[Technical Field]
[0001] The present invention relates to a warm water heating system which heats warm water
using a heat output heat exchanger provided in a heat pump, and a control device and
a control method of the warm water heating system.
[Background Art]
[0002] Generally, a warm water system which supplies warm water includes a heat storage
tank. In the warm water system, temperature control is performed by some water stored
in this heat storage tank obtaining heat from a heat output heat exchanger provided
in a main body of the warm water heat pump (e.g., see Patent Literature 1).
[0003] However, in the invention described in Patent Literature 1, there is a problem in
that installation cost or an installation space increase since the heat storage tank
is provided in the warm water system. Further, there is a problem in that it takes
time to increase a temperature since the water stored in the heat storage tank is
circulated to the heat output heat exchanger to increase the water temperature in
the heat storage tank.
[0004] Therefore, a method of providing a three-way valve in a warm water system to circulate
a part of output of warm water from a heat output heat exchanger to the heat output
heat exchanger and perform control so that a temperature of an entrance of the heat
output heat exchanger becomes a predetermined target temperature is described in Patent
Literature 2. A temperature increase rate of the warm water system can be increased
using this method.
[0005] A control device according to the preamble of claim 1 and a control method according
to the preamble of claim 9 are known from document
WO 2011/108392.
[Citation List]
[Patent Literature]
[0006]
[Patent Literature 1] Japanese Patent Laid-Open Publication No. 2002-340400
[Patent Literature 2] Japanese Patent Laid-Open Publication No. 2011-185477
[Summary of Invention]
[Problem to be Solved by the Invention]
[0007] When the method described in Patent Literature 2 is used, a three-way valve is fully
opened and entire output of warm water from a heat output heat exchanger is likely
to be circulated when a warm water system is in a transient state, such as at the
time of start-up of the heat pump, i.e., when a water temperature of the entire warm
water system is lower than a target temperature. In this case, when the water temperature
of the warm water system rapidly increases and a temperature of an entrance of the
heat output heat exchanger reaches a target temperature, an opening degree of the
three-way valve changes for the first time. However, since opening and closing of
the three-way valve is not instantly switched, an opening and closing operation of
the three-way valve cannot follow a temperature change of the warm water, and the
water temperature of the entrance of the heat output heat exchanger is likely to exceed
the target temperature. In this case, heat capacity exchanged in the heat output heat
exchanger of the heat pump may decrease and efficiency of the warm water heating system
may decrease.
[0008] The present invention provides a warm water heating system, a control device and
a control method which appropriately controls a temperature increase rate in a transient
state of a warm water system.
[Means for Solving the Problem]
[0009] The present invention provides a control device used to control a warm water heating
system, the control device including: a heat pump including a heat output heat exchanger
which takes heat from a heat source system and outputs heat; a heating portion which
heats water using the heat obtained from the heat output heat exchanger; an outflow
portion which flows the water heated by the heating portion to a heating target; a
circulation portion which circulates the water heated by the heating portion to an
upstream side of the heating portion; an inflow portion which flows water from the
heating target into the upstream side of the heating portion; and an adjustment unit
which adjusts flow amount distribution of the water from the heating portion to the
outflow portion and the circulation portion, wherein the control device includes an
upstream-side target temperature setting unit which sets a target temperature of the
water on the upstream side of the heating portion; and an adjustment amount determination
unit which determines an adjustment amount of the flow amount distribution by the
adjustment unit so that a temperature of the water on the upstream side of the heating
portion increases by a predetermined temperature until the temperature of the water
on the upstream side of the heating portion reaches the target temperature.
[0010] Further, the present invention provides for the adjustment amount determination unit
to determine the adjustment amount of the flow amount distribution by the adjustment
unit so that the temperature of the water on the upstream side of the heating portion
increases by a predetermined temperature calculated based on states of water flowing
in the heating portion, water circulated by the circulation portion, and water flowing
from the inflow portion into the upstream side of the heating portion until the temperature
of the water on the upstream side of the heating portion reaches the target temperature.
[0011] Further, in the present invention, it is preferable to further include an adjustment
temperature calculation unit which calculates, as an adjustment temperature used for
determination of the adjustment amount, a temperature difference between a temperature
of water obtained by mixing water flowing from the inflow portion into the upstream
side of the heating portion with water circulated by the circulation portion and a
temperature of the water flowing in the heating portion based on the states of the
water flowing in the heating portion, the water circulated by the circulation portion,
and the water flowing from the inflow portion into the upstream side of the heating
portion. It is preferable for the adjustment amount determination unit to determine
the adjustment amount of the flow amount distribution by the adjustment unit so that
the temperature of the water on the upstream side of the heating portion increases
by the adjustment temperature calculated by the adjustment temperature calculation
unit until the temperature of the water on the upstream side of the heating portion
reaches the target temperature.
[0012] Further, in the present invention, it is preferable for the adjustment amount determination
unit to determine the adjustment amount of the flow amount distribution by the adjustment
unit so that the temperature of the water flowing into the heating portion becomes
constant until the heat pump operates.
[0013] Further, in the present invention, it is preferable for the upstream-side target
temperature setting unit to set a target temperature of the water on the upstream
side of the heating portion based on a maximum heating amount in the heating portion,
a flow amount of the water flowing into the heating portion, and a target temperature
of the water on a downstream side of the heating portion.
[0014] Further, in the present invention, it is preferable to include a downstream-side
target temperature setting unit which sets the target temperature of the water on
the downstream side of the heating portion; and a heat pump adjustment amount determination
unit which determines an adjustment amount of heat pump control so that the temperature
of the water on the downstream side of the heating portion increases by a predetermined
temperature until the temperature of the water on the downstream side of the heating
portion reaches the target temperature.
[0015] Further, in the present invention, it is preferable for the heat pump adjustment
amount determination unit to determine the adjustment amount of the heat pump control
so that the temperature of the water on the downstream side of the heating portion
increases by a predetermined temperature calculated based on a state of the water
flowing in the heating portion and flowing from the heating portion into the adjustment
unit, and a heating amount in the heating portion until the temperature of the water
on the downstream side of the heating portion reaches the target temperature.
[0016] Further, in the present invention, it is preferable to include a heat pump adjustment
temperature calculation unit which calculates, as a heat pump adjustment temperature
used for determination of the adjustment amount of the heat pump control, the temperature
difference between the temperature of the water flowing in the heating portion when
the water is heated by the heating portion and the temperature of the water flowing
from the heating portion into the adjustment unit, based on the state of the water
flowing in the heating portion and the state of the water flowing from the heating
portion into the adjustment unit, and a heating amount in the heating portion. It
is preferable for the heat pump adjustment amount determination unit to determine
the adjustment amount of the heat pump control so that the temperature of the water
on the downstream side of the heating portion increases by the heat pump adjustment
temperature calculated by the heat pump adjustment temperature calculation unit until
the temperature of the water on the downstream side of the heating portion reaches
the target temperature.
[0017] Further, the present invention provides a control device used to control a warm water
heating system including: a heat pump including a heat output heat exchanger which
takes heat from a heat source system and outputs heat; a heating portion which heats
water using the heat obtained from the heat output heat exchanger; an outflow portion
which flows the water heated by the heating portion to a heating target; a circulation
portion which circulates the water heated by the heating portion to an upstream side
of the heating portion; an inflow portion which flows water from the heating target
into the upstream side of the heating portion, a downstream-side target temperature
setting unit which sets a target temperature of the water on a downstream side of
the heating portion; and a heat pump adjustment amount determination unit which determines
an adjustment amount of heat pump control so that a temperature of the water on the
downstream side of the heating portion increases by a predetermined temperature until
the temperature of the water on the downstream side of the heating portion reaches
the target temperature.
[0018] Further, the present invention provides for the heat pump adjustment amount determination
unit to determine the adjustment amount of the heat pump control so that the temperature
of the water on the downstream side of the heating portion increases by a predetermined
temperature calculated based on the state of water flowing in the heating portion
and the state of water flowing from the heating portion and a heating amount in the
heating portion until the temperature of the water on the downstream side of the heating
portion reaches the target temperature.
[0019] Further, in the present invention, it is preferable to include a heat pump adjustment
temperature calculation unit which calculates, as a heat pump adjustment temperature
used for determination of the adjustment amount of the heat pump control, the temperature
difference between the temperature of the water flowing in the heating portion when
the water is heated by the heating portion and the temperature of the water flowing
from the heating portion based on the state of the water flowing in the heating portion
and the state of the water flowing from the heating portion and the heating amount
in the heating portion, and it is preferable for the heat pump adjustment amount determination
unit to determine the adjustment amount of the heat pump control so that the temperature
of the water on the downstream side of the heating portion increases by the heat pump
adjustment temperature calculated by the heat pump adjustment temperature calculation
unit until the temperature of the water on the downstream side of the heating portion
reaches the target temperature.
[Effects of the Invention]
[0020] According to the present invention, the adjustment amount of the adjustment unit
or the adjustment amount of the heat pump is determined so that the temperature of
the warm water on the upstream side or the downstream side of the heating portion
increases by a predetermined temperature until the temperature of the warm water on
the upstream side of the heating portion reaches the target temperature. Accordingly,
it is possible to appropriately control the temperature increase rate in the transient
state of the warm water system.
[Brief Description of Drawings]
[0021]
Fig. 1 is a schematic configuration diagram of a warm water heating system according
to a first embodiment of the present invention.
Fig. 2 is a schematic block diagram showing a configuration of a control device according
to the first embodiment of the present invention.
Fig. 3 is a flowchart showing operation of the control device according to the first
embodiment of the present invention.
Fig. 4 is a schematic configuration diagram of a warm water heating system according
to a second embodiment of the present invention.
Fig. 5 is a schematic block diagram showing a configuration of a control device according
to the second embodiment of the present invention.
Fig. 6 is a schematic configuration diagram of a warm water heating system according
to a third embodiment of the present invention.
Fig. 7 is a schematic block diagram showing a configuration of a control device according
to the third embodiment of the present invention.
Fig. 8 is a flowchart showing operation of the control device according to the third
embodiment of the present invention.
Fig. 9 is a schematic configuration diagram of a warm water heating system according
to a fourth embodiment of the present invention.
[Description of Embodiments]
[0022] Hereinafter, embodiments of the present invention will be described in detail with
reference to the accompanying drawings.
(First embodiment)
[0023] Fig. 1 is a schematic configuration diagram of a warm water heating system according
to a first embodiment of the present invention.
[0024] The warm water heating system includes a heat pump 20 which takes heat from a heat
source system 10 and outputs heat, a warm water system 30 which heats water using
the heat output from the heat pump 20, and a control device 40 which controls the
warm water system 30.
[0025] The heat pump 20 includes a pipe filled with a heat medium, and an evaporator 21,
a compressor 22, a condenser 24 (a heat output heat exchanger), and an expansion valve
25 which are connected to the pipe.
[0026] The evaporator 21 increases a temperature of the heat medium using the heat output
from the heat source system 10.
[0027] The compressor 22 compresses and liquefies the heat medium whose temperature is increased
by the evaporator 21.
[0028] A vane 23 adjusts a flow amount of the heat medium liquefied by the compressor 22.
[0029] The condenser 24 supplies heat of the heat medium flowing from the vane 23 to the
warm water system 30.
[0030] The expansion valve 25 depressurizes and vaporizes the heat medium whose temperature
is decreased by the condenser 24.
[0031] The warm water system 30 is configured of an inflow portion 31, a circulation pump
32, a heating portion 33, a three-way valve 34 (adjustment portion), a circulation
portion 35, and an outflow portion 36.
[0032] The inflow portion 31 flows water from a heating target into the heating portion
33 through the circulation pump 32.
[0033] The circulation pump 32 pumps the inflow water to the heating portion 33.
[0034] The heating portion 33 heats the inflow water from the circulation pump 32 using
the heat supplied from the condenser 24 and supplies the heated water to the three-way
valve 34.
[0035] The three-way valve 34 flows a part of the water heated by the heating portion 33
into the circulation portion 35 and flows the remainder into the outflow portion 36
according to its opening degree (flow amount distribution).
[0036] The circulation portion 35 circulates the water from the three-way valve 34 to the
heating portion 33 through the circulation pump 32.
[0037] The outflow portion 36 flows the water from the three-way valve 34 to the heating
target.
[0038] Further, an inflow portion flow amount detector 51, an inflow portion temperature
detector 52, a heating portion flow amount detector 53, a heating portion upstream-side
temperature detector 54, and a heating portion downstream-side temperature detector
55 are provided in the warm water system 30.
[0039] The inflow portion flow amount detector 51 detects a flow amount F
1 of the water flowing through the inflow portion 31.
[0040] The inflow portion temperature detector 52 detects a temperature T
1 of the water flowing through the inflow portion 31.
[0041] The heating portion flow amount detector 53 detects a flow amount F
2 of the water flowing through the heating portion 33.
[0042] The heating portion upstream-side temperature detector 54 detects a temperature of
the water on an upstream side of the heating portion 33. In other words, the heating
portion upstream-side temperature detector 54 detects a temperature T
2 of the water before the water is heated in the heating portion 33.
[0043] The heating portion downstream-side temperature detector 55 detects a temperature
of the water on a downstream side of the heating portion 33. In other words, the heating
portion downstream-side temperature detector 55 detects a temperature T
3 of the water after the water is heated in the heating portion 33.
[0044] Fig. 2 is a schematic block diagram showing a configuration of the control device
40 according to the first embodiment of the present invention.
[0045] The control device 40 includes a sensor information acquisition unit 401, an upstream-side
temperature change rate calculation unit 402 (an adjustment temperature calculation
unit), an upstream-side target temperature setting unit 403, a heat pump information
input unit 404, an upstream-side immediate target temperature setting unit 405, and
a three-way valve control unit 406 (an adjustment amount determination unit).
[0046] The sensor information acquisition unit 401 acquires sensor information (a flow amount
or a temperature) detected by each detector provided in the warm water system 30.
[0047] The upstream-side temperature change rate calculation unit 402 calculates the change
rate (adjustment temperature) of the water temperature on the upstream side of the
heating portion 33, i.e., an increase rate of the water temperature based on the sensor
information acquired by the sensor information acquisition unit 401. The change rate
of the water temperature is calculated by applying the sensor information to a heat
balance model.
[0048] The upstream-side target temperature setting unit 403 sets a target temperature of
the water on the upstream side of the heating portion 33 when the warm water system
30 enters a steady state if the heat pump 20 and the warm water system 30 operate.
[0049] The heat pump information input unit 404 receives input of heat pump information
indicating whether the compressor 22 of the heat pump 20 has started operation.
[0050] The upstream-side immediate target temperature setting unit 405 sets the immediate
target temperature of the water on the upstream-side of the heating portion 33 at
a current time according to the information acquired from the sensor information acquisition
unit 401, the upstream-side temperature change rate calculation unit 402, the upstream-side
target temperature setting unit 403 and the heat pump information input unit 404.
Specifically, the upstream-side immediate target temperature setting unit 405 sets
the current water temperature on the upstream side of the heating portion 33 as the
immediate target temperature in a state in which the compressor 22 of the heat pump
20 does not operate. In other words, the upstream-side immediate target temperature
setting unit 405 sets the immediate target temperature to preserve the current water
temperature. Further, the upstream-side immediate target temperature setting unit
405 sets the immediate target temperature based on the temperature change rate calculated
by the upstream-side temperature change rate calculation unit 402 until the current
water temperature on the upstream side of the heating portion 33 reaches the upstream-side
target temperature after the compressor 22 operates. Also, the upstream-side immediate
target temperature setting unit 405 sets the target temperature set by the upstream-side
target temperature setting unit 403 as the immediate target temperature after the
current water temperature on the upstream side of the heating portion 33 has reached
the upstream-side target temperature.
[0051] The three-way valve control unit 406 performs control of an opening degree of the
three-way valve 34 under PID (Proportional/Integral/Differential) control based on
the immediate target temperature set by the upstream-side immediate target temperature
setting unit 405 and the current water temperature on the upstream side of the current
heating portion 33.
[0052] Next, operation of the control device 40 at the time of operation start of the warm
water heating system according to the present embodiment will be described.
[0053] Fig. 3 is a flowchart showing operation of the control device 40 according to the
first embodiment of the present invention.
[0054] First, the upstream-side target temperature setting unit 403 of the control device
40 receives input of a target temperature T
2d on the upstream side of the heating portion 33 from a manager before operation start
of the warm water heating system (step S1).
[0055] The manager of the warm water heating system operates the warm water system 30 after
the setting of the target temperature. When the warm water system 30 operates, the
upstream-side immediate target temperature setting unit 405 determines whether the
heat pump information received as input by the heat pump information input unit 404
indicates operation start of the compressor 22 (step S2). The heat pump information
indicates the operation start of the compressor 22 when the manager of the warm water
heating system operates the compressor 22.
[0056] When the upstream-side immediate target temperature setting unit 405 determines that
the heat pump information indicates that the compressor 22 has not yet operated (step
S2: NO), the upstream-side immediate target temperature setting unit 405 acquires
a temperature T
2 detected by the heating portion upstream-side temperature detector 54 from the sensor
information acquisition unit 401 and sets the temperature T
2, i.e., the water temperature on the upstream-side of the heating portion 33, as the
immediate target temperature T
2a (step S3). Then, the three-way valve control unit 406 determines the opening degree
so that the water temperature on the upstream side of the heating portion 33 becomes
constant as the immediate target temperature T
2a, i.e., the current temperature T
2, and controls the three-way valve 34 based on the opening degree (step S4). In other
words, the three-way valve control unit 406 controls the opening degree of the three-way
valve 34 so that the water for dissipating generated heat by the circulation pump
32 flows from the inflow portion 31.
[0057] Accordingly, the three-way valve 34 is adjusted with a small closing degree from
full opening with respect to the circulation portion 35, i.e., a small opening degree
with respect to the outflow portion 36, until the compressor 22 operates.
[0058] Thereafter, the process returns to step S2 and the operation of steps S2 to S4 is
repeatedly executed until the compressor 22 operates.
[0059] On the other hand, when the upstream-side immediate target temperature setting unit
405 determines that the heat pump information indicates the operation start of the
compressor 22 (step S2: YES), the upstream-side immediate target temperature setting
unit 405 acquires the temperature T
2 detected by the heating portion upstream-side temperature detector 54 from the sensor
information acquisition unit 401. The upstream-side immediate target temperature setting
unit 405 then determines whether the temperature T
2 reaches the target temperature T
2d set by the upstream-side target temperature setting unit 403 (step S5).
[0060] When the upstream-side immediate target temperature setting unit 405 determines that
the temperature T
2 is lower than the target temperature T
2d (step S5: NO), the upstream-side immediate target temperature setting unit 405 calculates
a temperature change rate dT
2/dt on the upstream side of the heating portion 33 using the temperatures T
1, T
2, and T
3 and the heat medium flow amounts F
1 and F
2 acquired by the sensor information acquisition unit 401 (step S6). The temperature
T
1 is a temperature of the water flowing through the inflow portion 31. Further, the
temperature T
2 is the temperature of the water on the upstream side of the heating portion 33. Further,
the temperature T
3 is the temperature of the water on the downstream side of the heating portion 33.
Further, the flow amount F
1 is the flow amount of the water flowing through the inflow portion 31. Further, the
flow amount F
2 is the flow amount of the water flowing through the heating portion 33.
[0061] Here, the upstream-side temperature change rate calculation unit 402 calculates the
temperature change rate dT
2/dt by substituting each piece of sensor information into Equation (1) shown below
indicating a heat balance model.
[Equation 1]

[0062] Here, M denotes an amount of the water held in the heating portion 33. Further, cp
n (n is a natural number) denotes a specific heat of the water at a temperature T
n. Since the specific heat is determined by a water temperature, the upstream-side
temperature change rate calculation unit 402 calculates the specific heat cp
n according to the temperature T
n. Further, Q
pump denotes an amount of heat input to the water in the circulation pump 32. Since the
amount of heat from the circulation pump 32 to the water is determined based on the
flow amount F
2 of the water passing through the circulation pump 32, and the number of rotations,
power consumption and characteristics of the circulation pump 32, the upstream-side
temperature change rate calculation unit 402 calculates the input heat amount Q
pump according to these values. Since detection delay is included in the sensor information
detected by each detection unit, the upstream-side temperature change rate calculation
unit 402 may identify the water amount M, the specific heat cp
n and the input heat amount Q
pump based on data of a transient state during actual operation, such that estimation
precision is improved.
[0063] Here, referring to Equation (1), a denominator of a right side of Equation (1) indicates
a heat capacity of the water held in the heating portion 33. Further, a numerator
of the right side of Equation (1) indicates a heat amount of a difference between
a heat amount of water obtained by mixing the water flowing from the inflow portion
31 into the upstream side of the heating portion 33 with the water circulated by the
circulation portion 35 and a heat amount of the water flowing in the heating portion
33. In other words, the temperature change rate dT
2/dt is calculated based on a difference between a temperature of the water obtained
by mixing the water flowing from the inflow portion 31 into the upstream side of the
heating portion 33 with the water circulated by the circulation portion 35 and the
temperature of the water flowing in the heating portion 33.
[0064] Then, the upstream-side immediate target temperature setting unit 405 sets a value
obtained by adding the temperature change rate calculated by the upstream-side temperature
change rate calculation unit 402 to the temperature T
2 acquired by the sensor information acquisition unit 401 as the immediate target temperature
T
2a (step S7). The three-way valve control unit 406 then determines the opening degree
so that the water temperature on the upstream side of the heating portion 33 is the
target temperature T
2a, and controls the three-way valve 34 based on the opening degree (step S8). Accordingly,
the three-way valve control unit 406 can control the opening degree of the three-way
valve 34 at an appropriate temperature change rate according to characteristics (each
portion temperature, a flow amount and a water amount held in the heating portion
33) of the warm water system 30 until the water temperature T
2 on the upstream side of the heating portion 33 reaches the target temperature T
2d. Thereafter, the operation of steps S5 to S8 is repeatedly executed until the temperature
T
2 reaches the target temperature T
2d in step S5.
[0065] When the upstream-side immediate target temperature setting unit 405 determines that
the temperature T
2 reaches the target temperature T
2d in step S5 (step S5: YES), the upstream-side immediate target temperature setting
unit 405 sets the target temperature T
2d as the immediate target temperature T
2a (step S9). The three-way valve control unit 406 then determines the opening degree
so that the water temperature on the upstream side of the heating portion 33 is the
immediate target temperature T
2a, i.e., the target temperature T
2d, and controls the three-way valve 34 based on the opening degree (step S10). Thereafter,
the control device 40 ends the control of the three-way valve 34 in the transient
state, and starts steady-state control to control the opening degree of the three-way
valve 34 based on the target temperature T
2d. The control of the three-way valve 34 in the steady state is the same as the process
of repeatedly executing steps S9 and S10.
[0066] Thus, according to the present embodiment, the three-way valve control unit 406 controls
the opening degree of the three-way valve 34 so that the temperature of the water
on the upstream side of the heating portion 33 increases by a predetermined temperature
until the temperature of the water on the upstream side of the heating portion 33
reaches the target temperature T
2d after the heat pump 20 operates. Accordingly, when the warm water system 30 is in
a transient state, the opening degree of the three-way valve 34 can be controlled
such that an opening and closing operation of the three-way valve 34 can follow the
temperature change of the warm water. Particularly, in the present embodiment, the
predetermined temperature is calculated based on states of the water flowing in the
heating portion 33, the water circulated by the circulation portion 35, and the water
flowing from the inflow portion 31 into the upstream side of the heating portion 33.
Accordingly, the control of the opening degree of the three-way valve 34 can be performed
according to the characteristics of the warm water heating system, and the water temperature
on the upstream side of the heating portion 33 can be increased to the target temperature
T
2a at an appropriate temperature increase rate. Particularly, appropriate control of
the opening degree can be performed using the temperature change rate dT
2/dt, which is the temperature difference between the temperature of the water obtained
by mixing the water from the inflow portion 31 into the upstream side of the heating
portion 33 with the water circulated by the circulation portion 35 and the temperature
of the water flowing in the heating portion 33, as in the present embodiment.
[0067] While the case in which the three-way valve control unit 406 in the present embodiment
performs the control of the opening degree using the temperature change rate dT
2/dt calculated by the upstream-side temperature change rate calculation unit 402 has
been described, the present invention is not limited thereto and the three-way valve
control unit 406 may control the opening degree of the three-way valve 34 so that
the water temperature on the upstream side of the heating portion 33 increases by
another predetermined temperature. However, when the predetermined temperature is
set to be too low, the opening degree to the outflow portion 36 is controlled to be
large such that temperature increase of the water temperature on the upstream side
of the heating portion 33 becomes slow and it takes time for the warm water system
30 to transition to the steady state. On the other hand, when the predetermined temperature
is set to be excessively high, the opening degree to the circulation portion 35 is
controlled to be large such that the temperature increase of the water temperature
on the upstream side of the heating portion 33 becomes fast and the opening and closing
operation of the three-way valve 34 may not follow the temperature change of the warm
water. In this case, the amount of heat exchanged in the condenser 24 of the heat
pump 20 may decrease and the efficiency of the warm water heating system may become
low.
(Second embodiment)
[0068] Next, a second embodiment of the present invention will be described. A warm water
heating system according to the second embodiment sets the target temperature on the
upstream side of the heating portion 33 of the warm water system 30 based on the characteristics
of the heat source system 10 and the warm water system 30.
[0069] Fig. 4 is a schematic configuration diagram of the warm water heating system according
to the second embodiment of the present invention.
[0070] The warm water heating system according to the second embodiment includes a heat
source upstream-side temperature detector 56 and a heat source flow amount detector
57, in addition to the heat source system 10 of the warm water heating system according
to the first embodiment, and operation of the control device 40 is different.
[0071] The heat source upstream-side temperature detector 56 detects a temperature T
4 of hot water on the upstream side of the heat source system 10.
[0072] The heat source flow amount detector 57 detects a flow amount F
3 of the hot water flowing through the heat source system 10.
[0073] Fig. 5 is a schematic block diagram showing a configuration of a control device 40
according to the second embodiment of the present invention.
[0074] The control device 40 according to the second embodiment includes a downstream-side
target temperature setting unit 407, in addition to the configuration of the control
device 40 according to the first embodiment, and operation of the upstream-side target
temperature setting unit 403 is different.
[0075] The downstream-side target temperature setting unit 407 sets a target temperature
of the water on the downstream side of the heating portion 33 when the warm water
system 30 enters a steady state if the heat pump 20 and the warm water system 30 operate.
[0076] The upstream-side target temperature setting unit 403 sets a target temperature of
the water on the upstream side of the heating portion 33 when the warm water system
30 enters the steady state, based on the target temperature on the downstream side,
and the sensor information acquired by the sensor information acquisition unit 401.
[0077] Next, operation of the control device 40 at the time of operation start of the warm
water heating system according to the present embodiment will be described.
[0078] The operation of the control device 40 according to the second embodiment differs
in operation of step S1 from the operation of the control device 40 in the first embodiment,
and operation after step S1 is the same as that in the first embodiment.
[0079] Therefore, the operation of step S1 in the second embodiment will be described herein.
[0080] First, the downstream-side target temperature setting unit 407 of the control device
40 receives input of a target temperature T
3d on a downstream side of the heating portion 33 from a manager before operation start
of the warm water heating system. Then, the upstream-side target temperature setting
unit 403 acquires a temperature T4 and a flow amount F
3 detected by the heat source upstream-side temperature detector 56 and the heat source
flow amount detector 57 from the sensor information acquisition unit 401. Also, the
upstream-side target temperature setting unit 403 calculates a maximum heating amount
of the condenser 24 at the time of maximum output of the heat pump 20 based on the
acquired temperature T
4 and flow amount F
3. Then, the upstream-side target temperature setting unit 403 calculates a target
temperature T
2d on the upstream side of the heating portion 33 based on the calculated maximum heating
amount, the flow amount F
2 of the water flowing in the heating portion 33, and the target temperature T
3d on the downstream side. Specifically, the upstream-side target temperature setting
unit 403 sets, as the target temperature T
2d, the water temperature on the upstream side of the heating portion 33 required for
setting the water temperature on the downstream side of the heating portion 33 as
a target temperature T
3d based on the maximum output of the heat pump 20.
[0081] Thereafter, a process after step S2 is executed as in the first embodiment, such
that the temperature of the warm water system 30 can be controlled to utilize maximum
capacity of the heat pump 20 according to a condition of the heat source system 10.
(Third embodiment)
[0082] Next, a third embodiment of the present invention will be described. A warm water
heating system according to the third embodiment controls an opening degree (an adjustment
amount of heat pump control) of a vane 23 of a heat pump 20 based on the temperature
on a downstream side of a heating portion 33 of a warm water system 30.
[0083] Fig. 6 is a schematic configuration diagram of the warm water heating system according
to the third embodiment of the present invention.
[0084] The warm water heating system according to the third embodiment includes a condenser
temperature detector 58, in addition to the warm water system 30 of the warm water
heating system according to the first embodiment, and operation of the control device
40 is different. Further, the warm water heating system according to the third embodiment
may not include the inflow portion temperature detector 52 and the inflow portion
flow amount detector 51.
[0085] The condenser temperature detector 58 detects a temperature T
5 of the condenser 24 of the heat pump 20.
[0086] Fig. 7 is a schematic block diagram showing a configuration of the control device
40 according to the third embodiment of the present invention.
[0087] The control device 40 according to the third embodiment includes a sensor information
acquisition unit 401, a downstream-side temperature change rate calculation unit 408
(heat pump adjustment temperature calculation unit), a downstream-side target temperature
setting unit 407, a downstream-side immediate target temperature setting unit 409,
and a vane control unit 410 (heat pump adjustment amount determination unit).
[0088] The sensor information acquisition unit 401 acquires sensor information (a flow amount
or a temperature) detected by each detector provided in the warm water system 30 and
the condenser 24.
[0089] The downstream-side temperature change rate calculation unit 408 calculates a change
rate (a heat pump adjustment temperature) of the water temperature on the downstream
side of the heating portion 33, i.e., an increase rate of the water temperature, based
on the sensor information acquired by the sensor information acquisition unit 401.
The change rate of the water temperature is calculated by applying the sensor information
to a heat balance model.
[0090] The downstream-side target temperature setting unit 407 sets a target temperature
of the water on the downstream side of the heating portion 33 when the warm water
system 30 enters a steady state if the heat pump 20 operates.
[0091] The downstream-side immediate target temperature setting unit 409 sets an immediate
target temperature of the water on the downstream side of the heating portion 33 at
a current time according to the information acquired from the sensor information acquisition
unit 401, the downstream-side temperature change rate calculation unit 408 and the
downstream-side target temperature setting unit 407. Specifically, the downstream-side
immediate target temperature setting unit 409 sets the immediate target temperature
based on the temperature change rate calculated by the downstream-side temperature
change rate calculation unit 408 until a current water temperature on the downstream
side of the heating portion 33 reaches the downstream-side target temperature. Also,
the downstream-side immediate target temperature setting unit 409 sets the target
temperature set by the downstream-side target temperature setting unit 407 as the
immediate target temperature after the current water temperature on the downstream
side of the heating portion 33 reaches the downstream-side target temperature.
[0092] The vane control unit 410 performs control of the opening degree of the vane 23 through
PID control based on the immediate target temperature set by the downstream-side immediate
target temperature setting unit 409 and the current water temperature on the downstream
side of the current heating portion 33.
[0093] Next, operation of the control device 40 at the time of operation start of the warm
water heating system according to the present embodiment will be described.
[0094] Fig. 8 is a flowchart showing operation of the control device 40 according to the
third embodiment of the present invention.
[0095] First, the downstream-side target temperature setting unit 407 of the control device
40 receives input of a target temperature T
3d on the downstream side of the heating portion 33 from a manager before operation
start of the warm water heating system (step S11).
[0096] The manager of the warm water heating system operates the warm water system 30 and
then operates the compressor 22 after the setting of the target temperature.
[0097] The downstream-side immediate target temperature setting unit 409 acquires a temperature
T
3 detected by the heating portion downstream-side temperature detector 55 from the
sensor information acquisition unit 401. The downstream-side immediate target temperature
setting unit 409 then determines whether the temperature T
3 reaches the target temperature T
3d set by the downstream-side target temperature setting unit 407 (step S12).
[0098] When the downstream-side immediate target temperature setting unit 409 determines
that the temperature T
3 is lower than the target temperature T
3d (step S12: NO), the downstream-side immediate target temperature setting unit 409
calculates a temperature change rate dT
3/dt on the downstream side of the heating portion 33 using temperatures T
2, T
3, and T
5 and a heat medium flow amount F
2 acquired by the sensor information acquisition unit 401 (step S13). The temperature
T
2 is a temperature of the water on the upstream side of the heating portion 33. Further,
the temperature T
3 is a temperature of the water on the downstream side of the heating portion 33. Further,
the temperature T
5 is a temperature of the heat medium in the condenser 24. Further, the flow amount
F
2 is a flow amount of the water flowing through the heating portion 33.
[0099] Here, the downstream-side temperature change rate calculation unit 408 calculates
the temperature change rate dT
3/dt by substituting each piece of sensor information into Equation (2) shown below
indicating a heat balance model.
[Equation 2]

[0100] Here, U and A denote a general heat transfer coefficient and a heat transfer area
of the condenser 24, respectively. While values of U and A may be calculated as design
values of the heat pump 20 in advance, the present invention is not limited thereto
and the values may be identified from the data in a steady state during an actual
operation. U and A can be calculated through calculation of Equation (3) shown below.
[Equation 3]

[0101] Here, referring to Equation (2), a denominator of a right side of Equation (2) indicates
a heat capacity of the water held in the heating portion 33. Further, a numerator
of the right side of Equation (2) indicates a heat amount of a difference between
a sum of a heat amount of water flowing in the heating portion 33 and a heat amount
heated in the heating portion 33 and a heat amount of the water flowing from the heating
portion 33 into the three-way valve 34. In other words, the temperature change rate
dT
3/dt is calculated based on a difference between a temperature of the water when the
water flowing in the heating portion 33 is heated by the heating portion 33 and the
temperature of the water flowing from the heating portion 33 into the three-way valve
34.
[0102] The downstream-side immediate target temperature setting unit 409 then sets, as an
immediate target temperature T
3a, a value obtained by adding the temperature change rate calculated by the downstream-side
temperature change rate calculation unit 408 to the temperature T
3 acquired by the sensor information acquisition unit 401 (step S14). The vane control
unit 410 then determines the opening degree of the vane 23 so that the water temperature
on a downstream side of the heating portion 33 becomes the immediate target temperature
T
3a, and controls the vane 23 to the opening degree (step S15). Accordingly, the vane
control unit 410 can control the opening degree of the vane 23 at an appropriate temperature
change rate according to characteristics of the heating portion 33 until the water
temperature T
3 on the downstream side of the heating portion 33 reaches the target temperature T
3d. Thereafter, the operation of steps S12 to S15 is repeatedly performed until the
temperature T3 reaches the target temperature T
3d in step S12.
[0103] When the downstream-side immediate target temperature setting unit 409 determines
that the temperature T
3 reaches the target temperature T
3d in step S12 (step S12: YES), the downstream-side immediate target temperature setting
unit 409 sets the target temperature T
3d to the immediate target temperature T
3a (step S16). The vane control unit 410 then determines the opening degree so that
the water temperature on the downstream side of the heating portion 33 is the immediate
target temperature T
3a, i.e., the target temperature T
3d, and controls the vane 23 with the opening degree (step S17). Thereafter, the control
device 40 ends the control of the compressor 22 in the transient state, and starts
steady-state control to control the opening degree of the vane 23 based on target
temperature T
3d. The control of the vane 23 in the steady state is the same as the process of repeatedly
executing steps S16 and S17.
[0104] Thus, according to the present embodiment, the vane control unit 410 controls the
opening degree of the vane 23 so that the temperature of the water on the downstream
side of the heating portion 33 increases by a predetermined temperature until the
temperature of the water on the downstream side of the heating portion 33 reaches
the target temperature T
3d after the heat pump 20 operates. Accordingly, when the warm water system 30 is in
a transient state, the opening degree of the vane 23 can be controlled so that the
opening degree control of the vane 23 can follow the temperature change of the warm
water. Particularly, in the present embodiment, the predetermined temperature is calculated
based on the state of the water flowing in the heating portion 33 and the state of
the water flowing from the heating portion 33 into the three-way valve 34, and the
heating amount in the heating portion 33. Accordingly, the control of the opening
degree of the vane 23 can be performed according to the characteristics of the warm
water heating system, and the water temperature on the downstream side of the heating
portion 33 can increase to the target temperature T
3a at an appropriate temperature increase rate. Particularly, as shown in the present
embodiment, appropriate control of the opening degree can be performed using the temperature
change rate dT
3/dt, which is the temperature difference between the temperature of the water when
the water flowing in the heating portion 33 is heated by the heating portion 33 and
the temperature of the water flowing from the heating portion 33 into the three-way
valve 34.
[0105] While the case in which the vane control unit 410 in the present embodiment performs
control of the opening degree using the temperature change rate dT
3/dt calculated by the downstream-side temperature change rate calculation unit 408
has been described, the present invention is not limited thereto and the opening degree
of the vane 23 may be controlled so that the water temperature on the downstream side
of the heating portion 33 increases by another predetermined temperature. However,
when the predetermined temperature is set to be too low, the increase rate of the
opening degree is controlled to be suppressed, a speed of a temperature increase of
the water temperature on the downstream side of the heating portion 33 decreases,
and it takes time for the warm water system 30 to transition to the steady state.
On the other hand, when the predetermined temperature is set to be excessively high,
the increase rate of the opening degree is controlled to be high, the speed of the
temperature increase of the water temperature on the downstream side of the heating
portion 33 increases, and the opening degree control of the vane 23 may not follow
the temperature change of the warm water. In this case, the amount of heat exchanged
in the condenser 24 of the heat pump 20 may become small, and efficiency of the warm
water heating system may become low.
(Fourth embodiment)
[0106] Next, a fourth embodiment of the present invention will be described. A warm water
heating system according to the fourth embodiment controls the opening degree of the
vane 23 of the heat pump 20 based on a state of the heating portion 33 of the warm
water system 30 as in the third embodiment while controlling the opening degree of
the three-way valve 34 based on the state of the warm water system 30 as in the second
embodiment.
[0107] Fig. 9 is a schematic configuration diagram of the warm water heating system according
to the fourth embodiment of the present invention.
[0108] The warm water heating system according to the fourth embodiment has both the configuration
of the warm water heating system according to the second embodiment and the configuration
of the warm water heating system according to the third embodiment. The configuration
of the control device 40 according to the fourth embodiment may also have both the
configuration of the control device 40 according to the second embodiment and the
configuration of the control device 40 according to the third embodiment.
[0109] Operation of the warm water heating system according to the fourth embodiment includes
the operation of the second embodiment and the operation of the third embodiment.
[0110] Specifically, when the setting of the downstream-side target temperature in step
S11 of the third embodiment is performed, calculation of the upstream-side target
temperature in step S1 of the second embodiment is performed using the downstream-side
target temperature.
[0111] Further, in steps S2 to S4 according to the second embodiment, the control device
40 performs only opening degree control of the three-way valve 34. On the other hand,
the control device 40 executes the process of steps S12 to S15 according to the third
embodiment in parallel while executing the process of steps S5 to S8. Also, the control
device 40 performs the process of steps S16 and S17 according to the third embodiment
when executing the process of steps S9 and S10 according to the second embodiment.
[0112] Accordingly, the control device 40 can appropriately control the opening degree of
the three-way valve 34 and the opening degree of the vane 23.
[0113] While the embodiments of the present invention have been described above in detail
with reference to the drawings, a specific configuration is not limited to the foregoing,
and various design changes or the like can be made without departing from the present
invention as defined in the claims.
[0114] The control device 40 described above includes a computer system therein. Also,
the above process is performed by storing the operation of each processing unit described
above in a computer-readable recording medium in the form of a program and by a computer
reading and executing this program. Here, the computer-readable recording medium refers
to a magnetic disk, a magneto-optical disc, a CD-ROM, a DVD-ROM, a semiconductor memory,
or the like. Further, this computer program may be distributed to a computer by a
communication line, and the computer receiving this distribution may execute the program.
[0115] Further, the above program may be intended to realize some of the functions described
above.
[0116] Further, the program may be a program capable of realizing the above-described functions
through a combination with a program previously recorded in a computer system, i.e.,
a differential file (a differential program).
[Industrial Applicability]
[0117] The present invention provides a control device for controlling a warm water heating
system including a heat pump including a heat output heat exchanger which takes heat
from a heat source system and outputs heat, a heating portion which heats water using
the heat obtained from the heat output heat exchanger, an outflow portion which flows
the water heated by the heating portion to a heating target, a circulation portion
which circulates the water heated by the heating portion to an upstream side of the
heating portion, an inflow portion which flows water from the heating target into
the upstream side of the heating portion, and an adjustment unit which adjusts flow
amount distribution of the water from the heating portion to the outflow portion and
the circulation portion, wherein the control device includes an upstream-side target
temperature setting unit which sets a target temperature of the water on the upstream
side of the heating portion, and an adjustment amount determination unit which determines
an adjustment amount of the flow amount distribution by the adjustment unit so that
the temperature of the water on the upstream side of the heating portion increases
by a predetermined temperature until a temperature of the water on the upstream side
of the heating portion reaches the target temperature. According to the present invention,
the adjustment amount in the adjustment unit or the adjustment amount of the heat
pump is determined so that the temperature of the warm water on the upstream side
or the downstream side of the heating portion increases by a predetermined temperature
until a temperature of the warm water on the upstream side of the heating portion
reaches the target temperature. Accordingly, it is possible to appropriately control
the temperature increase rate in the transient state of the warm water system.
[Reference Signs List]
[0118]
- 10
- Heat source system
- 20
- Heat pump
- 21
- Evaporator
- 22
- Compressor
- 24
- Condenser
- 25
- Expansion valve
- 30
- Warm water system
- 31
- Inflow portion
- 32
- Circulation pump
- 33
- Heating portion
- 34
- Three-way valve
- 35
- Circulation portion
- 36
- Outflow portion
- 40
- Control device
- 51
- Inflow portion flow amount detector
- 52
- Inflow portion temperature detector
- 53
- Heating portion flow amount detector
- 54
- Heating portion upstream-side temperature detector
- 55
- Heating portion downstream-side temperature detector
- 56
- Heat source upstream-side temperature detector
- 57
- Heat source flow amount detector
- 58
- Condenser temperature detector
- 401
- Sensor information acquisition unit
- 402
- Upstream-side temperature change rate calculation unit
- 403
- Upstream-side target temperature setting unit
- 404
- Heat pump information input unit
- 405
- Upstream-side immediate target temperature setting unit
- 406
- Three-way valve control unit
- 407
- Downstream-side target temperature setting unit
- 408
- Downstream-side temperature change rate calculation unit
- 409
- Downstream-side immediate target temperature setting unit
- 410
- Vane control unit
1. Steuerungsvorrichtung (40) zum Steuern eines Warmwasserheizsystems, wobei die Steuerungsvorrichtung
(40) umfasst:
eine Wärmepumpe (20), die einen Wärmeabgabe-Wärmetauscher (24) enthält, der Wärme
aus einem Wärmequellensystem (10) aufnimmt und Wärme abgibt,
einen Heizungsabschnitt (33), der Wasser mittels der Wärme erwärmt, die von dem Wärmeabgabe-Wärmetauscher
(24) erhalten wird,
einen Ausströmabschnitt (36), der das durch den Heizungsabschnitt (33) erwärmte Wasser
zu einem Heizungsziel leitet,
einen Zirkulierungsabschnitt (35), der das durch den Heizungsabschnitt (33) erwärmte
Wasser zu einer stromaufwärtigen Seite des Heizungsabschnitts (33) zirkuliert,
einen Einströmabschnitt (31), der Wasser von dem Heizungsziel in die stromaufwärtige
Seite des Heizungsabschnitts (33) leitet, und
eine Justiereinheit (34), die eine Strömungsmengenverteilung des Wassers von dem Heizungsabschnitt
(33) zu dem Ausströmabschnitt (36) und den Zirkulierungsabschnitt (35) justiert,
dadurch gekennzeichnet, dass die Steuerungsvorrichtung (40) eine stromaufwärtsseitige Solltemperatureinstelleinheit
(403) enthält, die eine Solltemperatur des Wassers auf der stromaufwärtigen Seite
des Heizungsabschnitts (33) einstellt, und
eine Justierbetragsbestimmungseinheit (406), die einen Justierbetrag der Strömungsmengenverteilung
durch die Justiereinheit (34) so bestimmt, dass eine Temperatur des Wassers auf der
stromaufwärtigen Seite des Heizungsabschnitts (33) um eine vorgegebene Temperatur
steigt, bis die Temperatur des Wassers auf der stromaufwärtigen Seite des Heizungsabschnitts
(33) die Solltemperatur erreicht, und wobei die Justierbetragsbestimmungseinheit (406)
den Justierbetrag der Strömungsmengenverteilung durch die Justiereinheit (34) so bestimmt,
dass die Temperatur des Wassers auf der stromaufwärtigen Seite des Heizungsabschnitts
(33) um eine vorgegebene Temperatur, die auf der Basis von Zuständen von Wasser, das
in dem Heizungsabschnitt (33) strömt, Wasser, das durch den Zirkulierungsabschnitt
(35) strömt, und Wasser, das von dem Einströmabschnitt (31) in die stromaufwärtige
Seite des Heizungsabschnitts (33) strömt, berechnet wird, steigt, bis die Temperatur
des Wassers auf der stromaufwärtigen Seite des Heizungsabschnitts (33) die Solltemperatur
erreicht.
2. Steuerungsvorrichtung (40) nach Anspruch 1, die ferner eine Justiertemperaturberechnungseinheit
(402) umfasst, die als eine Justiertemperatur, die für die Bestimmung des Justierbetrages
verwendet wird, eine Temperaturdifferenz zwischen einer Temperatur von Wasser, die
durch Vermischen von Wasser, das von dem Einströmabschnitt (31) in die stromaufwärtige
Seite des Heizungsabschnitts (33) strömt, mit Wasser, das durch den Zirkulierungsabschnitt
(35) strömt, erhalten wird, und der Temperatur des Wassers, das in dem Heizungsabschnitt
(33) strömt, auf der Basis der Zustände des Wassers, das in dem Heizungsabschnitt
(33) strömt, des Wassers, das durch den Zirkulierungsabschnitt (35) strömt, und des
Wassers, das von dem Einströmabschnitt (31) in die stromaufwärtige Seite des Heizungsabschnitts
(33) strömt, berechnet,
wobei die Justierbetragsbestimmungseinheit (406) den Justierbetrag der Strömungsmengenverteilung
durch die Justiereinheit (34) so bestimmt, dass die Temperatur des Wassers auf der
stromaufwärtigen Seite des Heizungsabschnitts (33) um die durch die Justiertemperaturberechnungseinheit
(402) berechnete Justiertemperatur steigt, bis die Temperatur des Wassers auf der
stromaufwärtigen Seite des Heizungsabschnitts (33) die Solltemperatur erreicht.
3. Steuerungsvorrichtung (40) nach einem der Ansprüche 1 bis 2, wobei die Justierbetragsbestimmungseinheit
(406) den Justierbetrag der Strömungsmengenverteilung durch die Justiereinheit (34)
so bestimmt, dass die Temperatur des Wassers, das in den Heizungsabschnitt (33) strömt,
konstant wird, bis die Wärmepumpe (20) arbeitet.
4. Steuerungsvorrichtung (40) nach einem der Ansprüche 1 bis 3, wobei die stromaufwärtsseitige
Solltemperatureinstelleinheit (403) eine Solltemperatur des Wassers auf der stromaufwärtigen
Seite des Heizungsabschnitts (33) auf der Basis eines maximalen Heizbetrages in dem
Heizungsabschnitt (33), einer Strömungsmenge des Wassers, das in den Heizungsabschnitt
(33) strömt, und einer Solltemperatur des Wassers auf einer stromabwärtigen Seite
des Heizungsabschnitts (33) einstellt.
5. Steuerungsvorrichtung (40) nach einem der Ansprüche 1 bis 4, ferner umfassend:
eine stromabwärtsseitige Solltemperatureinstelleinheit (407), die eine Solltemperatur
des Wassers auf der stromabwärtigen Seite des Heizungsabschnitts (33) einstellt, und
eine Wärmepumpenjustierbetragsbestimmungseinheit (410), die einen Justierbetrag der
Wärmepumpensteuerung so bestimmt, dass die Temperatur des Wassers auf der stromabwärtigen
Seite des Heizungsabschnitts (33) um eine vorgegebene Temperatur steigt, bis die Temperatur
des Wassers auf der stromabwärtigen Seite des Heizungsabschnitts (33) die Solltemperatur
erreicht.
6. Steuerungsvorrichtung (40) nach Anspruch 5, wobei die Wärmepumpenjustierbetragsbestimmungseinheit
(410) den Justierbetrag der Wärmepumpensteuerung so bestimmt, dass die Temperatur
des Wassers auf der stromabwärtigen Seite des Heizungsabschnitts (33) um eine vorgegebene
Temperatur, die auf der Basis eines Zustands des Wassers, das in dem Heizungsabschnitt
(33) strömt und das von dem Heizungsabschnitt (33) in die Justiereinheit (34) strömt,
und eines Heizbetrages in dem Heizungsabschnitt (33) berechnet wird, steigt, bis die
Temperatur des Wassers auf der stromabwärtigen Seite des Heizungsabschnitts (33) die
Solltemperatur erreicht.
7. Steuerungsvorrichtung (40) nach Anspruch 6, die ferner eine Wärmepumpenjustiertemperaturberechnungseinheit
(408) umfasst, die als eine Wärmepumpenjustiertemperatur, die für die Bestimmung des
Justierbetrages der Wärmepumpensteuerung verwendet wird, eine Temperaturdifferenz
zwischen der Temperatur des Wassers, das in dem Heizungsabschnitt (33) strömt, wenn
das Wasser durch den Heizungsabschnitt (33) erwärmt wird, und der Temperatur des Wassers,
das von dem Heizungsabschnitt (33) in die Justiereinheit (34) strömt, auf der Basis
des Zustands des Wassers, das in dem Heizungsabschnitt (33) strömt, des Zustands des
Wassers, das von dem Heizungsabschnitt (33) in die Justiereinheit (34) strömt, und
eines Heizbetrages in dem Heizungsabschnitt berechnet,
wobei die Wärmepumpenjustierbetragsbestimmungseinheit (410) den Justierbetrag der
Wärmepumpensteuerung (23) so bestimmt, dass die Temperatur des Wassers auf der stromabwärtigen
Seite des Heizungsabschnitts (33) um die durch die Wärmepumpenjustiertemperaturberechnungseinheit
(408) berechnete Wärmepumpenjustiertemperatur steigt, bis die Temperatur des Wassers
auf der stromabwärtigen Seite des Heizungsabschnitts (33) die Solltemperatur erreicht.
8. Warmwasserheizsystem, umfassend:
eine Wärmepumpe (20), die einen Wärmeabgabe-Wärmetauscher (24) enthält, der Wärme
aus einem Wärmequellensystem (10) entnimmt und Wärme abgibt,
einen Heizungsabschnitt (33), der Wasser mittels der Wärme erwärmt, die von dem Wärmeabgabe-Wärmetauscher
(24) erhalten wird,
einen Ausströmabschnitt (36), der das durch den Heizungsabschnitt (33) erwärmte Wasser
zu einem Heizungsziel leitet,
einen Zirkulierungsabschnitt (35), der das durch den Heizungsabschnitt (33) erwärmte
Wasser zu einer stromaufwärtigen Seite des Heizungsabschnitts (33) zirkuliert,
einen Einströmabschnitt (31), der Wasser von dem Heizungsziel in die stromaufwärtige
Seite des Heizungsabschnitts (33) leitet,
eine Justiereinheit (34), die eine Strömungsmengenverteilung des Wassers von dem Heizungsabschnitt
(33) zu dem Zirkulierungsabschnitt (35) und dem Ausströmabschnitt (36) justiert, und
die Steuerungsvorrichtung (40) nach einem der Ansprüche 1 bis 7.
9. Steuerungsverfahren zum Steuern eines Justierbetrages einer Justiereinheit (34) eines
Warmwasserheizsystems, umfassend:
eine Wärmepumpe (20), die einen Wärmeabgabe-Wärmetauscher (24) enthält, der Wärme
aus einem Wärmequellensystem (10) aufnimmt und Wärme abgibt,
einen Heizungsabschnitt (33), der Wasser mittels der Wärme erwärmt, die von dem Wärmeabgabe-Wärmetauscher
(24) erhalten wird,
einen Ausströmabschnitt (36), der das durch den Heizungsabschnitt (33) erwärmte Wasser
zu einem Heizungsziel leitet,
einen Zirkulierungsabschnitt (35), der das durch den Heizungsabschnitt (33) erwärmte
Wasser zu einer stromaufwärtigen Seite des Heizungsabschnitts (33) zirkuliert,
eine Einströmabschnitt (31), die Wasser von dem Heizungsziel in die stromaufwärtige
Seite des Heizungsabschnitts (33) leitet, und
die Justiereinheit (34), die eine Strömungsmengenverteilung des Wassers von dem Heizungsabschnitt
(33) zu dem Zirkulierungsabschnitt (35) und dem Ausströmabschnitt (36) justiert,
dadurch gekennzeichnet, dass das Steuerungsverfahren umfasst:
Bestimmen einer Solltemperatur des Wassers auf der stromaufwärtigen Seite des Heizungsabschnitts
(33), und
Bestimmen eines Justierbetrages der Strömungsmengenverteilung durch die Justiereinheit
(34) dergestalt, dass eine Temperatur des Wassers auf der stromaufwärtigen Seite des
Heizungsabschnitts (33) um eine vorgegebene Temperatur steigt, bis die Temperatur
des Wassers auf der stromaufwärtigen Seite des Heizungsabschnitts (33) die Solltemperatur
erreicht, wobei der Justierbetrag so bestimmt wird, dass die Temperatur des Wassers
auf der stromaufwärtigen Seite des Heizungsabschnitts (33) um die vorgegebene Temperatur,
die auf der Basis der Zustände von Wasser, das in dem Heizungsabschnitt (33) strömt,
Wasser, das durch den Zirkulierungsabschnitt (35) strömt, und Wasser, das von dem
Einströmabschnitt (31) in die stromaufwärtige Seite des Heizungsabschnitts (33) strömt,
berechnet wird, steigt, bis die Temperatur des Wassers auf der stromaufwärtigen Seite
des Heizungsabschnitts (33) die Solltemperatur erreicht.