Technical Field
[0001] The present invention relates to a hydrogen supply system capable of supplying hydrogen
at equal to or lower than a hydrogen concentration specified in a gas grid when hydrogen
is supplied to the gas grid in which mixing of hydrogen is allowed.
Background Art
[0002] Hydrogen as opposed to fossil fuels is clean energy that does not emit carbon dioxide
during combustion. Thus, attention has been paid as one of clean energy for countermeasures
against global warming, and technological development related to production, transportation,
and utilization of hydrogen has been advanced.
[0003] Under such circumstances, it has been proposed to supply hydrogen produced by electrolysis
of water using renewable energy, or the like, reforming of natural gas, or the like,
to a gas pipeline in which mixing of hydrogen is allowed. In this case, it is assumed
that a hydrogen concentration becomes equal to or higher than a hydrogen concentration
specified in a gas grid in the vicinity of a hydrogen supply point, and an amount
of hydrogen desired to be supplied cannot be supplied.
[0004] In addition, in order to supply hydrogen to a gas grid, PTL 1 below proposes a method
of mixing hydrogen with fossil fuel gas such as LP gas or natural gas so as to satisfy
city gas standards and supplying the mixture to the gas grid.
Citation List
Patent Literature
Summary of Invention
Technical Problem
[0006] In the invention described in PTL 1, fossil fuel gas is newly mixed in order to supply
hydrogen. Thus, in the invention described in PTL 1, supply cost is greatly increased.
[0007] It is therefore an object of the present invention to prevent increase in cost and
prevent a hydrogen concentration from exceeding a hydrogen concentration specified
value provided in a gas grid when supplying hydrogen produced as clean energy to the
gas grid.
Solution to Problem
[0008] In order to solve the above problems, a hydrogen supply system of the present invention
includes: a hydrogen production unit which produces hydrogen; a hydrogen boosting
unit which boosts a pressure of the hydrogen produced by the hydrogen production unit
to a pressure at which the hydrogen can be supplied to a gas grid; a grid gas lead-in
unit which leads grid gas from the gas grid; a hydrogen concentration adjustment unit
which adjusts mixed gas to have a hydrogen concentration equal to or lower than an
allowable hydrogen concentration specified in the gas grid; and a mixed gas return
unit which supplies the mixed gas to the gas grid.
[0009] Other means will be described in description of embodiments.
Advantageous Effects of Invention
[0010] According to the present invention, it is possible to supply hydrogen while preventing
increase in cost and preventing a hydrogen concentration from exceeding a hydrogen
concentration specified value provided in a gas grid when supplying hydrogen produced
as clean energy to the gas grid.
Brief Description of Drawings
[0011]
[FIG. 1] FIG. 1 is an explanatory diagram of a hydrogen supply system for explaining
a first embodiment.
[FIG. 2] FIG. 2 is an explanatory diagram of a hydrogen supply system for explaining
a second embodiment.
[FIG. 3] FIG. 3 is an explanatory diagram of a hydrogen supply system for explaining
a third embodiment.
[FIG. 4] FIG. 4 is an explanatory diagram of a hydrogen supply system for explaining
a fourth embodiment.
Description of Embodiments
[0012] Hereinafter, embodiments of the present invention will be described in detail with
reference to the drawings. Note that the same components are denoted by the same reference
numerals, and in a case where description thereof overlaps, the description thereof
may be omitted. In addition, the present invention is not limited to the following
embodiments.
<<First embodiments
[0013] FIG. 1 is an explanatory diagram for explaining a hydrogen supply system 100 according
to a first embodiment.
[0014] The hydrogen supply system 100 described in the first embodiment includes a hydrogen
production unit 101, a hydrogen boosting unit 102, a grid gas lead-in unit 103, a
hydrogen concentration adjustment unit 104, and a mixed gas return unit 105. The hydrogen
supply system 100 is connected to a gas grid 901 to supply hydrogen to the gas grid
901. At least blend gas of natural gas and hydrogen flows through the gas grid 901.
The blend gas may be referred to as mixed gas.
[0015] The hydrogen production unit 101 produces hydrogen. The hydrogen boosting unit 102
boosts a pressure of the hydrogen produced by the hydrogen production unit 101 to
a pressure at which the hydrogen can be supplied to the gas grid 901 and supplies
the hydrogen to the hydrogen concentration adjustment unit 104. The grid gas lead-in
unit 103 leads grid gas from the gas grid 901 and supplies the grid gas to the hydrogen
concentration adjustment unit 104. The hydrogen concentration adjustment unit 104
adjusts the mixed gas to have a hydrogen concentration equal to or lower than an allowable
hydrogen concentration specified in the gas grid 901. The mixed gas return unit 105
supplies the mixed gas adjusted by the hydrogen concentration adjustment unit 104
to the gas grid 901.
[0016] Here, the grid gas lead-in unit 103 and the mixed gas return unit 105 are connected
to the gas grid 901. In the gas grid 901, for example, mixed gas (grid gas) of natural
gas and hydrogen such as city gas exists. In the gas grid 901, an upper limit value
of the hydrogen concentration is provided from the viewpoint of preventing gas grid
hydrogen embrittlement and in order to use an existing natural gas utilization facility.
[0017] The hydrogen production unit 101 produces hydrogen 2 to be supplied to the gas grid
901. Here, while a production flow rate of the hydrogen 2 to be produced may be determined
through prediction from hydrogen demand, or the hydrogen 2 may be produced at a hydrogen
amount instructed by a gas grid manager, both of them are preferably determined in
consideration of the hydrogen demand. Here, examples of a method for producing hydrogen
by the hydrogen production unit 101 include a method of producing hydrogen by electrolysis
of water using electric power generated by renewable energy such as solar power generation
and wind power generation, a method of producing hydrogen by causing carbon monoxide
generated when coal is gasified to undergo shift reaction and then separating carbon
dioxide, a method of producing hydrogen by steam reforming of natural gas, and the
like, but are not limited to any of these. In order to achieve carbon free, in a case
where carbon dioxide is generated in a production process, it is preferable to collect
carbon dioxide and convert the carbon dioxide into valuable materials or store the
carbon dioxide.
[0018] A pressure of the hydrogen 2 produced by the hydrogen production unit 101 is boosted
to a pressure that can be supplied to the gas grid 901 by the hydrogen boosting unit
102. The pressure that can be supplied to the gas grid 901 varies depending on a location
of the gas grid 901 to which hydrogen is to be supplied, and is from 0 to 0.1 MPaG
in a low pressure gas grid, from 0.1 to 1.0 MPaG in an intermediate pressure gas grid,
equal to or higher than 1.0 MPaG in a high pressure gas grid, and the like, and is
changed depending on a point where hydrogen is to be supplied.
[0019] After the pressure of the hydrogen 2 is boosted, the hydrogen 2 is supplied to the
hydrogen concentration adjustment unit 104. The grid gas lead-in unit 103 connected
to the gas grid 901 supplies the grid gas 1 existing in the gas grid 901 to the hydrogen
concentration adjustment unit 104.
[0020] Next, when the grid gas 1 and the hydrogen 2 are supplied, the hydrogen concentration
adjustment unit 104 mixes these two kinds of gas to obtain mixed gas 3. Here, the
hydrogen concentration adjustment unit 104 adjusts a hydrogen concentration of the
mixed gas by changing a grid gas flow rate so as not to exceed the upper limit value
of the hydrogen concentration specified in the gas grid 901. Here, the upper limit
value of the hydrogen concentration specified in the gas grid 901 is also referred
to as an allowable hydrogen concentration. The reason why the grid gas flow rate is
changed is that the hydrogen production unit 101 needs to supply an amount in consideration
of hydrogen demand.
[0021] The mixed gas 3 adjusted by the hydrogen concentration adjustment unit 104 is supplied
to the gas grid 901 through the mixed gas return unit 105.
[0022] According to the hydrogen supply system 100 of the present embodiment, it is possible
to supply produced hydrogen at a hydrogen concentration equal to or lower than a specified
value provided in the gas grid 901.
<<Second embodiments
[0023] In a second embodiment, an example of a method of operating the grid gas lead-in
unit 103 which is one of the components of the hydrogen supply system 100 of the present
invention will be described. FIG. 2 illustrates a configuration diagram of the hydrogen
supply system 100 in which components of the grid gas lead-in unit 103 are illustrated
in detail.
[0024] As illustrated in FIG. 2, the grid gas lead-in unit 103 includes a grid gas hydrogen
concentration measurement unit 1031, a grid gas hydrogen concentration communication
unit 1032, a grid gas flow rate reception unit 1033, a grid gas flow rate adjustment
unit 1034, and a grid gas supply unit 1035, and is connected to the hydrogen concentration
adjustment unit 104 in the hydrogen supply system 100 and the gas grid 901.
[0025] The grid gas hydrogen concentration measurement unit 1031 measures the hydrogen concentration
in the grid gas. The grid gas hydrogen concentration communication unit 1032 transmits
data of the hydrogen concentration in the grid gas to the hydrogen concentration adjustment
unit 104. The grid gas flow rate reception unit 1033 receives the grid gas flow rate
calculated by the hydrogen concentration adjustment unit 104. The grid gas flow rate
adjustment unit 1034 adjusts and leads the grid gas. The grid gas supply unit 1035
supplies the grid gas to the hydrogen concentration adjustment unit 104.
[0026] First, the grid gas hydrogen concentration measurement unit 1031 measures the hydrogen
concentration in the grid gas. The grid gas hydrogen concentration communication unit
1032 transmits the measured grid gas hydrogen concentration data 201 to the hydrogen
concentration adjustment unit 104. Here, the grid gas hydrogen concentration data
201 is used to determine the grid gas flow rate. A measurement interval in the grid
gas hydrogen concentration measurement unit 1031 and a communication interval in the
grid gas hydrogen concentration communication unit 1032 are not limited, but are preferably
set to equal to or less than 5 minutes in consideration of coping with fluctuation
of the hydrogen concentration in the grid gas.
[0027] Next, the hydrogen concentration adjustment unit 104 determines the grid gas flow
rate that achieves the hydrogen concentration specified in the gas grid 901 from the
grid gas hydrogen concentration data 201 and the produced hydrogen amount. Grid gas
flow rate command data 202 determined by the hydrogen concentration adjustment unit
104 is transmitted to the grid gas flow rate reception unit 1033 by a grid gas flow
rate command unit 1044. The grid gas flow rate adjustment unit 1034 adjusts the flow
rate of the grid gas on the basis of the grid gas flow rate command data 202 received
by the grid gas flow rate reception unit 1033.
[0028] Here, a method for calculating the grid gas flow rate by the hydrogen concentration
adjustment unit 104 will be described in the third embodiment. Similarly to the communication
interval of the grid gas hydrogen concentration communication unit 1032, an interval
at which the grid gas flow rate reception unit 1033 receives data is preferably set
to equal to or less than 5 minutes.
[0029] The grid gas flow rate adjustment unit 1034 adjusts the grid gas flow rate to be
led from the gas grid 901 to a value of the grid gas flow rate command data 202 received
by the grid gas flow rate reception unit 1033. The grid gas supply unit 1035 supplies
the grid gas 1 to the hydrogen concentration adjustment unit 104. Thereafter, as described
in the first embodiment, the hydrogen concentration adjustment unit 104 mixes the
grid gas 1 and the hydrogen 2 produced by the hydrogen production unit 101. The mixed
gas 3 adjusted by the hydrogen concentration adjustment unit 104 is supplied to the
gas grid 901 through the mixed gas return unit 105.
[0030] According to the hydrogen supply system 100 including the grid gas lead-in unit 103
of the present embodiment, even in a case where the hydrogen concentration in the
grid gas fluctuates, the hydrogen concentration in the mixed gas adjusted by the hydrogen
concentration adjustment unit 104 can be made equal to or less than the specified
value of the gas grid 901.
<<Third embodiments
[0031] In a third embodiment, an example of a method for operating the hydrogen concentration
adjustment unit 104 which is one of the components of the hydrogen supply system 100
of the present invention will be described. FIG. 3 illustrates a configuration diagram
of the hydrogen supply system 100 in which components of the hydrogen concentration
adjustment unit 104 in FIG. 2 are illustrated in detail.
[0032] As illustrated in FIG. 3, the hydrogen concentration adjustment unit 104 includes
a grid gas hydrogen concentration reception unit 1041, a produced hydrogen flow rate
measurement unit 1042, a grid gas flow rate calculation unit 1043, a grid gas flow
rate command unit 1044, a gas mixing unit 1045, and a mixed gas supply unit 1046.
The hydrogen concentration adjustment unit 104 is connected to the hydrogen boosting
unit 102 and the grid gas lead-in unit 103 in the hydrogen supply system 100.
[0033] The grid gas hydrogen concentration reception unit 1041 receives the hydrogen concentration
in the grid gas from the grid gas lead-in unit 103. The produced hydrogen flow rate
measurement unit 1042 measures a flow rate of the hydrogen produced by the hydrogen
production unit 101. The grid gas flow rate calculation unit 1043 calculates a grid
gas flow rate at which a hydrogen concentration of the mixed gas becomes equal to
or lower than an allowable hydrogen concentration specified in the gas grid 901 from
the flow rate of the hydrogen produced by the hydrogen production unit 101. The grid
gas flow rate command unit 1044 commands the grid gas flow rate calculated by the
grid gas flow rate calculation unit 1043 to the grid gas lead-in unit 103. The gas
mixing unit 1045 mixes a specified amount of grid gas supplied from the grid gas lead-in
unit 103 and the hydrogen produced by the hydrogen production unit 101. The mixed
gas supply unit 1046 supplies the mixed gas mixed by the gas mixing unit 1045 to the
mixed gas return unit 105.
[0034] The hydrogen concentration adjustment unit 104 calculates a grid gas flow rate for
making the hydrogen concentration in the mixed gas 3 to be supplied to the gas grid
901 equal to or less than the specified value using the grid gas hydrogen concentration
data 201 which is the hydrogen concentration in the grid gas and the produced hydrogen
flow rate data 203. The grid gas hydrogen concentration data 201 measured by the grid
gas hydrogen concentration measurement unit 1031 described in the second embodiment
is received by the grid gas hydrogen concentration reception unit 1041 through the
grid gas hydrogen concentration communication unit 1032. The produced hydrogen flow
rate data 203 is data measured by the produced hydrogen flow rate measurement unit
1042. These two kinds of data are sent to the grid gas flow rate calculation unit
1043. Here, the flow rate of the grid gas 1 to be led by the grid gas lead-in unit
103 needs to flexibly cope with successive fluctuation of the flow rate of the hydrogen
to be produced by the hydrogen production unit 101. When a transmission interval of
the grid gas hydrogen concentration data 201 is slow and determination of the grid
gas flow rate is delayed, the hydrogen concentration in the mixed gas 3 to be supplied
to the gas grid 901 exceeds the specified value and cannot be supplied particularly
when the produced hydrogen flow rate increases. Thus, a reception interval of the
grid gas hydrogen concentration data 201 of the grid gas hydrogen concentration reception
unit 1041 and a measurement interval of the produced hydrogen flow rate data 203 of
the produced hydrogen flow rate measurement unit 1042 to be used for determining the
grid gas flow rate are preferably set to equal to or less than 5 minutes.
[0035] The grid gas flow rate calculation unit 1043 calculates the grid gas flow rate by
the following equation (1). F
G in equation (1) is the grid gas flow rate [Nm
3/h], F
H2.SUP is the produced hydrogen flow rate [Nm
3/h], x
H2.SET is a target hydrogen concentration [vol%] in the mixed gas, and x
H2.G is the grid gas hydrogen concentration [vol%]. Here, the target hydrogen concentration
x
H2.SET in the mixed gas is set to be equal to or less than the specified value of the hydrogen
concentration provided in the gas grid. The method of calculating the grid gas flow
rate is not limited to equation (1) .

[0036] Here, a calculation example using equation (1) will be described. First, it is assumed
that a hydrogen concentration specified value of 20 vol% is provided in the gas grid
901, the produced hydrogen flow rate is 100 Nm
3/h, the grid gas hydrogen concentration is 10 vol%, and the target hydrogen concentration
in the mixed gas is 20 vol%. A hydrogen user preferably increases the hydrogen concentration
in the gas grid 901 as much as possible, and thus, the target hydrogen concentration
in the mixed gas is set at the specified value of the hydrogen concentration provided
in the gas grid 901 in the present embodiment, but is not limited thereto. If the
above value is substituted into equation (1), the flow rate of the grid gas to be
led by the grid gas lead-in unit 103 is calculated to be 800 Nm
3/h.
[0037] As described above, the grid gas flow rate command data 202 calculated by the grid
gas flow rate calculation unit 1043 is transmitted from the grid gas flow rate command
unit 1044 to the grid gas flow rate reception unit 1033, and the grid gas flow rate
to be led is adjusted by the grid gas flow rate adjustment unit 1034. Here, an interval
of data to be transmitted to the grid gas flow rate reception unit 1033 is preferably
set to equal to or less than 5 minutes, similarly to the data reception interval at
the grid gas hydrogen concentration reception unit 1041 and the flow rate measurement
interval at the produced hydrogen flow rate measurement unit 1042. The specified amount
of the grid gas 1 thus adjusted and the hydrogen 2 produced by the hydrogen production
unit 101 are mixed at the gas mixing unit 1045. When the mixed gas is supplied to
the gas grid 901, it is preferable that there is no distribution of hydrogen in the
mixed gas. Thus, the gas mixing unit 1045 preferably mixes the hydrogen 2 and the
grid gas by a method such as a pressure ratio mixing method, a weight method, a flow
rate mixing method, or a half weight method, but the mixing method is not limited.
Thereafter, the mixed gas 3 is supplied from the mixed gas return unit 105 to the
gas grid 901 through the mixed gas supply unit 1046.
[0038] According to the hydrogen supply system 100 including the hydrogen concentration
adjustment unit 104 of the third embodiment, the hydrogen concentration in the mixed
gas adjusted by the hydrogen concentration adjustment unit 104 can be set to be equal
to or lower than the specified value of the gas grid 901 even in a case where the
produced hydrogen flow rate fluctuates.
<<Fourth embodiments
[0039] In a fourth embodiment, an example of a method of operating the mixed gas return
unit 105 which is one of the components of the hydrogen supply system 100 of the present
invention will be described. FIG. 4 is a configuration diagram of the hydrogen supply
system 100 in which components of the mixed gas return unit 105 in FIG. 3 are illustrated
in detail.
[0040] As illustrated in FIG. 3, the mixed gas return unit 105 includes a mixed gas flow
rate measurement unit 1051, a grid gas flow rate balance management unit 1052, a mixed
gas gas grid supply unit 1053, and a return gas calorimetry unit 1054. The mixed gas
return unit 105 is connected to the hydrogen concentration adjustment unit 104 in
the hydrogen supply system 100 and the gas grid 901.
[0041] The mixed gas flow rate measurement unit 1051 measures the flow rate of the mixed
gas. The grid gas flow rate balance management unit 1052 manages balance of the grid
gas by comparing the grid gas flow rate in the mixed gas obtained by subtracting the
produced hydrogen flow rate measured by the produced hydrogen flow rate measurement
unit 1042 from the mixed gas flow rate measured by the mixed gas flow rate measurement
unit 1051 with the grid gas flow rate commanded by the grid gas flow rate command
unit 1044 to the grid gas flow rate adjustment unit 1034. The mixed gas gas grid supply
unit 1053 supplies the mixed gas to the gas grid 901.
[0042] As described in the first to the third embodiments, the hydrogen concentration of
hydrogen 2 produced by the hydrogen production unit 101 is adjusted by the grid gas
lead-in unit 103 and the hydrogen concentration adjustment unit 104. Here, in order
to lead the grid gas 1 from the gas grid 901 and supply it to the gas grid 901 again,
a hydrogen supplier and a gas grid operator need to manage material balance of the
grid gas 1. By managing the balance of the grid gas flow rate, when the hydrogen supplier
leads the grid gas, the gas grid operator can set a fee structure different from a
fee structure for the existing grid gas user.
[0043] As illustrated in the fourth embodiment, the flow rate of the mixed gas 3 supplied
from the hydrogen concentration adjustment unit 104 is measured by the mixed gas flow
rate measurement unit 1051 and is transmitted to the grid gas flow rate balance management
unit 1052 as mixed gas flow rate data 204. The grid gas flow rate balance management
unit 1052 calculates the material balance of the grid gas using the mixed gas flow
rate data 204, the produced hydrogen flow rate data 203 measured by the produced hydrogen
flow rate measurement unit 1042, and the grid gas flow rate command data 202 determined
by the grid gas flow rate calculation unit 1043 and performs management so that the
same amount of the grid gas 1 lead from the gas grid 901 is normally returned to the
gas grid 901. Here, it is assumed that there is a time difference in each measurement
data depending on an operation period of each step and a length of a gas pipe, and
the balance of the material is not accurately matched in the data at the same time.
It is therefore preferable to manage the balance of the flow rate in a certain time
width. A status of the grid gas material balance management is also transmitted to
the gas grid operator 106 and is constantly grasped by both.
[0044] Finally, the mixed gas gas grid supply unit 1053 supplies gas to the gas grid 901
using, for example, a blower, or the like. A connection port with the gas grid 901
desirably has a structure in which the return gas is diffused in the gas grid 901
as much as possible.
[0045] According to the hydrogen supply system 100 including the mixed gas return unit 105
of the present embodiment, it is possible to set a fee structure different from a
fee structure for the existing grid gas user by managing the material balance of the
lead-in grid gas and the grid gas returned to the gas grid 901.
[0046] In addition, a hydrogen supply device supplies the mixed gas 3 to the gas grid 901
by the methods described in the first to third embodiments and the present embodiment,
but it is necessary to obtain revenue by charging according to the amount of hydrogen
supplied in the mixed gas 3. As a method of this charging, for example, there is a
method of calculating a charge amount on a calorie basis.
[0047] Specifically, the return gas calorimetry unit 1054 is provided in the mixed gas return
unit 105 in FIG. 4. The return gas calorimetry unit 1054 is a unit that calculates
an amount of heat of hydrogen in the supplied mixed gas from an amount of heat [MJ/m
3] corresponding to hydrogen content of the mixed gas 3, a flow rate [m
3/h], and a supply period [h]. A charge amount can be determined on the basis of the
amount of heat calculated by the return gas calorimetry unit 1054 and paid to the
supplier.
[0048] Then, a used gas calorimetry unit is provided on a hydrogen utilization device side
(not illustrated). The used gas calorimetry unit is a unit that calculates an amount
of heat of the used gas on the basis of a calorific value [MJ/m
3] of the used gas, a flow rate [m
3/h], and a supply period [h]. By measuring the amount of heat of the used gas by the
used gas calorimetry unit, a usage fee can be determined and charged to the user.
(Modifications)
[0049] The present invention is not limited to the above-described embodiments and includes
various modifications. For example, the above-described embodiments have been described
in detail for easy understanding of the present invention, and the present invention
is not necessarily limited to those having all the described components. In addition,
part of the components of a certain embodiment can be replaced with the components
of another embodiment, and the components of another embodiment can be added to the
configuration of a certain embodiment. In addition, it is also possible to add, delete,
or replace other components for part of the components of each embodiment.
[0050] Some or all of the above-described configurations, functions, processing units, processing
means, and the like, may be implemented by hardware such as an integrated circuit,
for example. Each of the above-described configurations, functions, and the like,
may be implemented by software by a processor interpreting and executing a program
for implementing each function. Information such as a program, a table, and a file
for implementing each function can be stored in a recording device such as a memory,
a hard disk, and a solid state drive (SSD), or a recording medium such as a flash
memory card and a digital versatile disk (DVD).
[0051] In addition, in each embodiment, control lines and information lines considered to
be necessary for description are illustrated, and not all control lines and information
lines in a product are necessarily illustrated. In practice, it may be considered
that almost all the components are connected to each other.
Reference Signs List
[0052]
- 1
- grid gas
- 2
- hydrogen
- 3
- mixed gas (blend gas)
- 100
- hydrogen supply system
- 101
- hydrogen production unit
- 102
- hydrogen boosting unit
- 103
- grid gas lead-in unit
- 1031
- grid gas hydrogen concentration measurement unit
- 1032
- grid gas hydrogen concentration communication unit
- 1033
- grid gas flow rate reception unit
- 1034
- grid gas flow rate adjustment unit
- 1035
- grid gas supply unit
- 104
- hydrogen concentration adjustment unit
- 1041
- grid gas hydrogen concentration reception unit
- 1042
- produced hydrogen flow rate measurement unit
- 1043
- grid gas flow rate calculation unit
- 1044
- grid gas flow rate command unit
- 1045
- gas mixing unit
- 1046
- mixed gas supply unit
- 105
- mixed gas return unit
- 1051
- mixed gas flow rate measurement unit
- 1052
- grid gas flow rate balance management unit
- 1053
- mixed gas gas grid supply unit
- 106
- gas grid operator
- 201
- grid gas hydrogen concentration data
- 202
- grid gas flow rate command data
- 203
- produced hydrogen flow rate data
- 204
- mixed gas flow rate data
- 901
- gas grid
1. A hydrogen supply system comprising:
a hydrogen production unit which produces hydrogen;
a hydrogen boosting unit which boosts a pressure of the hydrogen produced by the hydrogen
production unit to a pressure at which the hydrogen can be supplied to a gas grid;
a grid gas lead-in unit which leads grid gas from the gas grid;
a hydrogen concentration adjustment unit which adjusts mixed gas to have a hydrogen
concentration equal to or lower than an allowable hydrogen concentration specified
in the gas grid; and
a mixed gas return unit which supplies the mixed gas to the gas grid.
2. The hydrogen supply system according to claim 1, wherein
at least blend gas of natural gas and hydrogen flows through the gas grid.
3. The hydrogen supply system according to claim 1 or 2, wherein
the hydrogen production unit produces hydrogen by any one of a method of electrolysis
of water using electric power generated by renewable energy, a method of reforming
natural gas, and a method of producing hydrogen by gasifying coal and causing shift
reaction.
4. The hydrogen supply system according to claim 1 or 2, wherein
the grid gas lead-in unit includes:
a grid gas hydrogen concentration measurement unit which measures a hydrogen concentration
in grid gas;
a grid gas hydrogen concentration communication unit which transmits data of the hydrogen
concentration in the grid gas to the hydrogen concentration adjustment unit;
a grid gas flow rate reception unit which receives a grid gas flow rate calculated
by the hydrogen concentration adjustment unit;
a grid gas flow rate adjustment unit which adjusts and leads the grid gas; and
a grid gas supply unit which supplies the grid gas to the hydrogen concentration adjustment
unit.
5. The hydrogen supply system according to any one of claims 1 to 4, wherein
the hydrogen concentration adjustment unit includes:
a grid gas hydrogen concentration reception unit which receives the hydrogen concentration
in the grid gas from the grid gas lead-in unit;
a produced hydrogen flow rate measurement unit which measures a flow rate of the hydrogen
produced by the hydrogen production unit;
a grid gas flow rate calculation unit which calculates a grid gas flow rate such that
the mixed gas has a hydrogen concentration equal to or lower than the allowable hydrogen
concentration specified in the gas grid from the flow rate of the hydrogen produced
by the hydrogen production unit;
a grid gas flow rate command unit which commands the grid gas flow rate calculated
by the grid gas flow rate calculation unit;
a gas mixing unit which mixes a designated amount of the grid gas supplied from the
grid gas lead-in unit and the hydrogen produced by the hydrogen production unit; and
a mixed gas supply unit which supplies the mixed gas mixed by the gas mixing unit
to the mixed gas return unit.
6. The hydrogen supply system according to claim 5, wherein
the mixed gas return unit includes:
a mixed gas flow rate measurement unit which measures a flow rate of the mixed gas;
and
a grid gas flow rate balance management unit which manages balance of the grid gas
by comparing a grid gas flow rate in the mixed gas obtained by subtracting the produced
hydrogen flow rate measured by the produced hydrogen flow rate measurement unit from
the mixed gas flow rate measured by the mixed gas flow rate measurement unit with
the grid gas flow rate commanded by the grid gas flow rate command unit.
7. The hydrogen supply system according to claim 6, wherein
the mixed gas return unit further includes a return gas calorimetry unit which measures
an amount of heat of hydrogen in the return gas.