KR20180075292A - Ship - Google Patents

Abstract

The present invention relates to a ship, capable of supplying a sufficient amount of steam (H_2O) and electricity during anchoring. According to the present invention, the ship comprises: a water supply installed in a hull and supplying water; a plurality of auxiliary engines installed to be safety the water supply unit and producing electricity; a plurality of economizers heating the water supplied from the water supply unit by using auxiliary engine exhaust gas discharged from the auxiliary engines as a heat source to generate the steam (H_2O) requested from a customer; a branch unit to branch fuel supplied to the auxiliary engine from a fuel storage tank storing the fuel; a fuel cell system using the fuel supplied from the branch unit and the steam supplied from the economizer; a junction unit to joint fuel cell exhaust gas discharged from the fuel cell system and the auxiliary engine exhaust gas supplied to the economizer from the auxiliary engine; and an electric heater installed between the junction unit and the economizer, and using electricity to heat the exhaust gas supplied from the junction unit. The fuel cell system comprises: a hydrogen generation unit including a modifier to modify the fuel supplied from the branch unit and the steam supplied from the economizer, and a combustor; and a fuel cell including a fuel electrode (anode), an air electrode (cathode), and an electrolyte formed between the fuel and air electrodes to generate the electricity. The exhaust gas heated by the electric heater is supplied to the economizer to increase the amount of the steam (H_2O) produced by the economizer.

Description

Ship {Ship}

BACKGROUND OF THE INVENTION 1. Field of the Invention [0001] The present invention relates to a ship for transporting people, cargo and the like from water such as river and sea to a destination.

In general, ships are used in various fields such as transportation means for transporting passengers and cargoes to destinations, fishing vessels for capturing seafood, military vessels made for military purposes, and the like, which can be moved from water using power means. These ships are equipped with a main engine for rotating a propulsion device such as a propeller, an auxiliary engine for producing electricity used by the electric devices installed on the ship, steam (H ₂ O An economizer for producing electricity, and a main turbine for producing electricity from steam discharged from the economizer. Since the capacity of the auxiliary engine is smaller than that of the main engine, a plurality of the auxiliary engines are installed. A plurality of the economizers are installed so as to be connected to the engines, respectively. The exhaust gas discharged from each engine is converted into steam (H ₂ O) by heating the water with a heat source. The steam (H ₂ O) produced through the economizer is used for various purposes such as heating, fuel oil heating, and electric production.

On the other hand, when the main engine does not operate, the ship uses steam to produce steam (H ₂ O) and electricity. For example, when a ship is anchored in a port without navigating, some auxiliary engines of a plurality of auxiliary engines are used to produce steam (H ₂ O) and electricity. However, there is a problem in that some of the auxiliary engines can not satisfy the demand of steam (H ₂ O) and electricity.

In order to solve the above problems, the ship according to the prior art further installs an auxiliary boiler on the hull. The auxiliary boiler is a steam (H ₂ O) the steam (H ₂ O) supplied to the addition to the consumer or to the economizer production then heated to heat the water generated when combusting the fuel to produce steam (H ₂ O) To increase the electricity production. However, the ship according to the prior art has the following problems.

First, since the auxiliary boiler supplies the fuel from the fuel storage part to the ship according to the prior art, the size of the auxiliary boiler is large. Accordingly, since the weight of the auxiliary boiler in the hull having a limited space is increased, the loss of the hull space due to the auxiliary boiler is increased, thereby reducing the space utilization of the hull.

Second, because the size of the auxiliary boiler is large in the ship according to the related art, the space between the auxiliary boiler and the surrounding devices is narrow. Accordingly, there is a problem that it is difficult for a ship according to the related art to perform maintenance work and replacement work for the auxiliary boiler and the peripheral devices because an operator is difficult to enter between the auxiliary boiler and the peripheral device.

SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems, and it is an object of the present invention to provide a ship capable of supplying a sufficient amount of steam (H ₂ O) and electricity even at the time of berth without lowering the space utilization of the hull.

In order to solve the above-described problems, the present invention can include the following configuration.

A ship according to the present invention includes a water supply unit installed on a ship and supplying water; A plurality of auxiliary engines installed to be spaced apart from the water supply unit and generating electricity; A plurality of economizers for generating steam (H ₂ O) required by a customer by heating water supplied from the water supply unit using the auxiliary engine exhaust gas discharged from the auxiliary engines as a heat source; A branching portion for branching the fuel supplied to the auxiliary engine from a fuel storage tank for storing fuel; A fuel cell system for generating electricity using fuel supplied from the branching portion and steam supplied from the economizer; A merging unit for merging the fuel cell exhaust gas discharged from the fuel cell system and the auxiliary engine exhaust gas supplied from the auxiliary engine to the economizer; And an electric heater installed to be positioned between the merging unit and the economizer and for heating the exhaust gas supplied from the merging unit using electricity. Wherein the fuel cell system includes a hydrogen generator including a reformer and a combustor for reforming the fuel supplied from the branching section and the steam supplied from the economizer; And a fuel cell including an anode, a cathode, and an electrolyte formed between the anode and the cathode. The exhaust gas heated by the electric heater can be supplied to the economizer such that the amount of steam (H ₂ O) produced by the economizer increases.

In the vessel according to the present invention, the electric heater can heat the exhaust gas supplied to the economizer by using electricity produced by at least one of the plurality of auxiliary engines and the fuel cell.

The ship according to the present invention may include a power storage unit for storing electricity produced by at least one of the plurality of auxiliary engines and the fuel cell. Wherein the electric heater is installed to be connected to the electric power storage unit. When the amount of steam (H ₂ O) required by the customer is greater than a preset reference steam consumption amount, the electricity stored in the electric power storage unit is used to charge the electric power to the economizer It is possible to heat the supplied exhaust gas.

A fuel cell system according to the present invention is a fuel cell system comprising a fuel storage tank for storing fuel, a fuel supply unit for supplying fuel to a plurality of auxiliary engines for producing electricity, And a reformer and a combustor for reforming steam supplied from a plurality of economizers for generating steam (H ₂ O) required by a customer by heating water supplied from a water supply unit for supplying water as a heat source part; And a fuel cell including an anode, a cathode, and an electrolyte formed between the anode and the cathode. A fuel cell exhaust gas discharged from the fuel cell and a subsidiary engine exhaust gas supplied to the economizer from the auxiliary engine; and an exhaust gas supply unit installed to be positioned between the economizer and supplied from the merging unit using electricity, Can be supplied to the economizer such that the amount of steam (H ₂ O) produced by the economizer increases.

In the fuel cell system according to the present invention, the electric heater can heat the exhaust gas supplied to the economizer by using electricity produced by at least one of the plurality of auxiliary engines and the fuel cell.

The fuel cell system according to the present invention may include a power storage unit for storing electricity produced by at least one of the plurality of auxiliary engines and the fuel cell. Wherein the electric heater is installed to be connected to the electric power storage unit. When the amount of steam (H ₂ O) required by the customer is greater than a preset reference steam consumption amount, the electricity stored in the electric power storage unit is used to charge the electric power to the economizer It is possible to heat the supplied exhaust gas.

According to the present invention, the following effects can be obtained.

The present invention offer a sufficient amount of steam (H ₂ O) of in the implementation being, anchored so as to increase the production of raising the temperature of the exhaust steam (H ₂ O) to be supplied to the economizer demand by using an electric heater And the auxiliary boiler can be omitted, so that the space utilization for the hull can be increased and the load of the passenger and cargo can be increased.

The present invention can be implemented to further produce electricity using a fuel cell so as to increase the amount of electricity produced. In addition, the fuel cell exhaust gas discharged from the fuel cell can be supplied to the economizer by joining with the auxiliary engine exhaust gas discharged from the auxiliary engine So that the production of steam (H ₂ O) can be increased.

Since the size of the electric heater is smaller than that of the auxiliary boiler, the interval between the electric heater and the peripheral devices can be widened, so that maintenance work and replacement work for the electric heater and peripheral devices can be easily performed.

1 is a schematic block diagram of a ship according to the present invention;
2 is a conceptual diagram of an overall system according to the present invention
3 is a conceptual diagram of a fuel cell system according to the present invention.
FIGS. 4A and 4B are diagrams for explaining the operation of the fuel cell used in the present invention. FIG. 4A is a conceptual diagram of a solid oxide fuel cell (SOFC)
4B is a conceptual diagram of a polymer electrolyte fuel cell (PEMFC)
5 is an exemplary diagram illustrating a hydrogen generator according to an embodiment of the present invention.
6 is a conceptual diagram of a ship according to the present invention
7 is a schematic block diagram for explaining a fuel cell system and an electric heater in a ship according to the present invention
8 is a schematic block diagram for explaining a case in which only a part of a plurality of auxiliary engines is operated in a ship according to the present invention
9 is a schematic block diagram for explaining a power storage unit in a ship according to the present invention.

It should be noted that, in the specification of the present invention, the same reference numerals as in the drawings denote the same elements, but they are numbered as much as possible even if they are shown in different drawings.

Meanwhile, the meaning of the terms described in the present specification should be understood as follows.

The word " first, "" second," and the like, used to distinguish one element from another, are to be understood to include plural representations unless the context clearly dictates otherwise. The scope of the right should not be limited by these terms.

It should be understood that the terms "comprises" or "having" does not preclude the presence or addition of one or more other features, integers, steps, operations, elements, components, or combinations thereof.

It should be understood that the term "at least one" includes all possible combinations from one or more related items. For example, the meaning of "at least one of the first item, the second item and the third item" means not only the first item, the second item or the third item, but also the second item and the second item among the first item, Means any combination of items that can be presented from more than one.

Hereinafter, a ship according to the present invention will be described in detail with reference to the accompanying drawings.

Fig. 1 is a schematic block diagram of a ship according to the present invention, Fig. 2 is a conceptual diagram of an overall system according to the present invention, Fig. 3 is a conceptual diagram of a fuel cell system according to the present invention, FIG. 4A is a conceptual diagram of a solid oxide fuel cell (SOFC), FIG. 4B is a conceptual diagram of a polymer electrolyte fuel cell (PEMFC), and FIG. 5 is an exemplary view for explaining a hydrogen generator according to an embodiment of the present invention.

1 to 5, the vessel 1 according to the present invention is intended to increase the production amount of steam (H ₂ O) and electricity even when only a part of a plurality of auxiliary engines installed in the hull is operated. In particular, the vessel 1 according to the present invention can not only increase the electricity production amount by using the fuel cell but also merge the fuel cell exhaust gas discharged from the fuel cell with the auxiliary engine exhaust gas discharged from the auxiliary engine, The exhaust gas is heated by an electric heater and supplied to the economizer so that the production of steam (H ₂ O) can be increased. In addition, since the ship 1 according to the present invention uses an electric heater smaller in size than the auxiliary boiler, the space utilization of the hull can be increased as compared with the case where the auxiliary boiler is used, Maintenance operations and replacement operations for the devices can be performed smoothly.

1 to 5, a ship 1 according to the present invention is provided with a power generation system 10 on a ship 11. The hull 11 constitutes the overall appearance of the ship 1 according to the present invention. The power generation system 10 mainly includes an engine exhaust system 100 and a fuel cell system 8. The engine exhaust system 100 may include a main engine 101, a main economizer 102, a steam turbine 103, an auxiliary engine 3 and an economizer 4. The main engine 101 is connected to the main economizer 102 and the main economizer 102 is connected to the steam turbine 103. The auxiliary engine (3) is installed to be connected to the economizer (4). A plurality of the auxiliary engines 3 and the economizers 4 may be installed in the hull 11, respectively. Here, the main engine 101 and the auxiliary engine 3 may be a diesel engine or a gas engine. The fuel cell system 8 mainly includes a fuel cell 81 and a hydrogen generator 82. The fuel cell system 8 may be implemented by including a control unit 83 for controlling operations of all the configurations including the fuel cell 81 and the hydrogen generation unit 82 and the like.

The power generation system 10 includes a fuel storage tank 20, an air supply unit 30, a power conversion unit 40, a water supply unit 2, a branching unit 5, a merging unit 6, .

Between the fuel storage tank 20 and the auxiliary engine 3, a branching portion 5 for supplying fuel to the fuel cell system 8 may be installed. An electric heater 7 for heating the exhaust gas supplied to the economizer 4 may be installed between the auxiliary engine 3 and the economizer 4. The auxiliary engine 3 and the electric heater 7 are connected to each other by a merging portion for merging the auxiliary engine exhaust gas discharged from the auxiliary engine 3 and the fuel cell exhaust gas discharged from the fuel cell system 8 6 may be installed.

The fuel cell system 8 according to the present invention is configured to receive fuel from the hydrogen generation unit 82 and the hydrogen generation unit 82 to receive fuel from the fuel storage tank 20 that stores the fuel. The hydrogen generating unit 82 can receive the diesel fuel stored in the fuel storage tank 20 through the branching unit 5 when the engine is a diesel engine 101. The fuel cell system 8 according to the present invention is configured such that when the engine is a gas engine, the gaseous fuel stored in the fuel storage tank 20 is directly supplied through the branch portion 5 without passing through the hydrogen generating portion 82 It is possible. The fuel cell system 8 according to the present invention can supply the fuel cell exhaust gas discharged from the fuel cell 81 to the merging section 6. [

The engine exhaust system 100 includes a main engine 101, a main economizer 102, a steam turbine 103, a plurality of auxiliary engines 3, and a plurality of economizers 4.

The engine exhaust system 100 is a component included in a power generation system using an engine. The engine exhaust system 100 purifies the exhaust gas containing environmental pollutants such as nitrogen oxides (NOx) generated in the engine combustion chamber and recovers the heat of the exhaust gas And discharges it to the outside. In the engine exhaust system 100, a selective catalytic reduction (SCR) may be installed to reduce nitrogen oxides (NOx) and the like contained in the exhaust gas.

The main engine 101 generates exhaust gas as fuel and air are mixed and burned. The main economizer 102 can generate steam (H ₂ O) by heating the water supplied from the water supply unit 2 by using the main engine exhaust gas discharged from the main engine 101. Since the main engine exhaust gas discharged from the main engine 101 is at a high temperature, it may be a heat source for heating water. The steam (H ₂ O) generated in the main economizer 102 can be supplied to the steam turbine 103. The steam turbine 103 can generate electricity by driving a main generator (not shown) using steam (H ₂ O) supplied from the main economizer 102. Electricity produced by the main generator may be supplied to the electric device installed in the hull 11 and the electric heater 7. [ The steam (H ₂ O) produced and discharged from the steam turbine 103 may be supplied to a customer 50 (shown in FIG. 7). The customer 50 can receive various kinds of steam (H ₂ O). For example, the customer 50 may use steam (H ₂ O) as a heat source for heating or fuel oil.

The main engine 101 is activated when the ship 1 is in voyage, and is not activated when the ship 1 is docked in the port. This is because it is not necessary to activate the propulsion unit when the vessel 1 is stationed in the port. Accordingly, when the ship 1 is docked in the port, exhaust gas is not discharged from the main engine 101, so that the main economizer 102 can not generate steam (H ₂ O). Therefore, in this case, a part of a plurality of auxiliary engines 3 for electric production is operated to generate steam (H ₂ O) by heating the auxiliary engine exhaust gas discharged from the auxiliary engine 3 with a heat source . However, in this case, if the amount of steam (H ₂ O) required by the demander 50 is large, the auxiliary engine 3 alone can not meet the demand. In order to solve such a problem, the ship 1 according to the present invention joins the fuel cell exhaust gas discharged from the fuel cell system 8 to the auxiliary engine exhaust gas, To the economizer 4 so that the temperature of the exhaust gas supplied to the economizer 4 can be increased to increase the production of steam (H ₂ O). Accordingly, the ship 1 according to the present invention can supply a sufficient amount of steam (H ₂ O) to the demander 50, so that the demand of the demander 50 can be satisfied. Here, generating steam (H ₂ O) means that water is heated by the heat source and is phase-changed into steam (H ₂ O).

The main engine 101, the auxiliary engine 3 and the fuel cell system 8 may be supplied with fuel from a fuel storage tank 20 for storing fuel. When the engine is a diesel engine 101, the diesel engine 101 can receive diesel fuel from the fuel storage tank 20. The diesel fuel may be selected from the group consisting of marine gas oil (MGO), marine diesel oil (MDO), heavy fuel oil (HFO), methanol, dimethyl ether (DME) ) And the like.

The air supply unit 30 supplies air to the main engine 101, the auxiliary engine 3, and the fuel cell system 8. Normally, air means a gas including nitrogen, oxygen, carbon dioxide and the like, but also includes the case where all gases other than oxygen such as nitrogen or carbon dioxide, or both gases are removed from the air. The air supply unit 30 may be configured to supply the compressed high-pressure air or the atmospheric pressure after the external air is supplied and compressed. The air supply unit 30 may include a conduit for moving air and a conveying device such as a compressor or an impeller for generating a conveying force for moving the air.

The power conversion unit 40 converts the direct current (DC) output from the fuel cell system 8 according to the present invention into an alternating current (AC). The power conversion unit 40 includes a DC-DC converter for boosting or reducing the output voltage from the fuel cell system 8 according to the present invention, and a DC-AC converter for converting a direct current (DC) An inverter or the like. The power conversion unit 40 may discharge the electricity supplied from the fuel cell system 8 according to the present invention to the consumer 50. Although not shown, the power conversion unit 40 may be implemented to transmit and store electricity to an energy storage device, for example, a battery.

The customer 50 can use steam (H ₂ O) and electricity. For example, the customer 50 may receive steam (H ₂ O) from the main economizer 102 and the economizer 4. When the ship is anchored, the customer 50 can receive steam (H ₂ O) from the economizer 4. Accordingly, the customer 50 can use steam (H ₂ O) as a heat source for heating or fuel oil. The customer 50 can receive electricity generated by the steam turbine 103, the auxiliary engine 3, and the fuel cell system 8. The customer 50 can use the supplied electricity for the electrical equipment in the ship such as the basic electrical equipment of the ship and the cargo system electrical equipment.

The water supply unit 2 is for supplying water. For example, the water supply section 2 can supply water to the main economizer 102 and the economizer 4. The water supply part (2) is installed in the hull. The water supply unit 2 can supply water to the main economizer 102 and the economizer 4 by sucking water located outside the ship. The water supply unit 2 sucks the water stored in the water storage tank and supplies water to the main economizer 102 and the economizer 4 when a water storage tank for storing water is installed inside the ship It is possible. The water supply unit 2 may include a conduit for moving water and a pump for generating a transfer force for moving water along the conduit. The water supply 2 may be connected to the main economizer 102 and the economizer 4 through a conduit such as a pipe or pipe. Accordingly, the water supply unit 2 can supply water to the main economizer 102 and the economizer 4, respectively. The water supply unit 2 can supply water only to the economizer 4 without supplying water to the main economizer 102 when the ship 1 is docked in the port. Although not shown, a heating unit for heating the water supplied to the main economizer 102 and the economizer 4 may be installed between the water supply unit 2 and the main economizer 102 and the economizer 4 have. Accordingly, the main economizer 102 and the economizer 4 are supplied with at least one of water heated by the heating unit, steam (H ₂ O), and a fluid in which water and steam (H ₂ O) are mixed .

The auxiliary engine 3 is for producing electricity. The auxiliary engine 3 may be installed on the hull 11 so as to be spaced apart from the water supply unit 2. [ Since the auxiliary engine 3 is a power generation engine for producing electricity, the capacity of the auxiliary engine 3 is smaller than that of the main engine 101, which is a propelling engine. Accordingly, a plurality of the auxiliary engines 3 may be installed on the hull. For example, the auxiliary engine 3 may include a first auxiliary engine 31 and a second auxiliary engine 32. The auxiliary engine 3 may further include a plurality of auxiliary engines such as a third auxiliary engine and a fourth auxiliary engine in addition to the first auxiliary engine 31 and the second auxiliary engine 32. In the present specification, the auxiliary engine 3 includes the first auxiliary engine 31 and the second auxiliary engine 32 as examples. The first auxiliary engine 31 and the second auxiliary engine 32 may include a first generator and a second generator, respectively, so that the generators can generate electricity when they are operated. The auxiliary engine 3 includes the first auxiliary engine 31 and the second auxiliary engine 32 so that the economizer 4 is connected to the first auxiliary engine 31, (41), and a second economizer (42) connected to the second auxiliary engine (32).

The first auxiliary engine 31 may generate electricity by supplying fuel and air, mixing and burning the fuel and air, so that the first generator may generate electricity. The first auxiliary engine 31 receives fuel from the fuel storage tank 20 and receives air from the air supply unit 30. The first auxiliary engine 31 may be operated when the ship 1 is anchored, but it is not limited thereto and may be operated even when the ship 1 is navigating. Electricity produced by the first generator may be supplied to at least one of the electric heater 7 and the customer 50. When the first auxiliary engine 31 is operated, the auxiliary engine exhaust gas may be discharged from the first auxiliary engine 31. The high temperature auxiliary engine exhaust gas discharged from the first auxiliary engine 31 may be supplied to the first economizer 41 through a pipeline.

The second auxiliary engine 32 may supply the fuel and the air, and may generate the driving force by mixing and burning the fuel and the air so that the second generator may generate electricity. The second auxiliary engine 33 receives fuel from the fuel storage tank 20 and receives air from the air supply unit 30. [ The second auxiliary engine 32 may be operated when the ship 1 is anchored, but it is not limited thereto and may be operated even when the ship 1 is navigating. Electricity produced by the second generator may be supplied to at least one of the electric heater 7 and the customer 50. When the second auxiliary engine 32 is operated, the auxiliary engine exhaust gas may be discharged from the second auxiliary engine 32. The high temperature auxiliary engine exhaust gas discharged from the second auxiliary engine 32 may be supplied to the second economizer 42 through a pipeline.

The first auxiliary engine 31 and the second auxiliary engine 32 may be all operated according to the amount of fuel stored in the hull or only one of them may be operated. For example, if the amount of stored fuel is large, both the first sub engine 31 and the second sub engine 32 can be operated. The first auxiliary engine 31 and the second auxiliary engine 32 can be operated even when the amount of steam (H ₂ O) required by the customer 50 is large. However, in order to minimize the emission of harmful substances such as nitrogen oxides (NOx) and sulfur oxides (SOx) when the ship 1 is anchored in the port, the first auxiliary engine 31 and the second auxiliary engine 32 ) Can be operated. Ports are included in strict zones for environmental pollution. For example, a port may be included in an emission restriction area (ECA) where the emission of pollutants is limited. Accordingly, the marine vessel 1 according to the present invention joins the fuel cell exhaust gas discharged from the fuel cell system 8 to the auxiliary engine exhaust gas, and then the combined exhaust gas is heated by the electric heater 7 The amount of steam (H ₂ O) produced by the economizer (4) can be increased by supplying it to the economizer (4). Therefore, the ship 1 according to the present invention can operate the steam (or steam) by using the electric heater 7 and the fuel cell system 8 even if only either the first auxiliary engine 31 or the second auxiliary engine 32 is operated H ₂ O) can be increased, so that it is possible not only to satisfy the demand of the customer 50 but also to meet the regulations on environmental pollution. The ship 1 according to the present invention can meet the demand of the customer 50 for electricity by further producing electricity using the fuel cell system 8. [

The economizer 4 is for generating steam (H ₂ O). The economizer 4 may be connected to the auxiliary engine 3 and the water supply unit 2 through conduits. Accordingly, the economizer 4 can be supplied with the high-temperature auxiliary engine exhaust gas from the auxiliary engine 3, and can receive water from the water supply unit 2. The economizer 4 can heat the water by providing a channel through which the water supplied from the water supply unit 2 flows, into the pipeline through which the auxiliary engine exhaust gas discharged from the auxiliary engine 3 is discharged . Therefore, the economizer 4 can generate steam (H ₂ O) by heating the water supplied from the water supply unit 2 with the exhaust gas discharged from the auxiliary engine 3 as a heat source. A plurality of the economizers 4 may be installed. For example, the economizer 4 may include a first economizer 41 and a second economizer 42.

The first economizer 41 may be connected to the water supply unit 2, the first auxiliary engine 31, and the demander 50 through a channel. Accordingly, the first economizer 41 receives water from the water supply unit 2 and can receive the auxiliary engine exhaust gas from the first auxiliary engine 31. The first economizer 41 can heat the water supplied from the water supply unit 2 by using the auxiliary engine exhaust gas discharged from the first auxiliary engine 31 as a heat source. Accordingly, the first economizer 41 can generate steam (H ₂ O). The steam (H ₂ O) generated in the first economizer 41 may be supplied to the fuel cell system 8 and the demander 50 through a channel. The auxiliary engine exhaust gas heated by the water in the first economizer 41 can be discharged to the outside of the hull. The auxiliary engine exhaust gas, which heats and discharges water in the first economizer 41, may be a flue gas.

The second economizer 42 may be connected to the water supply unit 2, the second auxiliary engine 32, and the demander 50 via a channel. Accordingly, the second economizer 42 receives water from the water supply unit 2 and can receive the auxiliary engine exhaust gas from the second auxiliary engine 32. The second economizer 42 can heat the water supplied from the water supply unit 2 by using the auxiliary engine exhaust gas discharged from the second auxiliary engine 32 as a heat source. Accordingly, the second economizer 42 can generate steam (H ₂ O). The steam (H ₂ O) generated in the second economizer 42 may be supplied to the fuel cell system 8 and the customer 50 through a channel. The auxiliary engine exhaust gas heated by the water in the second economizer 42 can be discharged to the outside of the hull. The auxiliary engine exhaust gas, which heats and discharges water in the second economizer 42, may be a flue gas.

The first economizer 41 and the second economizer 42 may be operated as the first sub engine 31 and the second sub engine 32 operate. That is, when the first auxiliary engine 31 is activated, the first economizer 41 can be operated. When the second auxiliary engine 32 is operated, the second economizer 42 can be operated. Only one of the first auxiliary engine 31 and the second auxiliary engine 32 operates when the ship 1 is moored in the port so that the first economizer 41 and the second economizer 42 ) Can be operated. In this case, the water supply unit 2 can supply water only to the economizer that is operated. Accordingly, the water supplied to the economizer to be operated can be generated as steam (H ₂ O) and supplied to the consumer 50.

At least one of the first auxiliary engine 31 and the first economizer 41 and between the second auxiliary engine 32 and the second economizer 42 is discharged from the fuel cell system 8, A merging portion 6 for merging the fuel cell exhaust gases may be provided. Accordingly, the auxiliary engine exhaust gas supplied from the auxiliary engine 3 to the economizer 4 may be merged with the fuel cell exhaust gas supplied through the merging portion 6. [ An electric heater (7) may be installed between the merger (6) and the economizer (4).

The branch portion (5) is installed to be positioned between the fuel storage tank (20) and the auxiliary engine (3). The branching section 5 may branch the fuel supplied from the fuel storage tank 20 to the auxiliary engine 3. [ The branching section 5 is connected to the auxiliary engine 3 (not shown) in the fuel storage tank 20 so that fuel is supplied to the auxiliary engine 3, the reformer 821 of the fuel cell system 8 and the combustor 822, Can be branched. The branching section 5 may be connected to the auxiliary engine 3, the reformer 821 and the combustor 822 through pipes such as pipes or pipes, respectively. The branching section 5 opens or closes the flow path of the conduits so that the fuel stored in the fuel storage tank 20 is supplied to at least one of the auxiliary engine 3, the reformer 821 and the combustor 822 . For example, the branch portion 5 may be a three-way valve. Accordingly, the reformer 821 can receive a part of the fuel supplied from the fuel storage tank 20 to the auxiliary engine 3. [ The reformer 821 may receive residual fuel except for the fuel supplied to the auxiliary engine 3. The branching unit 5 may block the fuel supplied to the auxiliary engine 3 and supply the fuel from the fuel storage tank 20 to the reformer 821. [ Accordingly, the reformer 821 is supplied with a greater amount of fuel than when the residual fuel is supplied, so that the fuel (anode) 811b of the fuel cell 81 is supplied with fuel Can be supplied. Therefore, the fuel cell 81 can produce a larger amount of electricity. The branch portion 5 may also be installed between the fuel storage tank 20 and the main engine 101.

The confluence portion 6 is installed to be positioned between the auxiliary engine 3 and the economizer 4. In this case, the electric heater 7 may be installed between the merging unit 6 and the economizer 4 so as to be positioned at the rear end of the merging unit 6. The merging unit 6 may merge the fuel cell exhaust gas discharged from the fuel cell system 8 and the auxiliary engine exhaust gas supplied to the economizer 4 from the auxiliary engine 3. [ The merging unit 6 may be installed in a first duct connecting the auxiliary engine 3 and the economizer 4 and may be connected to the fuel cell system 8 through a second duct. Accordingly, the merging portion 6 can join the fuel cell exhaust gas traveling along the second conduit to the auxiliary engine exhaust gas supplied to the economizer 4 along the first conduit. Since the fuel cell exhaust gas discharged from the fuel cell system 8 is at a high temperature of about 800 ° C, it can be joined to the auxiliary engine exhaust gas to further increase the temperature of the auxiliary engine exhaust gas. Further, as the auxiliary engine exhaust gas and the fuel cell exhaust gas are merged in the merging section 6, the flow rate of the exhaust gas supplied to the economizer 4 can be further increased before the fuel cell exhaust gas is merged have. Accordingly, the economizer 4 can produce a greater amount of steam (H ₂ O). The confluence portion 6 adjusts the degree of opening of the first conduit and the second conduit so that the amount of the auxiliary engine exhaust gas supplied to the economizer 4 and the amount of the fuel cell exhaust gas are adjusted differently It is possible.

The electric heater (7) is for heating the exhaust gas using electricity. The electric heater 7 may be installed between the confluent unit 6 and the economizer 4. For example, the electric heater 7 may be installed in a duct connecting the merging unit 6 and the economizer 4. Accordingly, the electric heater 7 can heat the exhaust gas supplied from the merging unit 6 to the economizer 4 by using electricity. Here, the exhaust gas supplied to the economizer 4 in the merging unit 6 may be a mixed exhaust gas in which the auxiliary engine exhaust gas and the fuel cell exhaust gas are mixed. The electric heater 7 can heat the exhaust gas by contacting the exhaust gas with the heat transfer member by raising the temperature of the heat transfer member such as a heat wire using electricity. The exhaust gas heated by the electric heater 7 can be supplied to the economizer 4. Accordingly, the economizer 4 can be supplied with exhaust gas at a temperature higher than that before passing through the electric heater 7. Accordingly, the ship 1 according to the present invention can be constructed so that the electric heater 7 heats the exhaust gas supplied to the economizer 4 from the confluence portion 6, and the steam H generated by the economizer 4 ₂ O) can be increased. In the vessel 1 according to the present invention, the electric heater 7 further increases the temperature of the exhaust gas supplied to the economizer 4 so that the economizer 4 generates steam (H ₂ O) The required load can be reduced. Therefore, the vessel 1 according to the present invention can extend the service life of the economizer 4, thereby reducing maintenance and replacement costs for the economizer 4. Only one electric heater 7 may be provided, but a plurality of electric heaters 7 may be provided to further increase or maintain the temperature of the exhaust gas.

The electric heater 7 may be connected to the first auxiliary engine 31, the second auxiliary engine 32 and the fuel cell 81, respectively. Specifically, the electric heater 7 may be connected to the first generator of the first auxiliary engine 31, the second generator of the second auxiliary engine 32, and the fuel cell 81 by electric wires. Accordingly, the electric heater 7 can receive electricity generated by at least one of the first auxiliary engine 31, the second auxiliary engine 32, and the fuel cell 81. The electric heater 7 can heat the exhaust gas supplied to the economizer 4 from the merging unit 6 using the supplied electricity. Accordingly, since the ship 1 according to the present invention does not need to separately provide a power generator for supplying electricity to the electric heater 7, it is possible not only to enhance space utilization for the hull, The installation cost for supplying electricity can be reduced.

Since the electric heater 7 does not need a chamber in which fuel and air are mixed and burned like an auxiliary boiler, the electric heater 7 is smaller in size than the auxiliary boiler. Accordingly, in the vessel 1 according to the present invention, not only the electric heater 7 can be easily installed in a narrow space as compared with the auxiliary boiler, but also the weight of the electric heater 7 in the hull is lower than that of the auxiliary boiler Therefore, the space utilization of the hull can be increased. In addition, since the vessel 1 according to the present invention can widen the gap spaced apart from the peripheral devices installed around the electric heater 7 as compared with the auxiliary boiler, the distance between the electric heater 7 and the peripheral devices So that maintenance work and replacement work for the electric heater 7 and peripheral devices can be performed smoothly. Accordingly, the maintenance work time and the replacement operation time for the electric heater 7 and the peripheral devices can be shortened by preventing the ship 1 according to the present invention from delaying the operation time.

The fuel cell system 8 according to the present invention produces electricity using fuel, steam (H ₂ O), and air. Vessel (1) according to the present invention can supply fuel to the fuel cell system 8 via the branch (5), a steam to said fuel cell system (8) through the economizer (4) (H ₂ O), and can supply air to the fuel cell system 8 through the air supply unit 30. [ The air supply unit 30 may supply air to the combustor 822 and the cathode 811a of the fuel cell system 8. [ Accordingly, the fuel cell system 8 according to the present invention can produce electricity.

The fuel cell system 8 according to the present invention supplies the fuel cell exhaust gas discharged from the fuel cell 81 to the merging section 6 so as to be discharged from the auxiliary engine 3 and supplied to the economizer 4 Lt; RTI ID = 0.0 > engine exhaust < / RTI > Accordingly, the amount of exhaust gas supplied to the economizer 4 is increased, thereby increasing the production of steam (H ₂ O). In addition, the fuel cell system 8 according to the present invention can additionally produce electricity separately from the auxiliary engine 3. [ Therefore, the vessel 1 according to the present invention can satisfy the demand amount of steam (H ₂ O) and the demanded place 50 for electricity.

The fuel cell system 8 according to the present invention can be used in a small structure such as a home or an automobile, and can be used in a large structure such as a ship. The fuel cell system 8 according to the present invention may be implemented to operate in conjunction with a diesel engine, a gas engine, a steam turbine, a gas turbine, or a Rankine Cycle system using the combustion energy of the fuel.

In this specification, the term " ship " is not limited to a structure for navigating a watercraft, and includes not only a structure for navigating a watercraft, but also a floating oil production storage and unloading facility (FPSO) It includes the same sea structure.

Hereinafter, the fuel cell system 8 according to the present invention will be described in detail with reference to the accompanying drawings.

2 to 5, the fuel cell system 8 according to the present invention includes a fuel cell 81, and a hydrogen generation unit 82. [ The fuel cell system 8 according to the present invention may be implemented by including a controller 83 for controlling the operation of all the components including the fuel cell 81, the hydrogen generator 82, and the like. In this specification, the raw material and the raw water that are introduced into the hydrogen generating portion 82, and the fuel that is generated in the hydrogen generating portion 82 and flows into the fuel cell 81 are defined as the fuel.

The fuel cell 81 is supplied with the hydrogen-containing fuel from the hydrogen generator 82 and can generate electricity through an electrochemical reaction. For example, the fuel cell 81 can generate electricity through an electrochemical reaction with the air supplied from the air supply unit 30 by receiving fuel containing hydrogen from the reformer 821. The fuel cell 81 is implemented including a fuel cell stack. The fuel cell stack has an electrolyte layer 811c formed between a cathode 811a and an anode 811b and an electrolyte layer 811c formed between the anode 811b and the cathode 811a A unit battery module in which a hydrogen separator for supplying hydrogen, air, and heat is installed is connected in series to the required number of units. Here, the fuel electrode (anode) 811b may receive fuel containing hydrogen from the reformer 821. The reformer 821 can produce hydrogen-containing fuel by performing a reforming reaction on fuel supplied from the branching unit 5 and steam (H ₂ O) supplied from the economizer 4. The fuel anode 811b may be supplied with fuel directly from the branch portion 5 without passing through the reformer 821 when the engine is a gas engine.

The fuel cell 81 is a temperature sensor and a device for maintaining the temperature. That is, a heater or a cathode fan, a fuel electrode fan, a cooling plate, or the like. The temperature sensor senses the temperature of the fuel cell stack, the temperature of the cathode 811a, and the temperature of the anode 811b. The heater can heat the fuel cell to maintain the temperature required for the operation. The air cathode fan dissipates heat generated from the cathode 811a of the fuel cell stack. The fuel electrode fan dissipates the heat generated from the anode 811b of the fuel cell stack. The air cathode fan and the anode cathode fan may be implemented as a part of a heat exchanger used in a fuel cell stack.

When the fuel cell system 8 according to the present invention includes the control unit 83, the control unit 83 controls the heater, the cathode fan, and the anode electrode fan using the signal output from the temperature sensor, ) Is appropriately maintained. For example, the control unit 83 maintains the operating temperature of the phosphoric acid fuel cell (PAFC) at 190 to 210 ° C, maintains the operating temperature of the MCFC at 550 to 650 ° C, In the case of oxide fuel cells (SOFC), the operating temperature is maintained at 650 to 1000 ° C. For polymer electrolyte fuel cells (PEMFC), the operating temperature is maintained at 30 to 80 ° C.

Hereinafter, the operation of the fuel cell 81 provided in the fuel cell system 8 according to the present invention will be described with reference to FIGS. 4A and 4B. 4A is a conceptual diagram of a solid oxide fuel cell (SOFC), and FIG. 4B is a conceptual diagram of a polymer electrolyte fuel cell (PEMFC).

4A, a solid oxide fuel cell (SOFC) 811 has a structure in which oxygen ions generated by a reduction reaction of oxygen at a cathode 811a are supplied to an anode 811b through an electrolyte 811c, . Fuel containing hydrogen (H ₂ ) flows in the anode 811b and oxygen ions O ^2- and hydrogen H ₂ moved to the anode 811b through the electrolyte 811c. It reacts electrochemically with water (H ₂ 0) and the electron (e ^-) is generated. Since electrons are consumed at the cathode 811a, electricity flows when the cathode 811a and the anode 811b are connected to each other.

The solid oxide fuel cell (SOFC) (811) is a fuel electrode (anode) of carbon monoxide (CO), which may be included in the fuel supplied to (811b), carbon dioxide (CO ₂₎ and electrochemical unreacted material and unreacted as hydrogen (H ₂ ) and to discharge the water (H ₂ 0 as a liquid or gaseous), such as residual material and reaction product. In addition, unreacted oxygen and nitrogen are discharged from the cathode 811a of the solid oxide fuel cell (SOFC) 811.

Referring to Figure 4b a polymer electrolyte fuel cell (PEMFC) (812) is a fuel electrode (anode) (812a) a catalyst layer (812b) of hydrogen (H ₂₎ is a hydrogen ion (H ⁺⁾ and electrons (e ^-) in the formed in the generation by do. The hydrogen ion (H ⁺ ) moves to the cathode 812d through the polymer electrolyte membrane (polymer membrane) 812c. The polymer electrolyte fuel cell (PEMFC) 812 reacts with hydrogen ions (H ⁺ ) and oxygen (O ₂ ) in the catalyst layer 812e formed on the cathode 812d to produce water (H ₂ O). When the catalyst layer 812b formed on the anode 812a and the catalyst layer 812e formed on the cathode 812d are connected to each other, electricity flows.

The polymer electrolyte fuel cell (PEMFC) 812 discharges residual material such as unreacted hydrogen (H ₂ ) from the catalyst layer 812b of the anode 812a. In addition, the polymer electrolyte fuel cell (PEMFC) 812 discharges unreacted oxygen and water (H ₂ O) from the air electrode (cathode) 812d.

Other molten carbonate fuel cell (MCFC) is a fuel electrode (anode) of hydrogen (H ₂₎ and carbonate ions (CO ₃ ^2-) in the reaction water (H ₂ O) and carbon dioxide (CO _2), electron (e ^-) in the Is generated. The generated carbon dioxide (CO ₂ ) is sent to the cathode, and carbon dioxide (CO ₂ ) and oxygen (O ₂ ) react with each other at the cathode to produce carbonate ion (CO ₃ ^-2 ). Carbonate ions (CO ₃ ^-2 ) migrate through the electrolyte to the anode. In a molten carbonate fuel cell (MCFC), carbon dioxide (CO ₂ ) generated in the process of generating electricity can be implemented to be circulated in the fuel cell without being discharged to the outside.

2 to 5, the hydrogen generating unit 82 includes a device for generating a fuel, that is, hydrogen (H ₂ ) gas, necessary for the anode 811 b of the fuel cell 81 by using the raw material . In this specification, the raw material and the raw water that are introduced into the hydrogen generating portion 82 and the fuel that is generated in the hydrogen generating portion 82 and flows into the fuel cell 81 are defined as the fuel.

The hydrogen generating unit 82 may be designed to have various structures depending on the type of the fuel cell 81 or for improving the electricity generation efficiency. For example, when the fuel cell 81 is a PAFC or a SOFC, the hydrogen generator 82 may include a reformer and a combustor . In another embodiment, when the fuel cell 81 is a molten carbonate fuel cell (MCFC) or a polymer electrolyte fuel cell (PEMFC), the hydrogen generating unit 82 may include a reformer and a combustor as well as a water gas shift reactor , ≪ / RTI > WGS).

The water gasification reactor (WGS) may be a high temperature shift reactor (HTS), a mid-temperature shift reactor (MTS), a low-temperature shift reactor (LTS) Or a carbon monoxide remover. The carbon monoxide remover may include a selective oxidation reactor (PROX) for burning and removing only carbon monoxide (CO), or a methanation reactor for reducing carbon monoxide (CO) to hydrogen (H ₂ ) .

Referring to FIG. 5, an example of the hydrogen generator 82 in the fuel cell system 8 according to the present invention will be described as follows.

The hydrogen generator 82 may include a reformer 821 and a combustor 822.

The reformer (Reformer) (821) advances a reforming reaction of the steam (H ₂ 0) supplied from the fuel and the economizer (4) which is supplied is branched by the branch (5) containing hydrogen (H ₂₎ Thereby generating a reforming gas. In the reforming reaction, the reformer 821 may utilize thermal energy provided by the combustor 822. Hereinafter, the reforming gas from the reformer 821 is defined as fuel.

The reformer 821 includes a reforming catalyst layer that induces a reforming reaction. The reforming catalyst layer has a structure in which the reforming catalyst is packed with a catalyst supported on the carrier. The reforming catalyst is composed of nickel (Ni), ruthenium (Ru), platinum (Pt) or the like. The shape of the carrier carrying the catalyst may be, for example, granular, pellet or honeycomb, Resistant metal such as alumina (Al ₂ O ₃ ), titania (TiO ₂ ), or the like.

In the fuel cell system 8 according to the present invention, the reformer 821 may be installed outside the fuel cell 81. In this case, the fuel cell 81 is implemented as an externally reforming type. In the fuel cell system 8 according to the present invention, the reformer 821 may be installed inside the fuel cell 81 in the form of a reforming catalyst layer. In this case, the fuel cell 81 is implemented as an internal reforming type.

The combustor 822 provides heat to the reformer 821 so that the reforming reaction proceeds smoothly. When the reformer heating temperature by the combustor 822 is low, the reforming reaction by the endothermic reaction of the reformer 821 does not progress well and moisture (water droplets) is generated in the reformer 821 . When the heating temperature of the combustor 822 is high, the catalytic activity of the reforming catalyst layer of the reformer 821 may be lowered.

The combustor 822 is connected to the fuel cell stack 81 through the fuel cell stack 81 so as to increase the efficiency of the entire system. The combustor 822 includes a raw material supplied from the fuel storage tank 20, an exhaust gas discharged from an anode 811b of the fuel cell stack of the fuel cell 81 , Or a mixture of the two can be used as the fuel. The combustor 822 may use the air supplied from the air supply unit 30. In the fuel cell system 8 according to the present invention, the combustor 822 may further use air discharged from the cathode 811a of the fuel cell stack of the fuel cell 81. [

Although not shown, the hydrogen generator 82 may further include at least one temperature sensor, which detects the temperature of the reformer 821. The temperature of the reformer 821 is controlled by the conditions of the configuration of the reformer 821 and the mixing ratio of the fuel and steam (H ₂ O) supplied from the branching section 5, The range changes. 3), the control unit 83 may control the operation of the combustor 822 (shown in FIG. 3) by using a signal output from the temperature sensor. In the case where the fuel cell system 8 according to an embodiment of the present invention includes the control unit 83 The temperature of the reformer 821 is controlled by increasing or decreasing the amount of raw material combustion. For example, the control unit 83 may be implemented to control the temperature within the range of about ± 20 ° C. with respect to the optimum temperature range.

Here, the gas generated through the reforming reaction in the reformer 821 includes not only hydrogen (H ₂ ) but also carbon monoxide (CO), carbon dioxide (CO ₂ ), and the like. When the fuel cell 81 is a polymer electrolyte fuel cell (PEMFC), carbon monoxide (CO) poison the electrode catalyst of the fuel cell stack of the polymer electrolyte fuel cell (PEMFC) to shorten the life of the fuel cell 81. In order to reduce the concentration of carbon monoxide (CO) to 10-20 ppm or less, the hydrogen generating unit 82 may further include an aqueous gasification reactor (WGS) 823.

The water gasification reactor (WGS) 823 reacts with carbon monoxide (CO) and steam (H ₂ O) to produce carbon dioxide (CO ₂ ) and hydrogen (H ₂ ). As shown in FIG. 5, the water gasification reactor (WGS) 823 may include a high temperature water gasification reactor (HTS) and a low temperature aqueous gasification reactor (LTS).

The optimum temperature of the high temperature aqueous gasification reactor (HTS) and the low temperature aqueous gasification reactor (LTS) varies depending on the type of the catalyst used and the composition of the gas discharged by the equilibrium of the control temperature is determined. Although not shown in FIG. 5, a cooler and a temperature sensor may be installed in the high temperature aqueous gasification reactor (HTS) and the low temperature aqueous gasification reactor (LTS), respectively. When the fuel cell system 8 according to the present invention includes the control unit 83 (shown in FIG. 3), the control unit 83 controls the cooler using the signal output from the temperature sensor, (HTS) and the temperature of the low temperature aqueous gasification reactor (LTS). For example, the high temperature aqueous gasification reactor (HTS) is controlled within a range of 300 to 430 ° C, and the low temperature aqueous gasification reactor (LTS) is controlled within a range of 200 to 250 ° C.

Although not shown, the water gasification reactor (WGS) 823 may include a carbon monoxide remover. The carbon monoxide remover removes a very small amount of carbon monoxide (CO) that is not completely treated in the low temperature aqueous gasification reactor (LTS) at the end of the low temperature water gasification reactor (LTS). The carbon monoxide remover includes a selective oxidation unit (PROX), which receives air from an air supply unit and burns only the carbon monoxide (CO) in the gas discharged from the low temperature aqueous gasification reactor (LTS) H ₂ ) to reduce the concentration thereof.

The selective oxidation reactor (PROX) is equipped with a cooler and a temperature sensor. In the case where the fuel cell system 8 according to an embodiment of the present invention includes the control unit 83 (shown in FIG. 3), the control unit 83 controls the cooler by using a signal output from the temperature sensor The temperature of the selective oxidation reactor (PROX) is controlled. For example, the selective oxidation reactor (PROX) is controlled within the range of 120 to 160 占 폚. However, the optimal temperature of the selective oxidation reactor (PROX) is set differently depending on conditions such as the type of catalyst used and the method of use.

The catalyst layer of the selective oxidation reactor (PROX) is composed of a structure filled with a carrier carrying a selective oxidation catalyst. The selective oxidation catalyst is made of platinum (Pt) or the like, and the shape of the support carrying the catalyst may be, for example, a granular shape, a pellet shape, a honeycomb shape, etc. The material constituting the support may be alumina (Al ₂ O ₃ ) , Magnesium oxide (MgO), and the like.

Hereinafter, a ship 1 according to the present invention will be described in detail with reference to the accompanying drawings. Since the fuel cell system 8 according to the present invention is included in the vessel 1 according to the present invention, the vessel 1 according to the present invention will be described together.

Fig. 6 is a schematic block diagram of a ship according to the present invention. Fig. 7 is a schematic block diagram for explaining a fuel cell system and an electric heater in a ship according to the present invention. Fig. FIG. 9 is a schematic block diagram for explaining a power storage unit in a ship according to the present invention. FIG. 1 to 5, the same reference numerals are used.

6 to 8, a ship 1 according to the present invention includes an engine exhaust system 100, a fuel storage tank 20, a water supply unit 2, a branching unit 5, a merging unit 6, An electric heater 7 and a fuel cell system 8 according to the present invention. The ship 1 according to the present invention may further include an air supply unit 30, a power conversion unit 40, and a customer 50. The engine exhaust system 100 may include a main engine 101, a main economizer 102, a steam turbine 103, an auxiliary engine 3 and an economizer 4. The fuel cell system 8 may include a fuel cell 81, a hydrogen generator 82, and a controller 83. Here, the hydrogen generator 82 may include a reformer 821 and a combustor 822. The fuel cell 81 may include an anode 811b to receive fuel and a cathode 811a to receive air.

In the ship 1 according to the present invention, the engine exhaust system 100, the fuel storage tank 20, the air supply unit 30, the power conversion unit 40, the demander 50, The detailed description of the supply unit 2, the branching unit 5, the merging unit 6, the electric heater 7 and the fuel cell system 8 according to the present invention has been described above, The configuration and effects according to the present invention will be described.

Referring to FIGS. 6 to 8, in the fuel cell system 8 according to the present invention, the reformer 821 may be connected to the branch 5 through a channel. Accordingly, the reformer 821 can be supplied with the fuel branched by the branch portion 5. In this case, the reformer 821 may receive some of the fuel supplied to the auxiliary engine 3 from the fuel storage tank 20. [ The reformer 821 may be connected to the economizer 4 through a conduit. The reformer 821 reforms hydrogen supplied to the anode 811b by reforming the fuel supplied from the branching unit 5 and the steam H ₂ 0 supplied from the economizer 4 It can produce fuel including. The amount of fuel supplied to the anode 811b may vary depending on the amount of steam H ₂ 0 supplied from the economizer 4. For example, when the amount of steam (H ₂ 0) supplied from the economizer 4 is large, the amount of hydrogen supplied to the fuel electrode (anode) 811b may increase. When the customer 50 does not use the steam H ₂ 0, the reformer 821 can receive all the steam H ₂ 0 from the economizer 4, so that the anode 811 b Can be increased. Accordingly, the fuel cell system 8 according to the present invention can increase the amount of electricity produced. Although not shown, a steam storage unit for storing steam (H ₂ 0) may be installed between the economizer 4 and the demander 50. Accordingly, the customer 50 can use the steam H ₂ 0 stored in the steam storage unit when the steam H ₂ 0 is required. The anode 811b may be supplied with fuel directly from the branch portion 5 without passing through the reformer 821 when the engine 101 is a gas engine.

Therefore, the fuel cell system 8 according to the present invention can achieve the following operational effects.

First, the fuel cell system 8 according to the present invention can receive the fuel and the steam H ₂ 0 from the fuel storage tank 20 installed in the hull 11 and the economizer 4, it is possible to omit the fuel supply device and receiving a supply of steam (H ₂ 0) for receiving a steam generating device can be not only to reduce the construction cost of generating electricity increased space utilization.

Second, the fuel cell system 8 according to the present invention receives steam (H ₂ O) from the economizer 4 and can receive fuel from the fuel storage tank 20, The fuel cell 81 can further generate electricity, thereby increasing the amount of electricity produced.

6 to 8, in the fuel cell system 8 according to the present invention, the fuel cell 81 may be connected to the electric heater 7 through a wire. Accordingly, the fuel cell 81 can supply the electricity produced by the electric heater 7 to the electric heater 7. The electric heaters 7 may be connected to the plurality of auxiliary engines 3 through electric wires, respectively. The electric heater 7 is supplied from the merging unit 6 to the economizer 4 by using electricity produced by at least one of the plurality of auxiliary engines 3 and the fuel cell 81 The exhaust gas can be heated. Therefore, the fuel cell system 8 according to the present invention can achieve the following operational effects.

First, the fuel cell system 8 according to the present invention is realized such that the electric heater 7 uses electricity produced by at least one of the plurality of auxiliary engines 3 and the fuel cell 81, It is not necessary to separately provide an electric supply device for supplying electricity to the heater 7. [ Accordingly, the fuel cell system 8 according to the present invention can reduce the construction cost for producing electricity and can omit the electric supply device, thereby increasing the space utilization of the hull 11.

Second, since the fuel cell system 8 according to the present invention can supply electricity continuously to the electric heater 7 even if any of the auxiliary engine 3 and the fuel cell 81 is damaged or broken, It is possible to prevent the exhaust gas heating for increasing the production amount of H ₂ O from being interrupted.

Third, the ship 1 according to the present invention operates only a part of a plurality of auxiliary engines 3. That is, the exhaust gas supplied to the economizer 4 can be heated by using the electric heater 7 even when it is anchored in a port, so that the amount of steam (H ₂ 0) produced by the economizer 4 is increased, It is possible to satisfy the steam demand amount required by the steam generator 50.

6 to 8, in the fuel cell system 8 according to the present invention, the fuel cell 81 may be connected to a plurality of economizers 4 through a channel. Accordingly, the fuel cell 81 can supply the fuel cell exhaust gas to at least one of the plurality of economizers 4. For example, when only the first sub-engine 31 of the plurality of sub-engines 3 is activated as shown in FIG. 8, the fuel cell 81 is connected to the first sub-engine 31 in the first economizer 31 41 to the auxiliary engine exhaust gas. Accordingly, the fuel cell exhaust gas discharged from the fuel cell 81 may be joined to the auxiliary engine exhaust gas supplied from the first auxiliary engine 31 to the first economizer 41. [ The fuel cell exhaust gas may be discharged from at least one of the cathode 811a and the anode 811b. Therefore, the fuel cell system 8 according to the present invention increases the flow rate of the exhaust gas to be supplied to the economizer 4, so that the economizer 4 generates a larger amount of steam (for example, H ₂ 0), it is possible to satisfy the demanded amount of steam (H ₂ 0) required by the demander 50.

6 to 8, in the fuel cell system 8 according to the present invention, the electric heater 7 is installed at the front end of the economizer 4, and the exhaust gas 7 supplied to the economizer 4 Can be heated. The electric heater 7 is capable of heating the mixed exhaust gas supplied to the economizer 4 by joining and mixing the auxiliary engine exhaust gas and the fuel cell exhaust gas at the merging portion 6. Thus, the economizer 4 can be supplied with the exhaust gas at a higher temperature than the exhaust gas before passing through the electric heater 7. Therefore, the fuel cell system 8 according to the present invention can further increase the production amount of the steam (H ₂ 0) of the economizer 4, so that the demand amount of the steam (H ₂ 0) You can be more satisfied.

Referring to FIG. 9, the ship 1 according to the present invention may further include a power storage unit 9.

The power storage unit 9 is for storing electricity. The power storage unit 9 may be connected to one of the plurality of auxiliary engines 3 and the fuel cell 81 via a wire. The power storage unit 9 may be an energy storage system capable of storing electricity. Accordingly, the power storage unit 9 can receive and store electricity produced by at least one of the plurality of auxiliary engines 3 and the fuel cell 81. [ Although not shown, the power storage unit 9 may be connected to the main power generator to store electricity generated by the main power generator when the main engine 101 is operated. The power storage unit 9 may be one large-capacity electric storage unit, but is not limited thereto, and a plurality of low-capacity electric storage units may be connected as long as electricity can be stored. In this case, the low-capacity electric storage devices may be connected in series or in parallel. The other side of the power storage unit 9 may be connected to the electric heater 7 through electric wires. Accordingly, the electric power storage unit 9 can supply electricity to the electric heater 7 when the electric heater 7 is activated. The electric heater 7 may be activated when the amount of steam (H ₂ O) required by the customer 50 exceeds a predetermined reference steam demand. In this case, the electric heater 7 can heat the exhaust gas using the electricity stored in the electric power storage unit 9. The reference steam demand amount refers to the amount of steam (H ₂ O) used on average by the demander 50, and can be set in advance by an operator. The electric heater 7 may not be operated or operated according to the steam demanded by the demander 50.

For example, the electric heater 7 may be operated when the amount of steam (H ₂ O) required by the demander 50 exceeds a preset reference steam demand amount. In this case, the electric heater 7 can be operated using the electricity stored in the electric power storage unit 9. Accordingly, the electric heater 7 can heat the exhaust gas supplied to the economizer 4 from the confluent portion 6. [

For example, the electric heater 7 may not be operated if the amount of steam (H ₂ O) required by the demander 50 is equal to or less than a predetermined reference steam demand amount. In this case, the amount of steam (H ₂ O) produced by the economizer 4 can satisfy the amount of steam (H ₂ O) required by the consumer 50.

Therefore, the fuel cell system 8 according to the present invention can achieve the following operational effects.

First, the fuel cell system 8 according to the present invention heats the exhaust gas using electricity stored in the electric power storage unit 9 only when the electric heater 7 is operated. Therefore, the electric power stored in the electric power storage unit 9, It is possible to prevent the electric power stored in the electric heater 7 from being wasted and to increase the service life of the electric heater 7.

Second, in the fuel cell system 8 according to the present invention, when the power storage unit 9 is under sailing, electricity is supplied from the main power generator and stored, And the fuel cell 81, it is possible to prevent electricity from being consumed for operating the electric heater 7.

Third, the fuel cell system 8 according to the present invention stores electricity at all times in the power storage unit 9 in case the electric heater 7 is operated. Therefore, the first auxiliary engine 31, Even if at least one of the second auxiliary engine 32 and the fuel cell 81 is damaged or broken and can not be operated, the electric heater 7 can be used for the exhaust The gas can be heated. Therefore, when the amount of steam (H ₂ O) required by the demander 50 is large, the fuel cell system 8 according to the present invention can use the electricity stored in the electric power storage unit 9, and enabling rapid operation 7) the steam (H ₂ O) by the amount of steam (H ₂ O) to the consumer (50) the request can be quickly supplied.

It will be apparent to those skilled in the art that various modifications and variations can be made in the present invention without departing from the spirit or scope of the invention. Will be clear to those who have knowledge of.

1: Ships
2: water supply part 3: auxiliary engine
4: Economizer 5:
6: junction 7: electric heater
8: Fuel cell system 9: Power storage unit
31: first auxiliary engine 31: second auxiliary engine
41: First Economizer 42: Second Economizer
81: fuel cell 82: hydrogen generation unit
83:

Claims (6)

A water supply unit installed on the hull and supplying water;
A plurality of auxiliary engines installed to be spaced apart from the water supply unit and generating electricity;
A plurality of economizers for generating steam (H ₂ O) required by a customer by heating water supplied from the water supply unit using the auxiliary engine exhaust gas discharged from the auxiliary engines as a heat source;
A branching portion for branching the fuel supplied to the auxiliary engine from a fuel storage tank for storing fuel;
A fuel cell system for generating electricity using fuel supplied from the branching portion and steam supplied from the economizer;
A merging unit for merging the fuel cell exhaust gas discharged from the fuel cell system and the auxiliary engine exhaust gas supplied from the auxiliary engine to the economizer; And
And an electric heater installed to be positioned between the merging unit and the economizer and for heating the exhaust gas supplied from the merging unit using electricity,
The fuel cell system includes:
A hydrogen generator including a reformer and a combustor for reforming the fuel supplied from the branch and the steam supplied from the economizer; And
A fuel cell comprising an anode, an anode, and an electrolyte formed between the anode and the cathode,
Wherein the exhaust gas heated by the electric heater is supplied to the economizer so that the amount of steam (H ₂ O) produced by the economizer increases. The method according to claim 1,
Wherein the electric heater heats the exhaust gas supplied to the economizer using electricity produced by at least one of the plurality of auxiliary engines and the fuel cell. The method according to claim 1,
And a power storage unit for storing electricity produced by at least one of the plurality of auxiliary engines and the fuel cell,
Wherein the electric heater is installed to be connected to the electric power storage unit. When the amount of steam (H ₂ O) required by the customer is greater than a preset reference steam consumption amount, the electricity stored in the electric power storage unit is used to charge the electric power to the economizer And the exhaust gas to be supplied is heated. A fuel supply system for supplying fuel to a plurality of auxiliary engines for producing electricity in a fuel storage tank for storing fuel, the fuel being supplied from a branching portion for branching the fuel supplied to the auxiliary engines and the auxiliary engine exhaust gas discharged from the auxiliary engines, A hydrogen generator including a reformer and a combustor for reforming steam supplied from a plurality of economizers for generating steam (H ₂ O) required by a customer by heating water supplied from a water supplier; And
A fuel cell including an anode, an anode, and an electrolyte formed between the anode and the cathode,
A fuel cell exhaust gas discharged from the fuel cell and a subsidiary engine exhaust gas supplied to the economizer from the auxiliary engine; and an exhaust gas supply unit installed to be positioned between the economizer and supplied from the merging unit using electricity, Is supplied to the economizer so that the amount of steam (H ₂ O) produced by the economizer is increased. 5. The method of claim 4,
Wherein the electric heater heats the exhaust gas supplied to the economizer using electricity produced by at least one of the plurality of auxiliary engines and the fuel cell. 5. The method of claim 4,
And a power storage unit for storing electricity produced by at least one of the plurality of auxiliary engines and the fuel cell,
Wherein the electric heater is installed to be connected to the electric power storage unit. When the amount of steam (H ₂ O) required by the customer is greater than a preset reference steam consumption amount, the electricity stored in the electric power storage unit is used to charge the electric power to the economizer And the exhaust gas to be supplied is heated.

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