[0001] The present invention relates to a binary power generation systems, which generate
electricity with a low-temperature heat source such as hot spring water, and in particular,
relates to a binary power generation system including an intermediate heat exchanger.
[0002] Conventionally, binary power generation systems use a low-temperature (100°C to 150°C,
for example) heat source such as hot spring and industrial waste heat is known. In
the binary power generation systems, heat of the heat source is imparted through a
heat exchanger to a low-boiling medium which is a working medium, which brings the
medium to a boil and creates vapor pressure. The binary power generation systems use
this vapor pressure to rotate a turbine and thus generate power. Due to its structure,
however, binary power generation is low in energy efficiency and requires a large
number of heat sources to generate a small amount of electricity. The binary power
generation therefore has difficulty in ensuring heat sources.
[0003] With an aim to solve the foregoing problem, for example, the binary power generation
system disclosed in Patent Document 1 is suggested to improve a heat-energy use efficiency
overall in the binary power generation system and enhance power-generation efficiency.
[0004] Patent Document 1: Japanese Patent Application Publication (Kokai) No. 2014-177922
[0005] The binary power generation system disclosed in Patent Document 1 requires two kinds
of heat sources different in temperature, which makes the system complicated. The
system therefore needs to be of large size, which incurs high manufacturing cost.
[0006] In light of the issues mentioned above, the present invention is directed to an object
of providing a binary power generation system which is compact in size and improved
in power-generation efficiency.
[0007] The invention solves the issues as described below. A first invention provides a
binary power generation system. The binary power generation system includes an evaporator
configured to heat a low-boiling medium and turn a liquid state into a vapor state;
an expander configured to be activated by expansion of a vaporous low-boiling medium
discharged from the evaporator; a generator configured to generate power by the expander
being activated; a condenser configured to liquefy the vaporous low-boiling medium
discharged from the expander; a pump for circulating the low-boiling medium; a closed-loop
circulation pathway including the evaporator, the expander, the condenser, and the
pump; and an intermediate heat exchanger configured to exchange heat between the vaporous
low-boiling medium which is discharged from the expander and is still not flown into
the condenser, and a liquid low-boiling medium which is discharged from the pump and
is still not flown into the evaporator.
[0008] In a second invention according to the first invention, the circulation pathway includes
bypasses connecting the expander to the condenser, and the pump to the evaporator,
without passing through the intermediate heat exchanger. The binary power generation
system further includes a first temperature measuring device configured to measure
temperature T1 of the liquid low-boiling medium discharged from the pump; a second
temperature measuring device configured to measure temperature T2 of the vaporous
low-boiling medium discharged from the expander; and a medium flow-path switching
device configured to switch a flow path of the low-boiling medium between a fist pathway
passing through the intermediate heat exchanger and a second pathway which follows
the bypass without passing though the intermediate heat exchanger. The medium flow-path
switching device is configured to switch the flow path of the low-boiling medium from
the first pathway to the second pathway when a difference between the temperature
T1 and the temperature T2 is smaller than a predetermined temperature difference.
[0009] In a third invention, the expander is a scroll expander including a fixed scroll
and an orbiting scroll. The vaporous low-boiling medium is introduced from a central
portion into a gas pocket which is formed by spiral-shaped fixed and orbiting wraps
provided in the fixed and orbiting scrolls being meshed with each other.
[0010] The binary power generation system of the present invention is capable of cooling
the low-boiling medium which has not yet flown into the condenser and simultaneously
heating the low-boiling medium which has not yet flown into the evaporator. This makes
it possible to improve condensation and evaporation efficiencies and improve power-generation
efficiency overall in the system. It is then further possible to downsize the binary
power generation system and reduce manufacturing cost.
Fig. 1 illustrates a configuration of a binary power generation system according to
an embodiment of the present invention.
Fig. 2 illustrates a configuration of a binary power generation system according to
another embodiment of the present invention.
[0011] An embodiment of the present invention will be described below with reference to
the accompanying drawings. A binary power generation system 1 includes an evaporator
10, an expander 20, a generator 60, a condenser 30, a pump 40, a single intermediate
heat exchanger 70, and a circulation pathway 50 including the foregoing elements.
The evaporator 10 heats a low-boiling medium 90 and turns a liquid state into a vapor
state by using hot water 100 drawn from a hot source. The hot water 100 serves as
a heat source. Examples of the hot source include hot spring. The expander 20 expands
the vaporous low-boiling medium 90 discharged from the evaporator 10 to generate rotational
driving energy. The generator 60 uses rotational driving energy generated with the
expander 20 to generate power. The condenser 30 condenses the vaporous low-boiling
medium 90 discharged from the expander 20 in an expanded state into a liquid state.
The pump 40 circulates the low-boiling medium 90 liquefied in and discharged from
the condenser 30. The intermediate heat exchanger 70 cools the vaporous low-boiling
medium 90 which has been discharged from the expander 20 and has not yet flown into
the condenser 30. The intermediate heat exchanger 70 heats the liquid low-boiling
medium 90 which has been discharged from the pump 40 and has not yet flown into the
evaporator 10. The circulation pathway 50 has a closed-loop configuration wherein
the low-boiling medium 90 flows through the evaporator 10, the expander 20, the intermediate
heat exchanger 70, the condenser 30, and the pump 40 in the order named and returns
to the evaporator 10 through the intermediate heat exchanger 70.
[0012] In the binary power generation system 1 illustrated in Fig. 1, examples of the low-boiling
medium 90 includes an inert gas consisting mainly of chlorofluorocarbon having no
global warming potential such as HFC-245fa and HFC-134A, hydrocarbon such as pentane,
a mixture of water and ammonia. In particular, HFC-245fa is suitable for serving as
the low-boiling medium 90. However, examples of the low-boiling medium 90 are not
limited to the foregoing substances.
[0013] The evaporator 10 exchanges heat between the hot water 100 drawn from the hot source
and the circulation pathway 50, heats the low-boiling medium 90, and turns the liquid
state into the vapor state. The hot water 100 may be, for example, hot spring water.
The hot water 100 may be fresh water which is heated by exchanging heat with hot spring
water to prevent scale present in the hot spring water from depositing and negatively
affecting the binary power generation system 1.
[0014] The vaporous low-boiling medium 90 which has been discharged from the evaporator
10 passes through the circulation pathway 50 and flows into the expander 20.
[0015] In one example, the expander 20 may be a displacement-type expander. Examples of
the displacement-type expander include, but are not limited to, a scroll expander,
a screw expander, a claw expander, a reciprocating expander, a Roots-type expander.
In particular, the scroll expander including fixed and orbiting scrolls is suitable
for serving as the displacement-type expander, which has been disclosed by Japanese
Patent Application Publication (Kokai) No. 2012-007518 which is a publicly known document.
The expander 20 converts expansion energy of the vaporous low-boiling medium 90 flown
into the expander 20 into rotary motion. The generator 60 produces power with the
rotary motion.
[0016] When the scroll expander is used, a hyperbaric vaporous low-boiling medium 90 is
introduced from a central portion of the fixed scroll into a gas pocket. The gas pocket
is formed by meshing a spiral shaped orbiting wrap provided in an orbiting scroll
with a spiral shaped fixed wrap-provided in a fixed scroll. The orbiting scroll is
then brought into orbital motion due to energy caused during the vapor expansion.
An orbital force of the orbiting scroll is transmitted to the generator 60 mounted
on a shaft of the expander to generate power. The scroll expander thus configured
may provide high noise reduction. The size of the scroll expander may be small compared
with that of a turbine expander, and further the energy needed to drive the scroll
expander is low compared with the required energy in the turbine expander.
[0017] The vaporous low-boiling medium 90 discharged from the expander 20 passes through
the circulation pathway 50 and flows into the intermediate heat exchanger 70, the
details of which will be described below. The vaporous low-boiling medium 90 flown
into the intermediate heat exchanger 70 is then cooled with the intermediate heat
exchanger 70.
[0018] The condenser 30 exchanges heat between the vaporous low-boiling medium 90 which
has been expanded in the expander 20 and then cooled with the intermediate heat exchanger
70 and cooling water 200 drawn from a cold source to further cool the vaporous low-boiling
medium 90 and turn the vaporous state into the liquid state. Examples of the cooling
water 200 include groundwater.
[0019] The low-boiling medium 90 which has been cooled in the condenser 30 is liquefied
and then flows into the pump 40. The low-boiling medium 90 which has passed through
the condenser 30 occasionally fails to be thoroughly liquefied and partially remains
as vapor. When this happens, a receiver tank (not shown) may be disposed upstream
from the pump 40 to store the liquid low-boiling medium 90 to prevent the vapor from
flowing into the pump 40.
[0020] The intermediate heat exchanger 70 exchanges heat between the vaporous low-boiling
medium 90 which has been discharged from the expander 20 and has not yet flown into
the condenser 30 and the liquid low-boiling medium 90 which has been discharged from
the pump 40 and has not yet flown into the evaporator 10. As discussed previously,
the vaporous low-boiling medium 90 discharged from the expander 20 is cooled in the
intermediate heat exchanger 70 with the liquid low-boiling medium 90 which has been
discharged from the pump 40 and has not yet flown into the evaporator 10. Furthermore,
the liquid low-boiling medium 90 discharged from the pump 40 is heated in the intermediate
heat exchanger 70 with the vaporous low-boiling medium 90 discharged from the expander
20.
[0021] Heat exchangers that have been known in the art may use as the intermediate heat
exchanger 70. In particular, a plate-type heat exchanger is suitable for serving as
the intermediate heat exchanger 70.
[0022] The plate heat exchanger is produced by attaching a predetermined number of heat-transfer
plates to guide bars perpendicularly to guide bars, the plates being formed by stamping
convex-concave wave patterns on thin panels made of corrosion-resistant metal, such
as stainless and titanium, and sealing margins of the panels with synthetic rubber
gaskets, sandwiching the heat-transfer plates between stationary and movable frames
made of steel sheets, and fastening the stationary and mobile frames and the heat-transfer
plates together with bolts. Heat is exchanged between a high-temperature vaporous
low-boiling medium 90 which has been discharged from the expander 20 and flows through
flow paths formed between the plates, and a low-temperature liquid low-boiling medium
90 which has been discharged from the pump 40 and flows through flow paths formed
between the plates before being flown into the evaporator 10.
[0023] With a structure described above, the vaporous low-boiling medium 90 which has been
discharged from the expander 20 and has not yet flown into the condenser 30 is cooled
with the intermediate heat exchanger 70 to a temperature immediately before the vapor
starts being liquefied. This optimizes efficiency of the condenser 30. At the same
time, the liquid low-boiling medium 90 which has been discharged from the pump 40
and has not yet flown into the evaporator 10 is heated to a temperature immediately
before the liquid starts being evaporated. It is therefore possible to optimize a
heat source use efficiency of the binary power generation system 1 as a whole.
[0024] The low-boiling medium 90 which has been discharged from the pump 40 and has not
yet flown into the evaporator 10 is heated with the intermediate heat exchanger 70
to a temperature immediately before the low-boiling medium 90 starts being evaporated,
which is inherent to the low-boiling medium 90. The efficiency of the evaporator 10
then becomes maximum, which optimizes power generation efficiency.
[0025] Since the power generation efficiency is fully improved simply by employing the single
intermediate heat exchanger 70, the binary power generation system 1 may be downsized
and is easily installed even in a relatively small space, such as a site of a hot
spring facility. Furthermore, the binary power generation system 1 needs not be complicated
in structure, thus reducing manufacturing cost.
[0026] Fig. 2 illustrates a configuration of a binary power generation system 1a according
to another embodiment of the present invention. In the description of the present
embodiment, components having the same functions as those of the previous embodiment
will be provided with the same reference numerals as those used in the previous embodiment,
and the description thereof will be omitted.
[0027] Referring to Fig. 2, a circulation pathway 50 of the binary power generation system
1a includes bypasses 51 and 52. The bypass 51 connects an expander 20 to a condenser
30 without passing through an intermediate heat exchanger 70. The bypass 52 connects
the pump 40 to an evaporator 10 without passing through the intermediate heat exchanger
70.
[0028] The binary power generation system 1a further includes medium flow-path switching
devices 81 to 84. The medium flow-path switching devices 81 and 82 are disposed in
both end portions of the bypass 51. The circulation pathway 50 includes a divergent
pathway extending from the medium flow-path switching device 81 through the intermediate
heat exchanger 70 to the medium flow-path switching device 82. The medium flow-path
switching devices 83 and 84 are disposed in both end portions of the bypass 52. The
circulation pathway 50 includes a divergent pathway extending from the medium flow-path
switching device 83 through the intermediate heat exchanger 70 to the medium flow-path
switching device 84. The medium flow-path switching devices 81 and 82 are capable
of switching the flow path of the low-boiling medium 90 between a first pathway which
passes through the intermediate heat exchanger 70 and does not pass through the bypass
51, and a second pathway which bypasses the intermediate heat exchanger 70 and passes
the bypass 51. Likewise, the medium flow-path switching devices 83 and 84 are capable
of switching the flow path of the low-boiling medium 90 between a first pathway which
passes through the intermediate heat exchanger 70 and does not pass through the bypass
52, and a second pathway which bypasses the intermediate heat exchanger 70 and passes
through the bypass 52.
[0029] The binary power generation system 1a further includes a first temperature measuring
device 53 and a second temperature measuring device 54. The first temperature measuring
device 53 measures temperature T1 of the liquid low-boiling medium 90 at a point after
the liquid is discharged from the pump 40 and before the flow path of the low-boiling
medium 90 diverges toward the intermediate heat exchanger 70. The second temperature
measuring device 54 measures temperature T2 of the vaporous low-boiling medium 90
at a point after the vapor is discharged from the expander 20 and before the flow
path of the low-boiling medium 90 diverges toward the intermediate heat exchanger
70.
[0030] Normally, the temperature T1 of the liquid low-boiling medium 90 at the point after
the liquid is discharged from the pump 40 and before the flow path of the low-boiling
medium 90 diverges is sufficiently lower than the temperature T2 of the low-boiling
medium 90 which has been discharged from the expander 20. However, due to a change
in source temperature of the hot source and external air conditions, there is a chance
that temperature difference ΔT is not sufficient between the temperature T2 of the
low-boiling medium 90 discharged from the expander 20, and the temperature T1 of the
liquid low-boiling medium 90 at a point after the liquid is discharged from the pump
40 and before the flow path of the low-boiling medium 90 diverges. In this case, it
might not be efficient to use the intermediate heat exchanger 70 for exchanging heat
between the low-boiling medium 90 discharged from the expander 20 and the low-boiling
medium 90 discharged from the pump 40.
[0031] In this light, the binary power generation system 1a is configured to compare the
temperature T1 measured by the first temperature measuring device 53 with the temperature
T2 measured by the second temperature measuring device 54. If the difference ΔT is
equal to or smaller than a predetermined value, the binary power generation system
1a switches the medium flow-path switching devices 81 to 84 to allow the low-boiling
medium 90 to flow through the bypasses 51 and 52, instead of passing through the intermediate
heat exchanger 70.
[0032] Because of the constitution described above, there is less chance that the binary
power generation system 1a is affected by changes in heat source temperature and external
air environment.
- 1, 1a
- binary power generation system
- 10
- evaporator
- 20
- expander
- 30
- condenser
- 40
- pump
- 50
- circulation pathway
- 51, 52
- bypass
- 53
- first temperature measuring device
- 54
- second temperature measuring device
- 60
- generator
- 70
- intermediate heat exchanger
- 81 to 84
- medium flow-path switching device
- 90
- low-boiling medium
- 100
- hot water
- 200
- cooling water
1. A binary power generation system (1, 1a) comprising:
an evaporator (10) configured to heat a low-boiling medium (90) and turn a liquid
state into a vapor state;
an expander (20) configured to be activated by expansion of a vaporous low-boiling
medium (90) discharged from the evaporator (10);
a generator (60) configured to generate power by the expander (20) being activated;
a condenser (30) configured to liquefy the vaporous low-boiling medium (90) discharged
from the expander (20);
a pump (40) for circulating the low-boiling medium (90);
a closed-loop circulation pathway (50) including the evaporator (10), the expander
(20), the condenser (30), and the pump (40); and
an intermediate heat exchanger (70) configured to exchange heat between the vaporous
low-boiling medium (90) which is discharged from the expander (20) and is still not
flown into the condenser (30), and a liquid low-boiling medium (90) which is discharged
from the pump (40) and is still not flown into the evaporator (10).
2. The binary power generation system (1a) of claim 1,
wherein the circulation pathway (50) includes bypasses (51, 52) connecting the expander
(20) to the condenser (30), and the pump (40) to the evaporator (10), without passing
through the intermediate heat exchanger (70),
wherein the binary power generation system (1a) further comprises:
a first temperature measuring device (53) configured to measure temperature T1 of
the liquid low-boiling medium (90) discharged from the pump (40);
a second temperature measuring device (54) configured to measure temperature T2 of
the vaporous low-boiling medium (90) discharged from the expander (20); and
a medium flow-path switching device (81, 82, 83, 84) configured to switch a flow path
of the low-boiling medium (90) between a fist pathway passing through the intermediate
heat exchanger (70) and a second pathway which follows the bypass (51, 52) without
passing through the intermediate heat exchanger (70), and
wherein the medium flow-path switching device (81, 82, 83, 84) is configured to switch
the flow path of the low-boiling medium (90) from the first pathway to the second
pathway when a temperature difference between the temperature T1 and the temperature
T2 is smaller than a predetermined temperature difference.
3. The binary power generation system (1, 1a) of claim 1 or 2,
wherein the expander (20) is a scroll expander including a fixed scroll and an orbiting
scroll, and
wherein the vaporous low-boiling medium (90) is introduced from a central portion
into a gas pocket which is formed by spiral-shaped fixed and orbiting wraps provided
in the fixed and orbiting scrolls being meshed with each other.