JP2016175821A - Hydrogen generation system - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a hydrogen generation system in which hydrogen can be efficiently generated from organic hydride, energy loss at this time is reduced, and energy saving is caused.SOLUTION: Provided is a hydrogen generation system where microwaves are applied in the presence of a metal carrier catalyst, containing: a reaction vessel 11 filled with the metal carrier catalyst; an organic hydride feed part 12 of feeding the organic hydride to the reaction vessel 11; and a microwave feed part 20 of applying the microwaves to the reaction vessel 11, and the organic hydride is fed to the reaction vessel 11 at the flow velocity of 0.3 to 0.7 mL/min by the organic hydride feed part 12.SELECTED DRAWING: Figure 3

Description

  The present invention relates to a hydrogen generation system that generates hydrogen from organic hydride, and more particularly to a hydrogen generation system that generates hydrogen from organic hydride using selective heating by microwave irradiation.

Conventionally, a fuel cell is known as a clean power generation device that does not emit CO ₂ , but hydrogen as a fuel is a gas at normal temperature and pressure, and it is difficult to handle from the viewpoint of safety, and its storage There is a problem with transportation. For this reason, in recent years, an attempt has been made to develop a technique for storing and transporting hydrogen in large quantities and safely using a dehydrogenation reaction of an organic hydride (see, for example, Patent Document 1).

JP 2004-26593 A

  However, when extracting hydrogen from the organic hydride, heat energy must be applied (for example, heating to a temperature of about 250 to 350 ° C. in the presence of a catalyst), and overall energy efficiency Therefore, there is a demand for a technique for efficiently generating hydrogen from organic hydride with less energy loss.

  Therefore, the present inventors have focused on selective heating by microwave irradiation, and as a result of intensive studies to provide a hydrogen generation system with less energy loss, the present invention has been completed.

  That is, an object of the present invention is to provide an energy-saving hydrogen generation system that can efficiently generate hydrogen from an organic hydride with little energy loss.

  A hydrogen generation system according to the present invention is a hydrogen generation system that generates hydrogen from an organic hydride by irradiating microwaves in the presence of a metal-supported catalyst, and a reaction vessel filled with the metal-supported catalyst, and a reaction vessel An organic hydride supply unit that supplies organic hydride to the reaction vessel and a microwave supply unit that irradiates the reaction vessel with microwaves. It is as composition to supply to.

  According to the present invention, it is possible to provide an energy-saving hydrogen generation system with less energy loss.

It is explanatory drawing which shows the outline of the hydrogen production | generation system which concerns on embodiment of this invention. It is explanatory drawing which shows the outline of the hydrogen production | generation part of the hydrogen production | generation apparatus shown in FIG. It is a graph which shows the relationship between the flow rate of decalin supplied to a reaction container, and the production rate of naphthalene produced | generated by dehydrogenation of decalin. It is a graph which contrasts the result of Example 10 and Comparative Example 10. It is explanatory drawing which shows the outline of the elementary generation apparatus suitable for embodiment of this invention.

  Hereinafter, preferred embodiments of a hydrogen generation system according to the present invention will be described with reference to the drawings.

In this embodiment, microwaves are irradiated in the presence of the metal-supported catalyst to generate hydrogen from the organic hydride. For example, it can be implemented using a hydrogen generator as shown in FIG. .
FIG. 1 is an explanatory diagram showing an outline of a hydrogen generation apparatus suitable for use in the present embodiment. The hydrogen generation apparatus 1 includes a hydrogen generation unit 10 and a microwave supply unit 20.

As shown in FIGS. 1 and 2, the hydrogen generation unit 10 includes a reaction vessel 11 filled with a metal-supported catalyst and an organic hydride supply unit 12 that supplies organic hydride to the reaction vessel 11.
The reaction vessel 11 is a cylindrical vessel formed of a material that can transmit microwaves, such as a quartz tube, and one end side thereof is connected to the organic hydride supply unit 12 via a connection tube 13. Has been. The organic hydride is supplied to the reaction vessel 11 at a predetermined flow rate by a pump P provided in the organic hydride supply unit 12.
Further, a hydrogen storage container (not shown) is connected to the other end side of the reaction container 11 through a connection pipe 14.

  The microwave supply unit 20 includes a microwave oscillator 21 that generates and outputs a microwave, and the microwave oscillator 21 is connected to a waveguide 23 by a coaxial cable 22.

The microwave oscillator 21 is a semiconductor microwave oscillator including a microwave generation unit configured using a semiconductor element. The microwave generation unit includes, for example, a semiconductor amplification element such as a transistor and a resonance such as a tank circuit. It consists of a circuit. A Hartley oscillation circuit, a Colpitts oscillation circuit, or the like can be used for the microwave generation unit.
In addition to the microwave generator, the microwave oscillator 21 has, for example, a function of changing the frequency of the microwave and a function of changing the output of the microwave.

The waveguide 23 is a microwave propagation unit that propagates the microwave transmitted via the coaxial cable 22 to the installation position of the reaction vessel 11, and the reaction vessel in which the reaction vessel 11 provided in the hydrogen generation unit 10 is installed. An installation unit 24 is provided.
The reaction vessel installation portion 24 has through holes that are opened in both the upper surface portion and the lower surface portion, so that the reaction vessel 11 of the hydrogen generation unit 10 can be inserted. In order to prevent microwave leakage, a member for closing the through-hole after inserting the reaction vessel 11 is attached.

  Further, the waveguide 23 is provided with an isolator 25 so that the reflected wave does not return to the microwave oscillator 21, so that the microwaves are phase-matched by a tuner 26 such as a three-tab tuner or an EH tuner. It is. A short plunger 27 for reflecting a microwave to form a standing wave is provided on the end side of the waveguide 23. By adjusting the position of the short plunger 27, the position of the maximum electric field strength of the microwave standing wave is positioned in the transfer container setting unit 24, and the power of the microwave traveling wave and the reflected wave is measured by the power monitor 28. Is measured and displayed.

  In this embodiment, using such a hydrogen generator 1, the organic hydride is supplied from the organic hydride supply unit 12 to the reaction vessel 11 while irradiating the reaction vessel 11 filled with the metal-supported catalyst with microwaves. .

  The organic hydride is generally an organic compound that reversibly releases hydrogen through a catalytic reaction. For example, cyclic hydrocarbons obtained by hydrogenating aromatic hydrocarbons such as decalin, tetralin, cyclohexane or derivatives thereof are preferably used because of their high hydrogen content, but are liquid at room temperature and release hydrogen by a dehydrogenation reaction. If it does, it is not limited to these.

In this embodiment, the dehydration reaction of the organic hydride is promoted by the catalytic action of the metal-supported catalyst. However, after the hydrogen atoms desorbed from the organic hydride are adsorbed on the carrier, the metal is used as a catalyst component. Quickly desorbs into the gas phase as hydrogen molecules. This is explained as a reverse spillover phenomenon, and the specific composition of the metal-supported catalyst is not particularly limited as long as the catalyst activity can be sustained over a long period of time and microwave heating is possible. For example, a metal-supported catalyst obtained by supporting one or more metals such as palladium and platinum as a catalyst component on a porous carrier such as activated carbon can be used.
The composition ratio of the metal-supported catalyst is usually such that the metal as the catalyst component is supported in a proportion of 0.001 to 30 wt%, preferably 0.01 to 20 wt%, more preferably 1 to 15 wt%. It is not limited.

  The organic hydride dehydrogenation proceeds by applying thermal energy in the presence of a catalyst, but most of the organic hydride has low polarity and is not heated by microwaves. Therefore, according to this embodiment, when the metal-supported catalyst and the organic hydride in the reaction vessel 11 are irradiated with microwaves, the metal-supported catalyst is selectively heated to generate thermal energy necessary for the dehydrogenation reaction. Can be made. As a result, energy loss can be reduced and hydrogen can be generated efficiently.

In this embodiment, when the metal-supported catalyst and the organic hydride in the reaction vessel 11 are irradiated with microwaves, the organic hydride is supplied to the reaction vessel 11 at a flow rate of 0.3 to 0.7 mL / min. By adjusting the flow rate of the organic hydride supplied to the reaction vessel 11 in such a range, hydrogen can be efficiently generated from the organic hydride. If the above range is exceeded, the contact time (reaction time) between the organic hydride and the metal-supported catalyst is short, and the amount of unreacted organic hydride tends to increase. If the amount is less than the above range, the contact time (reaction time) between the organic hydride and the metal-supported catalyst is long and the amount of unreacted organic hydride decreases, but the supply amount of organic hydride per unit time decreases. , Tend to be inefficient.
From the viewpoint of efficiently generating hydrogen from organic hydride, the flow rate per unit cross-sectional area of the reaction vessel 11 is preferably 0.006 to 0.014 mL / min · mm ² .

  In the present embodiment, it is preferable that the particle size of the metal-supported catalyst filled in the reaction vessel 11 is 100 μm or less. By reducing the particle size of the metal-supported catalyst in this way, the total surface area of the powder, which is the metal-supported catalyst, is increased, and the contact area with the organic hydride is increased, so that hydrogen is generated more efficiently from the organic hydride. can do.

  Furthermore, in the present embodiment, the microwave output is preferably 270 to 370 W. By adjusting the microwave output to such a range, it is possible to easily raise the temperature of the metal-supported catalyst to a temperature required for the dehydration reaction of the organic hydride, and even if the organic hydride is continuously supplied, The temperature can be easily maintained and hydrogen can be efficiently generated without disturbing the dehydration reaction of the organic hydride.

  Hereinafter, the present invention will be described in more detail with reference to specific examples.

[Examples 1-9, Comparative Examples 1-9]
As a hydrogen generator, a single-mode hydrogen generator 1 (cross-section of the waveguide 23: 38.1 × 102.5 mm) as shown in FIG. 1 is used, and a semiconductor-type microwave oscillator ( Fuji Electric Koki Co., Ltd. product: GNU-201AE) was used. The frequency of the microwave was 2.45 GHz.

A quartz tube (tube length: 25 cm, inner diameter: 4 mm) was used as the reaction vessel 11, and 0.5 g of a metal-supported catalyst (average particle size: 97.5 μm, mesh size: 45 to 150 μm) in which 2 wt% of palladium was supported on activated carbon. The reaction vessel 11 was filled with glass wool on the top and bottom.
The reaction vessel 11 is fixed at a position where the electric field is maximized inside the reaction vessel installation portion 24 of the waveguide 23, the microwave oscillator 21 is activated, and the reaction is performed while irradiating the microwave with the output shown in Table 1. Hydrogen was generated by supplying 3 mL of decalin from the organic hydride supply unit 12 to the container 11 at a flow rate shown in Table 1. Thereafter, naphthalene and tetralin, which are products of decalin dehydrogenation, and unreacted decalin are recovered and quantified from the reaction system, and the molar ratio [%] of naphthalene is obtained. The production rate [% / min] was calculated. The results are shown in Table 1 and graphically shown in FIG.
The graph shown in FIG. 3 is a graph in which the horizontal axis represents the flow rate [mL / min] and the vertical axis represents the production rate of naphthalene [% / min].

The production rate of naphthalene calculated here corresponds to the production rate of hydrogen accompanying the production of naphthalene. From the graph shown in FIG. 3, the hydrogen production rate is 0.5 mL / min for any microwave output. It can be confirmed that the production rate of hydrogen is maximized, and hydrogen can be efficiently generated in the range of 0.3 to 0.7 mL / min. Further, since the cylindrical inner diameter of the reaction vessel 11 is 4 mm, the flow rate of the organic hydride per unit cross-sectional area in the cylindrical radial cross section is 0.0060 to 0 from the viewpoint of generating hydrogen more efficiently. 0139 mL / min · mm ² is preferable.

[Example 10]
While supplying methylcyclohexane at a flow rate of 0.2 mL to a quartz tube filled with 2.5 g of a metal-supported catalyst (average particle size: 97.5 μm, mesh size: 45 to 150 μm) with palladium supported on activated carbon at 2 wt%, Irradiated with waves. At this time, the temperature of the reaction system was measured and found to be about 330 °.
From the start of microwave irradiation, the change in the yield of hydrogen over time was determined. A graph of the results is shown in FIG.

[Comparative Example 10]
Ceramics while supplying methylcyclohexane at a flow rate of 0.2 mL into a quartz tube filled with 2.5 g of a metal-supported catalyst (average particle size: 97.5 μm, mesh size: 45 to 150 μm) with 2 wt% palladium supported on activated carbon Heated with a heater. The heating conditions were such that the temperature of the reaction system was about 330 °, the same as in Example 10.
From the start of heating with the ceramic heater, the change in the yield of hydrogen over time was determined. A graph of the results is shown in FIG.

  As can be seen from the graph shown in FIG. 4, according to the hydrogen generation system of the present embodiment, a high yield of hydrogen can be generated in a short time, and a small amount of hydrogen can be generated each time a predetermined amount is required. For example, the hydrogen generation system can be suitably used for home use.

  As mentioned above, although preferable embodiment of the hydrogen generation system of this invention was described, the hydrogen generation system which concerns on this invention is not limited only to embodiment mentioned above, A various change implementation is possible in the range of this invention. Needless to say.

For example, in the above-described embodiment, the hydrogen generator 1 configured to irradiate the reaction vessel 11 with the microwave in a kind of resonance state using the waveguide 23 is used. The configuration is not limited to this. The hydrogen generator may be configured as shown in FIG.
In addition, FIG. 5 is explanatory drawing which shows the outline of the hydrogen generator which concerns on this modification.

  The hydrogen generator shown in FIG. 5 includes a cylindrical reaction vessel 111 made of a material that can transmit microwaves, such as a quartz tube, as in the above-described device. Inside the reaction vessel 111, The same metal-supported catalyst as described above is filled.

  The reaction vessel 111 is installed so as to stand in a vertical direction in a processing chamber 100 formed so that microwaves do not leak, and organic hydride is supplied from below. As a result, the organic hydride supplied to the reaction vessel 111 rises in the reaction vessel 111 through the gap between the metal supported catalysts heated by the microwaves irradiated from the microwave supply unit 102, and the metal supported catalyst. The dehydrogenation reaction proceeds by the catalytic action. When hydrogen is generated by the dehydrogenation reaction of the organic hydride, the generated hydrogen gas is collected from above the reaction vessel 111 and the dehydride of the organic hydride can be recovered.

At this time, since the organic hydride is normally supplied at normal temperature, a temperature distribution is generated in the metal-supported catalyst due to heat transfer from the metal-supported catalyst to the organic hydride, and the temperature on the side where the organic hydride is supplied is lowered. Tend.
In promoting the dehydrogenation reaction of the organic hydride by the catalytic action of the metal-supported catalyst, there is a preferable temperature range for allowing the reaction to proceed efficiently. For this reason, it is not preferable that a temperature distribution exists in the metal-supported catalyst, and it is desired to maintain a uniform temperature as a whole.
This modification is for reducing the temperature distribution of such a metal-supported catalyst and allowing the dehydrogenation reaction to proceed efficiently.

  Therefore, the hydrogen generator according to this modification is a hydrogen generator that generates hydrogen from an organic hydride by irradiating microwaves in the presence of a metal-supported catalyst, and is a reaction filled with the metal-supported catalyst. A container, and a microwave supply unit that irradiates the microwave to the reaction container, wherein the microwave supply unit is disposed along a longitudinal direction of the reaction container; and the antenna element And a phase control circuit connected corresponding to each of the antenna elements, and a composition wave of microwaves radiated from each of the antenna elements with a phase controlled is irradiated to the reaction vessel with a predetermined directivity It is as.

  The microwave supply unit 102 includes a plurality of antenna elements 103 arranged along the longitudinal direction of the reaction vessel 111 and a phase control circuit 104 connected to each of the antenna elements 103. In the example shown in FIG. 5, each antenna element 103 is connected to the demultiplexing circuit 105 via the phase control circuit 104. A microwave oscillator 106 is connected to the demultiplexing circuit 105, and the microwave generated by the microwave oscillator 106 is demultiplexed to each antenna element 103 by the demultiplexing circuit 105.

In the example shown in FIG. 5, the temperature sensor 101 is attached to the reaction vessel 111 so as to be embedded in the metal-supported catalyst. As a result, the temperature distribution of the metal-supported catalyst can be monitored as needed, and the temperature distribution information of the metal-supported body monitored by the temperature sensor 101 is input to the arithmetic processing unit 107.
The temperature sensor 101 may be a non-contact type sensor using infrared rays or the like, but is preferably a contact type sensor as illustrated in consideration of the influence of microwaves.

  The position information of the antenna element 103 with respect to the reaction vessel 111 is input to the arithmetic processing unit 107 in advance. Based on this position information and the temperature distribution information from the temperature sensor 101, the information processing unit 107 corresponds to each antenna element 103. A phase displacement amount in the connected phase control circuit 104 is calculated. Based on the calculation result, the phase of the microwave radiated from each antenna element 103 is controlled, and the microwave radiated with the phase controlled from each antenna element 103 is synthesized by the Huygens-Fresnel principle. The synthesized wave is irradiated to the reaction vessel 111 with a predetermined directivity.

  Thereby, the directivity of the microwave is controlled so that the microwave is concentrated on the low temperature portion of the metal-supported catalyst filled in the reaction vessel 111, or the microwave is swept, so that the reaction vessel 111 The heating temperature of the packed metal-supported catalyst is maintained uniformly so that the dehydration reaction of the organic hydride can be performed efficiently.

  An amplifier circuit may be connected to each antenna element 103 together with the phase control circuit 104 as necessary to amplify the phase-controlled microwave, or an isolator may be connected to block the reflected microwave. It may be. As the antenna element 103, a planar antenna such as a microstrip antenna (patch antenna) can be used, but the microwave supply unit 102 may be configured using a phased array antenna. When a phased array antenna is used, either an active type or a passive type may be used.

  In the example shown in FIG. 5, four antenna elements 103 are arranged in a line along the longitudinal direction of the reaction vessel 111, but the arrangement of the antenna elements 103 is arbitrarily selected depending on the size of the reaction vessel 111. it can. Depending on the length of the reaction vessel 111, a predetermined number of antenna elements 103 can be arranged at intervals of half or less of the wavelength of the emitted microwaves. Further, the antenna elements 103 are arranged around the reaction vessel 111. It is good also as multiple rows so that it may surround.

  The microwave oscillator 106 is a semiconductor type microwave oscillator including a microwave generation unit configured using a semiconductor element. The microwave generation unit includes, for example, a semiconductor amplification element such as a transistor and a resonance such as a tank circuit. It consists of a circuit. A Hartley oscillation circuit, a Colpitts oscillation circuit, or the like can be used for the microwave generation unit.

The microwave generally refers to an electromagnetic wave having a frequency of 300 MHz to 30 GHz (wavelength of 1 m to 1 cm). For example, a microwave MW of 2.45 GHz or 5.80 GHz can be oscillated.
The microwave output is not particularly limited, but may be set, for example, within a range of several tens of watts to several hundreds of watts, or may be a larger output.

  INDUSTRIAL APPLICABILITY The present invention can be used for an apparatus or an apparatus that generates hydrogen from an organic hydride by irradiating microwaves in the presence of a metal-supported catalyst.

DESCRIPTION OF SYMBOLS 1 Hydrogen production | generation apparatus 10 Hydrogen production | generation part 11 Reaction container 12 Organic hydride supply part 20 Microwave supply part 21 Microwave oscillator 23 Waveguide 24 Reaction container installation part

Claims (4)

A hydrogen generation system for generating hydrogen from an organic hydride by irradiating microwaves in the presence of a metal-supported catalyst,
A reaction vessel filled with the metal-supported catalyst;
An organic hydride supply unit for supplying the organic hydride to the reaction vessel;
A microwave supply unit for irradiating the reaction vessel with the microwave,
The hydrogen generation system, wherein the organic hydride supply unit supplies the organic hydride to the reaction vessel at a flow rate of 0.3 to 0.7 mL / min. ^2. The hydrogen generation system according to claim 1, wherein the flow rate of the organic hydride per unit cross-sectional area of the reaction vessel is 0.0060 to 0.0139 mL / min · mm ² .   The hydrogen generation system according to claim 1 or 2, wherein an average particle size of the metal-supported catalyst is 100 µm or less.   The hydrogen generation system according to any one of claims 1 to 3, wherein the output of the microwave is 270 to 370 W.

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