein may allow
unbalanced and/or uneven loads of the units and allow control to the capacity of the
cold-water temperature and the hot-water temperature independently (e.g., allowing
uneven loads and control for different water temperatures).
[0064] It is to be understood that the processes described with reference to the flowchart
of FIG. 3 and/or the processes described in other figures may be implemented as computer
software programs or in hardware. The computer program product may include a computer
program stored in a computer readable non-volatile medium. The computer program includes
program codes for performing the method shown in the flowcharts and/or GUIs. The processes
and logic flows described in this document can be performed by one or more programmable
processors (e.g., controller(s) of an HVACR system, controller(s) of a unit) executing
one or more computer programs to perform functions by operating on input data and
generating output. The processes and logic flows can also be performed by, and apparatus
can also be implemented as, special purpose logic circuitry, e.g., a field programmable
gate array, an application specific integrated circuit, or the like.
[0065] Processors suitable for the execution of a computer program include, by way of example,
both general and special purpose microprocessors (e.g., controller(s) of an HVACR
system, controller(s) of a unit), and any one or more processors of any kind of digital
computer. Generally, a processor will receive instructions and data from a read only
memory or a random-access memory or both. The essential elements of a computer are
a processor for performing instructions and one or more memory devices for storing
instructions and data.
[0066] It is to be understood that different features, variations and multiple different
embodiments have been shown and described with various details. What has been described
in this application at times in terms of specific embodiments is done for illustrative
purposes only and without the intent to limit or suggest that what has been conceived
is only one particular embodiment or specific embodiments. It is to be understood
that this disclosure is not limited to any single specific embodiments or enumerated
variations. Many modifications, variations and other embodiments will come to mind
of those skilled in the art, and which are intended to be and are in fact covered
by both this disclosure. It is indeed intended that the scope of this disclosure should
be determined by a proper legal interpretation and construction of the disclosure,
including equivalents, as understood by those of skill in the art relying upon the
complete disclosure present at the time of filing.
Aspects:
[0067] It is appreciated that any one of aspects can be combined with each other.
[0068] Aspect 1. A heating, ventilation, air conditioning, and refrigeration (HVACR) system,
the system comprising: a first heat transfer circuit; a second heat transfer circuit;
a fluid loop between the first heat transfer circuit and the second heat transfer
circuit; a heat exchanger connecting to the fluid loop; and a controller configured
to: determine an operation parameter of the system; and control the heat exchanger
to remove heat from the fluid loop when the operation parameter is above a first threshold.
[0069] Aspect 2. The HVACR system of aspect 1, wherein the controller is further configured
to control the heat exchanger to add heat to the fluid loop when the operation parameter
is below a second threshold.
[0070] Aspect 3. The HVACR system of aspect 1 or aspect 2, wherein the first heat transfer
circuit includes a fluid inlet configured to receive fluid from the fluid loop and
a fluid outlet for fluid flowing out to the fluid loop, the first heat transfer circuit
is configured to add heat to the fluid loop.
[0071] Aspect 4. The HVACR system of any one of aspects 1-3, further comprising: a cooled
loop configured to add heat to the fluid loop via the first heat transfer circuit,
the cooled loop being a source of heat of the system.
[0072] Aspect 5. The HVACR system of any one of aspects 1-4, wherein the second heat transfer
circuit includes a fluid inlet configured to receive fluid from the fluid loop and
a fluid outlet for fluid flowing out to the fluid loop, the second heat transfer circuit
is configured to remove heat from the fluid loop.
[0073] Aspect 6. The HVACR system of any one of aspects 1-5, further comprising: a heated
loop configured to remove heat from the fluid loop via the second heat transfer circuit,
the heated loop being a sink of heat of the system.
[0074] Aspect 7. The HVACR system of any one of aspects 1-6, further comprising: a flow
control device, the controller is further configured to control the flow control device
to direct a fluid flow from the fluid loop to the heat exchanger when the operation
parameter is above the first threshold.
[0075] Aspect 8. The HVACR system of aspect 7, wherein the controller is further configured
to control the flow control device to direct the fluid flow from the fluid loop to
the heat exchanger when the operation parameter is below a second threshold.
[0076] Aspect 9. The HVACR system of aspect 8, wherein the controller is further configured
to control the flow control device to block the fluid flow from the fluid loop to
the heat exchanger when the operation parameter is at or below the first threshold
and is at or above the second threshold.
[0077] Aspect 10. The HVACR system of any one of aspects 1-9, wherein the operation parameter
is a temperature of a fluid flow downstream of the first heat transfer circuit and
upstream of the second heat transfer circuit.
[0078] Aspect 11. A method of operating a heating, ventilation, air conditioning, and refrigeration
(HVACR) system, the system including a first heat transfer circuit; a second heat
transfer circuit; a fluid loop between the first heat transfer circuit and the second
heat transfer circuit; a heat exchanger connecting to the fluid loop; and a controller,
the method comprising: determining an operation parameter of the system; and controlling
the heat exchanger to remove heat from the fluid loop when the operation parameter
is above a first threshold.
[0079] Aspect 12. The method of aspect 11, further comprising: controlling the heat exchanger
to add heat to the fluid loop when the operation parameter is below a second threshold.
[0080] Aspect 13. The method of aspect 11 or aspect 12, wherein the first heat transfer
circuit includes a fluid inlet configured to receive fluid from the fluid loop and
a fluid outlet for fluid flowing out to the fluid loop, the first heat transfer circuit
is configured to add heat to the fluid loop.
[0081] Aspect 14. The method of any one of aspects 11-13, wherein the system further comprises
a cooled loop configured to add heat to the fluid loop via the first heat transfer
circuit, the cooled loop being a source of heat of the system.
[0082] Aspect 15. The method of any one of aspects 11-14, wherein the second heat transfer
circuit includes a fluid inlet configured to receive fluid from the fluid loop and
a fluid outlet for fluid flowing out to the fluid loop, the second heat transfer circuit
is configured to remove heat from the fluid loop.
[0083] Aspect 16. The method of any one of aspects 11-15, wherein the system further comprises
a heated loop configured to remove heat from the fluid loop via the second heat transfer
circuit, the heated loop being a sink of heat of the system.
[0084] Aspect 17. The method of any one of aspects 11-16, wherein the system further comprises
a flow control device, the method further comprises controlling the flow control device
to direct a fluid flow from the fluid loop to the heat exchanger when the operation
parameter is above the first threshold.
[0085] Aspect 18. The method of aspect 17, further comprising: controlling the flow control
device to direct the fluid flow from the fluid loop to the heat exchanger when the
operation parameter is below a second threshold.
[0086] Aspect 19. The method of aspect 18, further comprising: controlling the flow control
device to block the fluid flow from the fluid loop to the heat exchanger when the
operation parameter is at or below the first threshold and is at or above the second
threshold.
[0087] Aspect 20. The method of any one of aspects 11-19, wherein the operation parameter
is a temperature of a fluid flow downstream of the first heat transfer circuit and
upstream of the second heat transfer circuit.
[0088] The terminology used in this specification is intended to describe particular embodiments
and is not intended to be limiting. The terms "a," "an," and "the" include the plural
forms as well, unless clearly indicated otherwise. The terms "comprises" and/or "comprising,"
when used in this specification, specify the presence of the stated features, integers,
steps, operations, elements, and/or components, but do not preclude the presence or
addition of one or more other features, integers, steps, operations, elements, and/or
components.
[0089] With regard to the preceding description, it is to be understood that changes may
be made in detail, especially in matters of the construction materials employed and
the shape, size, and arrangement of parts without departing from the scope of the
present disclosure. This specification and the embodiments described are exemplary
only, with the true scope and spirit of the disclosure being indicated by the claims
that follow.