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WO2025116113A1 - Fuel reforming apparatus having double pipe structure - Google Patents

Fuel reforming apparatus having double pipe structure Download PDF

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Publication number
WO2025116113A1
WO2025116113A1 PCT/KR2023/021001 KR2023021001W WO2025116113A1 WO 2025116113 A1 WO2025116113 A1 WO 2025116113A1 KR 2023021001 W KR2023021001 W KR 2023021001W WO 2025116113 A1 WO2025116113 A1 WO 2025116113A1
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WIPO (PCT)
Prior art keywords
pipe
fuel
combustion gas
main
exhaust
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
PCT/KR2023/021001
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French (fr)
Korean (ko)
Inventor
황정태
손성효
김재동
전철희
이진원
차병욱
김석현
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Bumhan Fuel Cell Co Ltd
Original Assignee
Bumhan Fuel Cell Co Ltd
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Publication date
Application filed by Bumhan Fuel Cell Co Ltd filed Critical Bumhan Fuel Cell Co Ltd
Priority claimed from KR1020230185515A external-priority patent/KR20250079813A/en
Publication of WO2025116113A1 publication Critical patent/WO2025116113A1/en
Pending legal-status Critical Current
Anticipated expiration legal-status Critical

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/06Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds in tube reactors; the solid particles being arranged in tubes
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/38Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D14/00Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
    • F23D14/12Radiant burners
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/06Combination of fuel cells with means for production of reactants or for treatment of residues
    • H01M8/0606Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
    • H01M8/0612Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/10Fuel cells with solid electrolytes
    • H01M8/12Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte

Definitions

  • the present invention relates to a fuel reforming device, and more specifically, to a fuel reforming device having a double-pipe structure in which combustion gas paths are formed in two.
  • a reforming reaction device that produces hydrogen through a natural gas-steam reforming reaction
  • a reformer is a reactor that produces hydrogen using natural gas, the main component of which is methane, as a raw material.
  • the raw material gas and steam are converted into a reformed gas mixed with hydrogen, carbon monoxide, and carbon dioxide on a catalyst, and since a strong endothermic reaction occurs, a separate supply of reaction heat is required.
  • the reformer is connected to a steam generator required for the reaction and a preheater for preheating the reactants, and the entire process is configured.
  • the heat of the steam generator and the preheater can be supplied by recovering waste heat from the combustion exhaust gas discharged by heating the catalyst layer or the produced reformed gas. Therefore, in order to increase the efficiency of the entire process including the steam reformer, it is required to increase the heat exchange efficiency.
  • Heat exchange in conventional industrial reformers mainly uses the radiation heat transfer method.
  • the heat flux from the reaction heat generated in the combustor to the reaction tube is very large, which is advantageous for maximizing the processing capacity, but there is a risk of local heating of the reaction tube due to direct contact with the flame, etc., and the reaction stability and conversion efficiency are reduced because the reaction does not occur uniformly.
  • the reaction deviation between the reaction tubes is severe, making operation, maintenance, and management difficult, and there is a problem that expensive heat-resistant materials are required in the device.
  • the technical problem to be achieved by the present invention is to provide a fuel reforming device having a double-pipe structure that improves the heat transfer performance required for a reforming reaction by providing a double structure for the combustion gas flow path and supplies uniform heat to cause a catalytic reaction.
  • one embodiment of the present invention provides a fuel reforming device having a double-pipe structure including a housing, a burner which generates combustion gas using air and fuel gas supplied downward, a main passageway located at the center of the housing which forms a passageway through which the combustion gas generated from the burner moves upward, a reforming reaction section which surrounds the main passageway and has a reforming catalyst provided therein, a combustion gas discharge port located above the burner but formed on one side of the lower portion of the main passageway through which the combustion gas is discharged, and an exhaust passageway which forms a passageway through which the combustion gas introduced through the main passageway moves downward toward the combustion gas discharge port.
  • an upper channel may be further included, formed at the upper end of the main channel pipe and the reforming reaction section, connecting the main channel pipe and the discharge channel pipe.
  • the housing and the reforming reaction unit may be formed concentrically with the main flow pipe, and the discharge flow pipe may be formed inside the reforming reaction unit.
  • the exhaust conduit may include a plurality of exhaust conduit pipes spaced apart from each other inside the reforming reaction unit.
  • the upper and lower ends of the main flow pipe and the exhaust flow pipe are open, the upper ends of the main flow pipe and the exhaust flow pipe are connected to the upper flow pipe, and the main flow pipe and the lower ends of the exhaust flow pipe can be mutually blocked.
  • the length of the main flow pipe may be formed longer than the length of the discharge flow pipe.
  • the device further includes an air inlet formed at the lowest side of the housing and through which air is supplied, and a fuel gas inlet formed at the lowest side of the housing and through which fuel gas is supplied, wherein the air inlet and the fuel gas inlet can be located at the bottom of the burner.
  • the heat transfer performance required for a reforming reaction is improved, and uniform heat is supplied to effectively cause a catalytic reaction.
  • Figure 1 is a drawing illustrating a fuel reforming device having a double-pipe structure according to one embodiment of the present invention.
  • Figure 2 is a cross-sectional view illustrating the internal structure of a fuel reforming device according to one embodiment of the present invention.
  • FIG. 3 is a cross-sectional drawing of a fuel reforming device according to one embodiment of the present invention.
  • the fuel reforming device (10) described below relates to a catalytic reactor for hydrocarbon steam reforming, and forms a combustion gas path with a double structure. Since the fuel reforming device (10) according to the present invention causes a reforming reaction by filling a catalyst between the combustion gas paths in the form of a double tube, heat transfer for generating hydrogen from hydrocarbon raw materials and steam can be induced more effectively.
  • FIG. 1 is a drawing illustrating a fuel reforming device having a double-pipe structure according to one embodiment of the present invention
  • FIG. 2 is a longitudinal sectional view illustrating the internal structure of a fuel reforming device according to one embodiment of the present invention
  • FIG. 3 is a cross-sectional view illustrating a fuel reforming device according to one embodiment of the present invention.
  • Figure 1 (a) is a three-dimensional drawing of a fuel reformer, and (b) is a plan view of the fuel reformer.
  • the fuel reforming device (10) of the present invention may include a housing (110), a burner (120), a fuel gas inlet (130), an air inlet (140), a main flow path (150), an upper flow path (160), an exhaust flow path (170), a combustion gas outlet (180), a reforming reaction unit (190), a raw material gas inlet (200), a reforming gas outlet (210), a spark plug tube (220), a temperature sensor tube (230), and a catalyst exchange tube (240).
  • the housing (110) provides an internal space in which a burner (120), a main duct (150), an upper duct (160), an exhaust duct (170), and a reforming reaction unit (190) can be arranged, and the exhaust duct (170) can be densely arranged and formed in a cylindrical shape to miniaturize the device, but is not limited thereto.
  • a fuel gas inlet (130), an air inlet (140), a combustion gas outlet (180), a raw material gas inlet (200), and a reforming gas outlet (210) can be formed in a form that protrudes outward.
  • the burner (120) can generate reaction heat and combustion gas using air and fuel gas supplied from below.
  • the burner (120) supplies reaction heat required for the reforming reaction, and can perform a process of receiving air and fuel from the outside and combusting them to generate reaction heat in the inner center of the housing (110).
  • the combustion gas generated from the burner (120) can spray heat in the form of a flame by combustion.
  • the burner (120) according to the present invention may be provided as a metal fiber burner.
  • the metal fiber burner has the advantage of enabling better heat transfer of combustion gas to the main flow pipe (150) and combustion gas discharge port (180), thereby enabling a uniform temperature distribution and more efficient catalytic reaction.
  • the air inlet (140) is a place where air is injected from the outside and can be formed at the lowest end of the side of the housing (110).
  • the fuel gas inlet (130) and the air inlet (140) are located at the bottom of the burner (120) so that the burner (120) can be supplied with fuel gas and air necessary for combustion.
  • the fuel gas inlet (!30) and the air inlet (140) can be formed in a direction perpendicular to each other with respect to the housing (110).
  • the main flow path (150) can form a main flow path through which combustion gas generated from the burner (120) can move upward.
  • the main flow path (150) can be located at the inner center of the housing (110). The combustion gas generated from the burner (120) can move upward through the main flow path formed by the main flow path (150).
  • the upper passage (160) may be formed at the upper end of the main passage pipe (150) and may serve to connect the main passage pipe (150) and the exhaust passage pipe (170).
  • the upper passage (160) may be provided as a space formed between the upper end of the main passage pipe (150) and the upper cap (111) of the housing (110).
  • the exhaust pipe (170) can form a path through which combustion gas introduced through the main pipe (150) can pass through the upper path (160) and flow downward toward the combustion gas discharge port (180) located at the bottom.
  • the exhaust pipe (170) may be formed inside the reforming reaction unit (190).
  • the lower end of the exhaust pipe (170) is connected to a combustion gas discharge port (180), and combustion gas moving downward through the exhaust pipe (170) may be discharged to the combustion gas discharge port (180).
  • the combustion gas discharge port (180) is positioned higher than the burner (120), but is formed on one side of the lower portion of the main pipe (150), so that the combustion gas passing through the exhaust pipe (170) can be discharged to the outside.
  • combustion gas exhaust port (180) may be formed at a higher position than the lower end of the main pipe (150) and lower than the lower end of the exhaust pipe (170).
  • the combustion gas moves upward through the main flow path (150) located at the top of the burner (120), moves vertically along the flow path shape of the upper flow path (160), and then moves vertically again to move to the exhaust flow path (170) located at the bottom.
  • the combustion gas that has moved vertically downward moves downward along the exhaust flow path (170), and then moves vertically to be discharged through the combustion gas discharge port (180) formed on the side of the housing (110).
  • the reforming reaction unit (190) is formed in a shape that surrounds the main flow pipe (150), and a reforming catalyst (250) can be filled inside.
  • the reforming reaction unit (190) can be arranged in a concentric circle centered on the main flow pipe (150) through which combustion gas generated from the burner (120) passes in order to reform the raw material gas.
  • the catalyst (250) for reforming is not limited in type, but may include at least one selected from the group consisting of one or more metals selected from gold, silver, iron, cobalt, nickel, copper, manganese, aluminum, zinc, titanium, hafnium, platinum, rhodium, ruthenium, osmium, iridium, palladium, zirconium, and lanthanide metals, or oxides thereof, and complexes thereof.
  • a filling film (191) may be formed at the upper and lower portions of the inside of the reforming reaction unit (190), and the filling film (191) may be provided to confine the reforming catalyst (250) in a limited space inside the reforming reaction unit (190).
  • the filling film (191) be installed entirely at the upper and lower portions of the inside of the reforming reaction unit (190) except for the area where the exhaust conduit (170) is formed.
  • a reforming reaction can occur in which the raw material gas of the carbon compound and water vapor, which are the reaction raw materials, are converted into a reforming gas containing hydrogen.
  • the reforming reaction unit (190) is not limited in its shape, but can be implemented in a cylindrical shape corresponding to the shape of the housing (110).
  • the housing (110) and the reforming reaction unit (190) can be arranged concentrically around the main flow pipe (150).
  • the exhaust path pipe (170) may be formed inside the reforming reaction unit (190). More specifically, a plurality of exhaust path pipes (170) may be provided, and a plurality of exhaust path pipes (170) may be spaced apart from each other inside the reforming reaction unit (190).
  • a plurality of exhaust pipes (170) may be spaced apart and arranged along the outer circumference of the reforming reaction unit (190). That is, a plurality of exhaust pipes (170) may be formed at positions with a certain radius centered on the main pipe (150). At this time, the number and arrangement structure of the exhaust pipes (170) are not particularly limited, but may be adjusted for compactness and efficient heat exchange of the fuel reforming device (10).
  • the outer surface at the center of the reforming reaction unit (190) transfers heat to the raw material gas inside as it comes into contact with the main passage (150) through which the combustion gas generated from the burner (120) passes.
  • the reforming reaction unit (190) can transfer heat by the combustion gas passing through the reforming reaction unit (190) to the raw material gas by providing a plurality of spaced-apart exhaust passages (170) inside. That is, the reforming reaction unit (190) can have heat transfer performed in two ways by the main passage (150) and the exhaust passage (170). The heat transferred by the main passage (150) and the exhaust passage (170) in this way can be used for the reforming reaction, which is an endothermic reaction that is performed in the reforming reaction unit (190).
  • the fuel reforming device (10) according to one embodiment of the present invention is exemplified as having eight exhaust pipes (170), but is not limited thereto, and the number may be changed depending on the size of the fuel reforming device being implemented or the size of the exhaust pipes.
  • the raw material gas supplied from the raw material gas inlet (200) arranged at the bottom may undergo a reforming reaction while passing through the reforming catalyst (250) filled inside.
  • the reformed gas reformed while passing through the reforming catalyst (250) may be discharged through the reforming gas discharge port (210) formed on one side of the upper portion of the reforming reaction unit (190).
  • the raw material gas inlet (200) and the reformed gas outlet (210) can be formed in a direction perpendicular to each other with respect to the housing (110).
  • the main flow path (150) formed at the center of the reforming reaction unit (190) and the exhaust flow path (170) spaced apart from each other in the circumferential direction inside the reforming reaction unit (190) can supply uniform heat to the reforming reaction unit (190) to prevent local heating from occurring.
  • the device compactness rate can be dramatically increased. That is, while miniaturizing the fuel reforming device (10), local heating of the reforming reaction unit (190) can be suppressed, thereby realizing a uniform reaction and high thermal efficiency.
  • the spark plug tube (220) is a tube into which a spark plug can be installed.
  • the temperature sensor tube (230) is a tube in which a temperature sensor for measuring the temperature of the catalyst is installed.
  • three temperature sensor tubes (230) can be formed to protrude side by side along the length direction on the outer surface of the housing (110).
  • the plurality of temperature sensor tubes (230) can each measure the temperature of each region of the catalyst.
  • the catalyst exchange tube (240) can serve as a passage for replacing the catalyst filled inside the reforming reaction unit (190).

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  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
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  • Sustainable Development (AREA)
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  • Life Sciences & Earth Sciences (AREA)
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  • Hydrogen, Water And Hydrids (AREA)

Abstract

An embodiment of the present invention provides a fuel reforming apparatus having a double pipe structure, the fuel reforming apparatus including: a housing; a burner which generates combustion gas by using air and fuel gas supplied to the lower part thereof; a main channel pipe which forms a fluid channel in which the combustion gas generated from the burner moves upward, and is positioned at the center of the housing; a reforming reaction part which surrounds the main channel pipe and in which a reforming catalyst is provided; a combustion gas discharge port, which is positioned above the burner and formed at one side of a lower part of the main channel pipe and to which the combustion gas is discharged; and a discharge channel pipe forming a fluid channel through which the combustion gas introduced through the main channel pipe moves downward toward the combustion gas discharge port.

Description

이중관 구조를 가지는 연료 개질장치Fuel reformer with double-pipe structure

본 발명은 연료 개질장치에 관한 것으로, 더욱 상세하게는 연소가스의 유로가 이중으로 형성되는 이중관 구조를 가지는 연료 개질장치에 관한 것이다.The present invention relates to a fuel reforming device, and more specifically, to a fuel reforming device having a double-pipe structure in which combustion gas paths are formed in two.

본 발명의 적용이 가능한 하나의 예로서, 천연가스-수증기 개질반응을 통해 수소를 생산하는 개질반응 장치(이하, 개질기)를 들 수 있다. 개질기는 메탄이 주성분인 천연가스를 원료로 수소를 제조하는 반응기이다. 원료가스와 수증기는 촉매상에서 수소, 일산화탄소, 이산화탄소가 혼합된 개질가스(reformed gas)로 전환되며, 강한 흡열 반응을 일으키므로 별도의 반응열의 공급이 필요하다.As one example where the present invention can be applied, a reforming reaction device (hereinafter, “reformer”) that produces hydrogen through a natural gas-steam reforming reaction can be cited. A reformer is a reactor that produces hydrogen using natural gas, the main component of which is methane, as a raw material. The raw material gas and steam are converted into a reformed gas mixed with hydrogen, carbon monoxide, and carbon dioxide on a catalyst, and since a strong endothermic reaction occurs, a separate supply of reaction heat is required.

개질기는 반응에 필요한 수증기 발생기와 반응물을 예열하는 예열기가 연계되어 전체 공정이 구성된다. 이때, 수증기 발생기와 예열기의 열은 촉매층을 가열하고 배출되는 연소 배가스 혹은 생산된 개질가스에서 나오는 폐열을 회수하여 공급될 수 있다. 이에, 수증기 개질기를 포함하여 전체 공정의 효율을 높이기 위하여 열교환 효율을 높이는 것이 요구된다.The reformer is connected to a steam generator required for the reaction and a preheater for preheating the reactants, and the entire process is configured. At this time, the heat of the steam generator and the preheater can be supplied by recovering waste heat from the combustion exhaust gas discharged by heating the catalyst layer or the produced reformed gas. Therefore, in order to increase the efficiency of the entire process including the steam reformer, it is required to increase the heat exchange efficiency.

통상의 산업용 개질기에서의 열교환은 주로 복사 전열(radiation heat transfer) 방식이 적용된다. 이때, 연소기에서 발생된 반응열에 대한 반응 튜브로의 열 플럭스(heat flux)는 매우 크기 때문에 처리용량 극대화에는 유리하나 화염과의 직접적인 접촉 등에 의해 반응 튜브의 국부 가열 위험이 있으며, 그로 인한 균일한 반응이 일어나지 않아 반응 안정성과 전환 효율이 저하된다. 또한, 반응 튜브 간 반응 편차가 심하여 운전, 유지 및 관리에 어려움이 있으며, 장치 내 고가의 내열 재료가 요구되는 문제점을 가진다.Heat exchange in conventional industrial reformers mainly uses the radiation heat transfer method. At this time, the heat flux from the reaction heat generated in the combustor to the reaction tube is very large, which is advantageous for maximizing the processing capacity, but there is a risk of local heating of the reaction tube due to direct contact with the flame, etc., and the reaction stability and conversion efficiency are reduced because the reaction does not occur uniformly. In addition, the reaction deviation between the reaction tubes is severe, making operation, maintenance, and management difficult, and there is a problem that expensive heat-resistant materials are required in the device.

이는 장치 소형화의 요구가 증대되고 있는 면에서 더욱 큰 걸림돌이 된다. 따라서 장치 내 반응 튜브가 배열되는 중심선의 직경을 줄이는 것과 같은 장치 부피를 최소화할 수 있으면서도 개질기 내 반응열에 대한 열 교환 효율을 높일 수 있는 기술에 대한 연구개발이 필요한 실정이다.This becomes an even bigger obstacle as the demand for device miniaturization increases. Therefore, research and development is needed on technology that can minimize the device volume, such as by reducing the diameter of the center line where the reaction tubes are arranged within the device, while increasing the heat exchange efficiency for the reaction heat within the reformer.

본 발명이 이루고자 하는 기술적 과제는 연소가스의 유로를 이중 구조로 마련함에 따라 개질반응에 필요한 열전달 성능을 향상시키고, 균일한 열을 공급하여 촉매 반응을 일으키는 이중관 구조를 가지는 연료 개질장치를 제공하는 것이다.The technical problem to be achieved by the present invention is to provide a fuel reforming device having a double-pipe structure that improves the heat transfer performance required for a reforming reaction by providing a double structure for the combustion gas flow path and supplies uniform heat to cause a catalytic reaction.

본 발명이 이루고자 하는 기술적 과제는 이상에서 언급한 기술적 과제로 제한되지 않으며, 언급되지 않은 또 다른 기술적 과제들은 아래의 기재로부터 본 발명이 속하는 기술 분야에서 통상의 지식을 가진 자에게 명확하게 이해될 수 있을 것이다.The technical problems to be achieved by the present invention are not limited to the technical problems mentioned above, and other technical problems not mentioned can be clearly understood by a person having ordinary skill in the technical field to which the present invention belongs from the description below.

상기 기술적 과제를 달성하기 위하여, 본 발명의 일실시예는 하우징과, 하부로 공급되는 공기 및 연료가스를 이용하여 연소가스를 생성하는 버너와, 상기 버너로부터 생성된 연소가스가 상향 이동하는 유로를 형성하며, 상기 하우징의 중심에 위치하는 메인 유로관과, 상기 메인 유로관을 둘러싸며, 내부에 개질용 촉매가 마련되는 개질 반응부와, 상기 버너의 상부에 위치하되 상기 메인 유로관의 하부의 일측에 형성되어, 상기 연소가스가 배출되는 연소가스 배출구와, 상기 메인 유로관을 통해 유입된 연소가스가 상기 연소가스 배출구를 향해 하향 이동하는 유로를 형성하는 배출 유로관을 포함하는 이중관 구조를 가지는 연료 개질장치를 제공한다.In order to achieve the above technical problem, one embodiment of the present invention provides a fuel reforming device having a double-pipe structure including a housing, a burner which generates combustion gas using air and fuel gas supplied downward, a main passageway located at the center of the housing which forms a passageway through which the combustion gas generated from the burner moves upward, a reforming reaction section which surrounds the main passageway and has a reforming catalyst provided therein, a combustion gas discharge port located above the burner but formed on one side of the lower portion of the main passageway through which the combustion gas is discharged, and an exhaust passageway which forms a passageway through which the combustion gas introduced through the main passageway moves downward toward the combustion gas discharge port.

본 발명의 실시예에 있어서, 상기 메인 유로관 및 상기 개질 반응부의 상단에 형성되어, 상기 메인 유로관 및 상기 배출 유로관의 사이를 연결하는 상단 유로를 더 포함할 수 있다.In an embodiment of the present invention, an upper channel may be further included, formed at the upper end of the main channel pipe and the reforming reaction section, connecting the main channel pipe and the discharge channel pipe.

본 발명의 실시예에 있어서, 상기 하우징 및 상기 개질 반응부는 상기 메인 유로관을 동심원으로 하며, 상기 배출 유로관은 상기 개질 반응부의 내부에 형성될 수 있다.In an embodiment of the present invention, the housing and the reforming reaction unit may be formed concentrically with the main flow pipe, and the discharge flow pipe may be formed inside the reforming reaction unit.

본 발명의 실시예에 있어서, 상기 배출 유로관은, 상기 개질 반응부의 내부에 이격 배치되는 복수개의 배출 유로관들을 포함할 수 있다.In an embodiment of the present invention, the exhaust conduit may include a plurality of exhaust conduit pipes spaced apart from each other inside the reforming reaction unit.

본 발명의 실시예에 있어서, 상기 메인 유로관 및 상기 배출 유로관의 상단과 하단은 개방되어 있고, 상기 메인 유로관 및 상기 배출 유로관의 상단은 상기 상단 유로로 연결되며, 상기 메인 유로관과, 상기 배출 유로관의 하단은 상호간 차단될 수 있다.In an embodiment of the present invention, the upper and lower ends of the main flow pipe and the exhaust flow pipe are open, the upper ends of the main flow pipe and the exhaust flow pipe are connected to the upper flow pipe, and the main flow pipe and the lower ends of the exhaust flow pipe can be mutually blocked.

본 발명의 실시예에 있어서, 상기 메인 유로관의 길이가 상기 배출 유로관의 길이보다 길게 형성될 수 있다.In an embodiment of the present invention, the length of the main flow pipe may be formed longer than the length of the discharge flow pipe.

본 발명의 실시예에 있어서, 상기 하우징의 최하단 측부에 형성되며, 공기가 공급되는 공기 주입구와, 상기 하우징의 최하단 측부에 형성되어, 연료가스가 공급되는 연료가스 주입구를 더 포함하되, 상기 공기 주입구 및 상기 연료가스 주입구는 상기 버너의 하부에 위치할 수 있다.In an embodiment of the present invention, the device further includes an air inlet formed at the lowest side of the housing and through which air is supplied, and a fuel gas inlet formed at the lowest side of the housing and through which fuel gas is supplied, wherein the air inlet and the fuel gas inlet can be located at the bottom of the burner.

본 발명의 실시예에 따르면, 연소가스의 유로를 이중 구조로 마련함에 따라 개질반응에 필요한 열전달 성능을 향상시키고, 균일한 열을 공급하여 촉매 반응을 효과적으로 일으킬 수 있다.According to an embodiment of the present invention, by providing a combustion gas path with a double structure, the heat transfer performance required for a reforming reaction is improved, and uniform heat is supplied to effectively cause a catalytic reaction.

본 발명의 효과는 상기한 효과로 한정되는 것은 아니며, 본 발명의 설명 또는 청구범위에 기재된 발명의 구성으로부터 추론 가능한 모든 효과를 포함하는 것으로 이해되어야 한다.The effects of the present invention are not limited to the effects described above, and should be understood to include all effects that can be inferred from the composition of the invention described in the description or claims of the present invention.

도1은 본 발명의 일 실시예에 따른 이중관 구조를 가지는 연료 개질장치를 도시한 도면이다.Figure 1 is a drawing illustrating a fuel reforming device having a double-pipe structure according to one embodiment of the present invention.

도2는 본 발명의 일 실시예에 따른 연료 개질장치의 내부 구조를 설명하기 위해 도시한 종단면도이다.Figure 2 is a cross-sectional view illustrating the internal structure of a fuel reforming device according to one embodiment of the present invention.

도3은 본 발명의 일 실시예에 따른 연료 개질장치의 횡단면을 도시한 도면이다.FIG. 3 is a cross-sectional drawing of a fuel reforming device according to one embodiment of the present invention.

이하에서는 첨부한 도면을 참조하여 본 발명을 설명하기로 한다. 그러나 본 발명은 여러 가지 상이한 형태로 구현될 수 있으며, 따라서 여기에서 설명하는 실시예로 한정되는 것은 아니다. 그리고 도면에서 본 발명을 명확하게 설명하기 위해서 설명과 관계없는 부분은 생략하였으며, 명세서 전체를 통하여 유사한 부분에 대해서는 유사한 도면 부호를 붙였다.Hereinafter, the present invention will be described with reference to the attached drawings. However, the present invention can be implemented in various different forms, and therefore is not limited to the embodiments described herein. In addition, in order to clearly describe the present invention in the drawings, parts that are not related to the description are omitted, and similar parts are assigned similar drawing reference numerals throughout the specification.

명세서 전체에서, 어떤 부분이 다른 부분과 "연결(접속, 접촉, 결합)"되어 있다고 할 때, 이는 "직접적으로 연결"되어 있는 경우뿐 아니라, 그 중간에 다른 부재를 사이에 두고 "간접적으로 연결"되어 있는 경우도 포함한다. 또한 어떤 부분이 어떤 구성요소를 "포함"한다고 할 때, 이는 특별히 반대되는 기재가 없는 한 다른 구성요소를 제외하는 것이 아니라 다른 구성요소를 더 구비할 수 있다는 것을 의미한다.Throughout the specification, when a part is said to be "connected (connected, contacted, joined)" to another part, this includes not only the case where it is "directly connected" but also the case where it is "indirectly connected" with another member in between. Also, when a part is said to "include" a certain component, this does not mean that other components are excluded, unless otherwise specifically stated, but that other components can be included.

본 명세서에서 사용한 용어는 단지 특정한 실시예를 설명하기 위해 사용된 것으로, 본 발명을 한정하려는 의도가 아니다. 단수의 표현은 문맥상 명백하게 다르게 뜻하지 않는 한, 복수의 표현을 포함한다. 본 명세서에서, "포함하다" 또는 "가지다" 등의 용어는 명세서상에 기재된 특징, 숫자, 단계, 동작, 구성요소, 부품 또는 이들을 조합한 것이 존재함을 지정하려는 것이지, 하나 또는 그 이상의 다른 특징들이나 숫자, 단계, 동작, 구성요소, 부품 또는 이들을 조합한 것들의 존재 또는 부가 가능성을 미리 배제하지 않는 것으로 이해되어야 한다.The terminology used herein is for the purpose of describing particular embodiments only and is not intended to be limiting of the present invention. The singular expression includes the plural expression unless the context clearly indicates otherwise. As used herein, the terms "comprises" or "has" and the like are intended to specify the presence of a feature, number, step, operation, component, part or combination thereof described in the specification, but should be understood to not exclude in advance the possibility of the presence or addition of one or more other features, numbers, steps, operations, components, parts or combinations thereof.

이하 첨부된 도면을 참고하여 본 발명의 실시예를 상세히 설명하기로 한다.Hereinafter, an embodiment of the present invention will be described in detail with reference to the attached drawings.

이하에서 설명하는 연료 개질장치(10)는 탄화수소 수증기 개질용 촉매반응기에 관한 것으로서, 연소가스 유로를 이중 구조로 형성한다. 본 발명에 따른 연료 개질장치(10)는 이중관 형태의 연소가스 유로 사이에 촉매가 충진되어 개질반응이 일어나므로, 탄화수소계 원료 및 수증기로부터 수소를 생성시키는 열전달을 더욱 효과적으로 유도할 수 있다.The fuel reforming device (10) described below relates to a catalytic reactor for hydrocarbon steam reforming, and forms a combustion gas path with a double structure. Since the fuel reforming device (10) according to the present invention causes a reforming reaction by filling a catalyst between the combustion gas paths in the form of a double tube, heat transfer for generating hydrogen from hydrocarbon raw materials and steam can be induced more effectively.

도1은 본 발명의 일 실시예에 따른 이중관 구조를 가지는 연료 개질장치를 도시한 도면이고, 도2는 본 발명의 일 실시예에 따른 연료 개질장치의 내부 구조를 설명하기 위해 도시한 종단면도이며, 도3은 본 발명의 일 실시예에 따른 연료 개질장치의 횡단면을 도시한 도면이다.FIG. 1 is a drawing illustrating a fuel reforming device having a double-pipe structure according to one embodiment of the present invention, FIG. 2 is a longitudinal sectional view illustrating the internal structure of a fuel reforming device according to one embodiment of the present invention, and FIG. 3 is a cross-sectional view illustrating a fuel reforming device according to one embodiment of the present invention.

도1의 (a)는 연료 개질장치의 입체도이고, (b)는 연료 개질장치의 평면도이다.Figure 1 (a) is a three-dimensional drawing of a fuel reformer, and (b) is a plan view of the fuel reformer.

도1 내지 도3을 참조하면, 본 발명의 연료 개질장치(10)는 하우징(110), 버너(120), 연료가스 주입구(130), 공기 주입구(140), 메인 유로관(150), 상단 유로(160), 배출 유로관(170), 연소가스 배출구(180), 개질 반응부(190), 원료가스 주입구(200), 개질가스 배출구(210), 점화플러그 관(220), 온도센서 관(230), 그리고 촉매 교환 관(240)을 포함할 수 있다.Referring to FIGS. 1 to 3, the fuel reforming device (10) of the present invention may include a housing (110), a burner (120), a fuel gas inlet (130), an air inlet (140), a main flow path (150), an upper flow path (160), an exhaust flow path (170), a combustion gas outlet (180), a reforming reaction unit (190), a raw material gas inlet (200), a reforming gas outlet (210), a spark plug tube (220), a temperature sensor tube (230), and a catalyst exchange tube (240).

하우징(110)은 버너(120), 메인 유로관(150), 상단 유로(160), 배출 유로관(170), 및 개질 반응부(190)가 배치 가능한 내부 공간을 마련하고, 배출 유로관(170)을 조밀하게 배치하고 장치의 소형화를 위하여 그 형상이 원통형으로 형성될 수 있으나 이에 제한되는 것은 아니다. 하우징(110)의 외측에는 연료가스 주입구(130), 공기 주입구(140), 연소가스 배출구(180), 원료가스 주입구(200), 및 개질가스 배출구(210)가 외부로 돌출된 형태로 형성될 수 있다.The housing (110) provides an internal space in which a burner (120), a main duct (150), an upper duct (160), an exhaust duct (170), and a reforming reaction unit (190) can be arranged, and the exhaust duct (170) can be densely arranged and formed in a cylindrical shape to miniaturize the device, but is not limited thereto. On the outside of the housing (110), a fuel gas inlet (130), an air inlet (140), a combustion gas outlet (180), a raw material gas inlet (200), and a reforming gas outlet (210) can be formed in a form that protrudes outward.

버너(120)는 하부로 공급되는 공기 및 연료가스를 이용하여 반응열 및 연소가스를 생성할 수 있다. 버너(120)는 개질 반응에 필요한 반응열을 공급하는 것으로, 외부로부터 공기와 연료를 공급받아 하우징(110)의 내부 중심에 반응열을 생성하기 위하여 연소시키는 공정을 수행할 수 있다. 예컨대, 버너(120)에서 발생된 연소가스는 연소에 의해 화염 형태로 열을 분사할 수 있다.The burner (120) can generate reaction heat and combustion gas using air and fuel gas supplied from below. The burner (120) supplies reaction heat required for the reforming reaction, and can perform a process of receiving air and fuel from the outside and combusting them to generate reaction heat in the inner center of the housing (110). For example, the combustion gas generated from the burner (120) can spray heat in the form of a flame by combustion.

본 발명에 따른 버너(120)는 메탈화이버 버너(metal fiber burner)로 마련될 수 있다. 메탈화이버 버너는 연소가스가 메인 유로관(150) 및 연소가스 배출구(180)에 열전달이 보다 잘 이루어질 수 있도록 함으로써, 균일한 온도가 분포되어 촉매 반응을 더 효율적으로 일으킬 수 있는 이점이 있다.The burner (120) according to the present invention may be provided as a metal fiber burner. The metal fiber burner has the advantage of enabling better heat transfer of combustion gas to the main flow pipe (150) and combustion gas discharge port (180), thereby enabling a uniform temperature distribution and more efficient catalytic reaction.

연료가스 주입구(130)는 외부로부터 연료가스가 주입되는 곳으로, 하우징(110)의 측부의 최하단에 형성될 수 있다.The fuel gas inlet (130) is a place where fuel gas is injected from the outside and can be formed at the lowest end of the side of the housing (110).

공기 주입구(140)는 외부로부터 공기가 주입되는 곳으로, 하우징(110)의 측부의 최하단에 형성될 수 있다.The air inlet (140) is a place where air is injected from the outside and can be formed at the lowest end of the side of the housing (110).

연료가스 주입구(130) 및 공기 주입구(140)는 버너(120)의 하부에 위치하여, 버너(120)가 연소하는데 필요한 연료가스 및 공기를 공급받을 수 있다.The fuel gas inlet (130) and the air inlet (140) are located at the bottom of the burner (120) so that the burner (120) can be supplied with fuel gas and air necessary for combustion.

연료가스 주입구(!30)와 공기 주입구(140)는 하우징(110)에 대하여 서로 수직하는 방향으로 형성될 수 있다.The fuel gas inlet (!30) and the air inlet (140) can be formed in a direction perpendicular to each other with respect to the housing (110).

메인 유로관(150)은 버너(120)로부터 생성된 연소가스가 상향 이동할 수 있는 메인 유로를 형성할 수 있다. 메인 유로관(150)은 하우징(110)의 내부 중심에 위치할 수 있다. 버너(120)에서 발생한 연소가스는 메인 유로관(150)에 의해 형성되는 메인 유로를 지나 상부로 이동할 수 있다.The main flow path (150) can form a main flow path through which combustion gas generated from the burner (120) can move upward. The main flow path (150) can be located at the inner center of the housing (110). The combustion gas generated from the burner (120) can move upward through the main flow path formed by the main flow path (150).

메인 유로관(150) 및 배출 유로관(170)의 상단과 하단은 모두 개방된 형태로 형성될 수 있다. 그리고, 메인 유로관(150) 및 배출 유로관(170)의 상단은 상단 유로(160)로 연결될 수 있다.The upper and lower ends of the main flow pipe (150) and the discharge flow pipe (170) can both be formed in an open form. In addition, the upper ends of the main flow pipe (150) and the discharge flow pipe (170) can be connected to the upper flow pipe (160).

상단 유로(160)는 메인 유로관(150)의 상단에 형성되어, 메인 유로관(150)과 배출 유로관(170)의 사이를 연결하는 역할을 할 수 있다. 상단 유로(160)는 메인 유로관(150)의 상단과 하우징(110)의 상부캡(111)의 사이에 형성되는 이격 공간으로 마련될 수 있다.The upper passage (160) may be formed at the upper end of the main passage pipe (150) and may serve to connect the main passage pipe (150) and the exhaust passage pipe (170). The upper passage (160) may be provided as a space formed between the upper end of the main passage pipe (150) and the upper cap (111) of the housing (110).

배출 유로관(170)은 메인 유로관(150)을 통해 유입된 연소가스가 상단 유로(160)를 지나 하부에 위치한 연소가스 배출구(180)를 향해 하향할 수 있는 유로를 형성할 수 있다.The exhaust pipe (170) can form a path through which combustion gas introduced through the main pipe (150) can pass through the upper path (160) and flow downward toward the combustion gas discharge port (180) located at the bottom.

배출 유로관(170)은 개질 반응부(190)의 내부에 형성될 수 있다. 배출 유로관(170)의 하단은 연소가스 배출구(180)와 연결되고, 배출 유로관(170)을 통해 하향 이동한 연소가스는 연소가스 배출구(180)로 배출될 수 있다.The exhaust pipe (170) may be formed inside the reforming reaction unit (190). The lower end of the exhaust pipe (170) is connected to a combustion gas discharge port (180), and combustion gas moving downward through the exhaust pipe (170) may be discharged to the combustion gas discharge port (180).

도2를 참조하면, 메인 유로관(150)의 길이가 배출 유로관(170)의 길이보다 길게 형성됨에 따라, 메인 유로관(150)의 외벽에 의해 배출 유로관(170)을 통과한 연소가스는 메인 유로관(150)으로 다시 유입될 수 없다. 즉, 메인 유로관(150)과 배출 유로관(170)의 하단은 상호간 차단될 수 있다.Referring to FIG. 2, since the length of the main flow pipe (150) is formed longer than the length of the exhaust flow pipe (170), combustion gas passing through the exhaust flow pipe (170) cannot flow back into the main flow pipe (150) due to the outer wall of the main flow pipe (150). In other words, the lower ends of the main flow pipe (150) and the exhaust flow pipe (170) can be mutually blocked.

연소가스 배출구(180)는 버너(120)보다 높은 위치에 위치하되, 메인 유로관(150)의 하부의 일측에 형성되어, 배출 유로관(170)을 통과한 연소가스가 외부로 배출될 수 있도록 배출구를 형성할 수 있다.The combustion gas discharge port (180) is positioned higher than the burner (120), but is formed on one side of the lower portion of the main pipe (150), so that the combustion gas passing through the exhaust pipe (170) can be discharged to the outside.

보다 구체적으로 설명하면, 연소가스 배출구(180)는 메인 유로관(150)의 하단보다는 높은 위치에 형성되고, 배출 유로관(170)의 하단보다는 낮은 위치에 형성될 수 있다.To be more specific, the combustion gas exhaust port (180) may be formed at a higher position than the lower end of the main pipe (150) and lower than the lower end of the exhaust pipe (170).

버너(120)로부터 생성된 연소가스의 이동 경로에 대하여 설명하면, 연소가스는 버너(120)의 상부에 위치한 메인 유로관(150)을 통해 상향 이동하고, 상단 유로(160)의 유로 형태를 따라 수직 이동한 후, 하부에 위치한 배출 유로관(170)으로 이동하기 위해 다시 수직 이동할 수 있다. 하부로 수직 이동한 연소가스는 배출 유로관(170)을 따라 하향 이동한 후, 수직 이동하여 하우징(110)의 측부에 형성되는 연소가스 배출구(180)로 배출될 수 있다.Regarding the movement path of the combustion gas generated from the burner (120), the combustion gas moves upward through the main flow path (150) located at the top of the burner (120), moves vertically along the flow path shape of the upper flow path (160), and then moves vertically again to move to the exhaust flow path (170) located at the bottom. The combustion gas that has moved vertically downward moves downward along the exhaust flow path (170), and then moves vertically to be discharged through the combustion gas discharge port (180) formed on the side of the housing (110).

개질 반응부(190)는 메인 유로관(150)을 둘러싸는 형태로 형성되며, 내부에 개질용 촉매(250)가 충진될 수 있다. 개질 반응부(190)는 원료가스를 개질하기 위하여, 버너(120)로부터 발생된 연소가스가 지나는 메인 유로관(150)을 중심으로 동심원에 배치될 수 있다.The reforming reaction unit (190) is formed in a shape that surrounds the main flow pipe (150), and a reforming catalyst (250) can be filled inside. The reforming reaction unit (190) can be arranged in a concentric circle centered on the main flow pipe (150) through which combustion gas generated from the burner (120) passes in order to reform the raw material gas.

개질용 촉매(250)로는 그 종류에 제한되는 것은 아니지만, 금, 은, 철, 코발트, 니켈, 구리, 망간, 알루미늄, 아연, 티타늄, 하프늄, 백금, 로듐, 루테늄, 오스뮴, 이리듐, 팔라듐, 지르코늄 및 란탄족 금속에서 선택되는 하나 이상의 금속 또는 이들의 산화물 및 이들의 복합체로 이루어진 군으로부터 선택되는 어느 하나 이상을 포함할 수 있다.The catalyst (250) for reforming is not limited in type, but may include at least one selected from the group consisting of one or more metals selected from gold, silver, iron, cobalt, nickel, copper, manganese, aluminum, zinc, titanium, hafnium, platinum, rhodium, ruthenium, osmium, iridium, palladium, zirconium, and lanthanide metals, or oxides thereof, and complexes thereof.

도2를 참조하면, 개질 반응부(190)의 내부에는 상부 및 하부에 충진막(191)이 형성될 수 있고, 충진막(191)은 개질 반응부(190) 내부의 제한된 공간에 개질용 촉매(250)를 구속하기 위해 마련된 것일 수 있다. 예컨대, 충진막(191)은 배출 유로관(170)이 형성된 영역을 제외한 개질 반응부(190)의 내부의 상부 및 하부에 전체적으로 설치되는 것이 바람직하다.Referring to FIG. 2, a filling film (191) may be formed at the upper and lower portions of the inside of the reforming reaction unit (190), and the filling film (191) may be provided to confine the reforming catalyst (250) in a limited space inside the reforming reaction unit (190). For example, it is preferable that the filling film (191) be installed entirely at the upper and lower portions of the inside of the reforming reaction unit (190) except for the area where the exhaust conduit (170) is formed.

개질 반응부(190)에서는 반응 원료인 탄소화합물의 원료가스와 수증기가 수소를 포함하는 개질 가스로 전환되는 개질 반응이 일어날 수 있다. 개질 반응부(190)는 그 형태가 제한되는 것은 아니지만, 하우징(110)의 형상과 대응되는 원통형으로 구현될 수 있다.In the reforming reaction unit (190), a reforming reaction can occur in which the raw material gas of the carbon compound and water vapor, which are the reaction raw materials, are converted into a reforming gas containing hydrogen. The reforming reaction unit (190) is not limited in its shape, but can be implemented in a cylindrical shape corresponding to the shape of the housing (110).

하우징(110) 및 개질 반응부(190)는 메인 유로관(150)을 중심으로 동심원으로 배열될 수 있다.The housing (110) and the reforming reaction unit (190) can be arranged concentrically around the main flow pipe (150).

배출 유로관(170)은 개질 반응부(190)의 내부에 형성될 수 있다. 보다 구체적으로, 배출 유로관(170)은 복수개로 마련될 수 있고, 복수개의 배출 유로관(170)들은 개질 반응부(190)의 내부에 이격 배치될 수 있다.The exhaust path pipe (170) may be formed inside the reforming reaction unit (190). More specifically, a plurality of exhaust path pipes (170) may be provided, and a plurality of exhaust path pipes (170) may be spaced apart from each other inside the reforming reaction unit (190).

도3을 참조하면, 복수개의 배출 유로관(170)들은 개질 반응부(190)의 외주 방향을 따라 이격되어 배치될 수 있다. 즉, 복수개의 배출 유로관(170)들은 메인 유로관(150)을 중심으로 하여 일정 반경의 위치에 다수개로 형성될 수 있다. 이때, 배출 유로관(170)의 개수 및 배치 구조는 크게 제한이 없으나, 연료 개질장치(10)의 컴팩트화 및 효율적인 열 교환을 위해 조절될 수 있다.Referring to FIG. 3, a plurality of exhaust pipes (170) may be spaced apart and arranged along the outer circumference of the reforming reaction unit (190). That is, a plurality of exhaust pipes (170) may be formed at positions with a certain radius centered on the main pipe (150). At this time, the number and arrangement structure of the exhaust pipes (170) are not particularly limited, but may be adjusted for compactness and efficient heat exchange of the fuel reforming device (10).

개질 반응부(190)의 중심부에 있는 외표면은 버너(120)로부터 발생된 연소가스가 지나는 메인 유로관(150)과 접촉함에 따라 내부에 있는 원료가스로 열이 전달된다. 그리고, 개질 반응부(190)는 이격 배치되는 복수개의 배출 유로관(170)들을 내부에 마련함에 따라 개질 반응부(190)를 지나는 연소가스에 의한 열을 원료가스로 전달할 수 있다. 즉, 개질 반응부(190)는 메인 유로관(150) 및 배출 유로관(170)에 의해 이중으로 열전달이 이루어질 수 있다. 이렇게 메인 유로관(150) 및 배출 유로관(170)에 의해 전달된 열은 개질 반응부(190)에서 진행되는 흡열 반응인 개질 반응에 이용될 수 있다.The outer surface at the center of the reforming reaction unit (190) transfers heat to the raw material gas inside as it comes into contact with the main passage (150) through which the combustion gas generated from the burner (120) passes. In addition, the reforming reaction unit (190) can transfer heat by the combustion gas passing through the reforming reaction unit (190) to the raw material gas by providing a plurality of spaced-apart exhaust passages (170) inside. That is, the reforming reaction unit (190) can have heat transfer performed in two ways by the main passage (150) and the exhaust passage (170). The heat transferred by the main passage (150) and the exhaust passage (170) in this way can be used for the reforming reaction, which is an endothermic reaction that is performed in the reforming reaction unit (190).

본 발명의 일 실시예에 따른 연료 개질장치(10)는 8개의 배출 유로관(170)을 마련하는 것으로 예시하였으나, 이에 제한되지 않고, 구현되는 연료 개질장치의 크기 또는 배출 유로관의 크기에 따라 그 개수는 변경 가능하다.The fuel reforming device (10) according to one embodiment of the present invention is exemplified as having eight exhaust pipes (170), but is not limited thereto, and the number may be changed depending on the size of the fuel reforming device being implemented or the size of the exhaust pipes.

개질 반응부(190)에서는 하부에 배치된 원료가스 주입구(200)로부터 공급받은 원료가스가 내부에 충진된 개질용 촉매(250)를 통과하면서 개질 반응이 진행될 수 있다. 개질용 촉매(250)를 통과하면서 개질된 개질 가스는 개질 반응부(190)의 상단 일측에 형성된 개질가스 배출구(210)로 배출될 수 있다.In the reforming reaction unit (190), the raw material gas supplied from the raw material gas inlet (200) arranged at the bottom may undergo a reforming reaction while passing through the reforming catalyst (250) filled inside. The reformed gas reformed while passing through the reforming catalyst (250) may be discharged through the reforming gas discharge port (210) formed on one side of the upper portion of the reforming reaction unit (190).

예컨대, 원료가스 주입구(200)와 개질가스 배출구(210)는 하우징(110)에 대하여 서로 수직하는 방향으로 형성될 수 있다.For example, the raw material gas inlet (200) and the reformed gas outlet (210) can be formed in a direction perpendicular to each other with respect to the housing (110).

개질 반응부(190)의 중심에 형성되는 메인 유로관(150)과 개질 반응부(190)의 내부에 원주 방향으로 이격 배치되는 배출 유로관(170)은, 개질 반응부(190)에 균일한 열을 공급하여 국부적 가열이 일어나는 것을 방지할 수 있다.The main flow path (150) formed at the center of the reforming reaction unit (190) and the exhaust flow path (170) spaced apart from each other in the circumferential direction inside the reforming reaction unit (190) can supply uniform heat to the reforming reaction unit (190) to prevent local heating from occurring.

또한, 개질 반응부(190)의 내부에 2차적인 흡열 반응을 유도하는 복수개의 배출 유로관(170)들을 마련함으로써, 장치 컴팩트화율을 획기적으로 높일 수 있는 효과를 가진다. 즉, 연료 개질장치(10)의 소형화를 이루면서도 개질 반응부(190)의 국부 가열을 억제할 수 있어 균일한 반응과 높은 열효율을 구현할 수 있다.In addition, by providing a plurality of exhaust conduits (170) that induce secondary endothermic reactions inside the reforming reaction unit (190), the device compactness rate can be dramatically increased. That is, while miniaturizing the fuel reforming device (10), local heating of the reforming reaction unit (190) can be suppressed, thereby realizing a uniform reaction and high thermal efficiency.

점화플러그 관(220)은 점화플러그가 설치가능한 관이다.The spark plug tube (220) is a tube into which a spark plug can be installed.

온도센서 관(230)은 촉매의 온도를 측정하기 위한 온도센서가 설치되는 관으로서, 본 발명에서는 3개의 온도센서 관(230)이 하우징(110)의 외표면에 길이방향에 따라 나란히 돌출 형성될 수 있다. 복수개의 온도센서 관(230)은 촉매의 영역별 온도를 각각 측정할 수 있다.The temperature sensor tube (230) is a tube in which a temperature sensor for measuring the temperature of the catalyst is installed. In the present invention, three temperature sensor tubes (230) can be formed to protrude side by side along the length direction on the outer surface of the housing (110). The plurality of temperature sensor tubes (230) can each measure the temperature of each region of the catalyst.

촉매 교환 관(240)은 개질 반응부(190) 내부에 충진되어 있는 촉매를 교체하기 위한 통로 역할을 할 수 있다.The catalyst exchange tube (240) can serve as a passage for replacing the catalyst filled inside the reforming reaction unit (190).

전술한 본 발명의 설명은 예시를 위한 것이며, 본 발명이 속하는 기술분야의 통상의 지식을 가진 자는 본 발명의 기술적 사상이나 필수적인 특징을 변경하지 않고서 다른 구체적인 형태로 쉽게 변형이 가능하다는 것을 이해할 수 있을 것이다. 그러므로 이상에서 기술한 실시예들은 모든 면에서 예시적인 것이며 한정적이 아닌 것으로 이해해야만 한다. 예를 들어, 단일형으로 설명되어 있는 각 구성 요소는 분산되어 실시될 수도 있으며, 마찬가지로 분산된 것으로 설명되어 있는 구성 요소들도 결합된 형태로 실시될 수 있다.The above description of the present invention is for illustrative purposes, and those skilled in the art will understand that the present invention can be easily modified into other specific forms without changing the technical idea or essential characteristics of the present invention. Therefore, it should be understood that the embodiments described above are exemplary in all respects and not restrictive. For example, each component described as a single component may be implemented in a distributed manner, and likewise, components described as distributed may be implemented in a combined form.

본 발명의 범위는 후술하는 청구범위에 의하여 나타내어지며, 청구범위의 의미 및 범위 그리고 그 균등 개념으로부터 도출되는 모든 변경 또는 변형된 형태가 본 발명의 범위에 포함되는 것으로 해석되어야 한다.The scope of the present invention is indicated by the claims set forth below, and all changes or modifications derived from the meaning and scope of the claims and their equivalent concepts should be interpreted as being included in the scope of the present invention.

Claims (7)

하우징과,Housing and, 하부로 공급되는 공기 및 연료가스를 이용하여 연소가스를 생성하는 버너와,A burner that generates combustion gas using air and fuel gas supplied from below, 상기 버너로부터 생성된 연소가스가 상향 이동하는 유로를 형성하며, 상기 하우징의 중심에 위치하는 메인 유로관과,A main duct located at the center of the housing, through which combustion gas generated from the burner moves upward, 상기 메인 유로관을 둘러싸며, 내부에 개질용 촉매가 마련되는 개질 반응부와,A reforming reaction section surrounding the main euro pipe and having a reforming catalyst provided inside, 상기 버너의 상부에 위치하되 상기 메인 유로관의 하부의 일측에 형성되어, 상기 연소가스가 배출되는 연소가스 배출구와,A combustion gas discharge port formed on one side of the lower portion of the main pipe and positioned above the burner, through which the combustion gas is discharged; 상기 메인 유로관을 통해 유입된 연소가스가 상기 연소가스 배출구를 향해 하향 이동하는 유로를 형성하는 배출 유로관을 포함하는 이중관 구조를 가지는 연료 개질장치.A fuel reforming device having a double-pipe structure including an exhaust pipe forming a path through which combustion gas introduced through the main combustion pipe moves downward toward the combustion gas exhaust port. 제1항에 있어서,In the first paragraph, 상기 메인 유로관 및 상기 개질 반응부의 상단에 형성되어, 상기 메인 유로관 및 상기 배출 유로관의 사이를 연결하는 상단 유로를 더 포함하는 것을 특징으로 하는 이중관 구조를 가지는 연료 개질장치.A fuel reforming device having a double-pipe structure, characterized in that it further includes an upper duct formed at the upper end of the main duct and the reforming reaction section and connecting the main duct and the exhaust duct. 제2항에 있어서,In the second paragraph, 상기 하우징 및 상기 개질 반응부는 상기 메인 유로관을 동심원으로 하며, 상기 배출 유로관은 상기 개질 반응부의 내부에 형성되는 것을 특징으로 하는 이중관 구조를 가지는 연료 개질장치.A fuel reforming device having a double-pipe structure, wherein the housing and the reforming reaction unit are formed concentrically around the main duct, and the exhaust duct is formed inside the reforming reaction unit. 제3항에 있어서,In the third paragraph, 상기 배출 유로관은,The above discharge pipe, 상기 개질 반응부의 내부에 이격 배치되는 복수개의 배출 유로관들을 포함하는 것을 특징으로 하는 이중관 구조를 가지는 연료 개질장치.A fuel reforming device having a double-pipe structure, characterized by including a plurality of exhaust paths spaced apart from each other inside the reforming reaction section. 제3항에 있어서,In the third paragraph, 상기 메인 유로관 및 상기 배출 유로관의 상단과 하단은 개방되어 있고,The top and bottom of the above main euro pipe and the above discharge euro pipe are open, 상기 메인 유로관 및 상기 배출 유로관의 상단은 상기 상단 유로로 연결되며,The upper ends of the above main flow pipe and the above discharge flow pipe are connected to the upper flow pipe, 상기 메인 유로관과, 상기 배출 유로관의 하단은 상호간 차단되는 것을 특징으로 하는 이중관 구조를 가지는 연료 개질장치.A fuel reforming device having a double-pipe structure, characterized in that the main fuel pipe and the lower end of the exhaust fuel pipe are mutually blocked. 제5항에 있어서,In paragraph 5, 상기 메인 유로관의 길이가 상기 배출 유로관의 길이보다 길게 형성되는 것을 특징으로 하는 이중관 구조를 가지는 연료 개질장치.A fuel reforming device having a double-pipe structure, characterized in that the length of the main fuel pipe is formed longer than the length of the exhaust fuel pipe. 제1항에 있어서,In the first paragraph, 상기 하우징의 최하단 측부에 형성되며, 공기가 공급되는 공기 주입구와,An air inlet formed at the lowest side of the housing and through which air is supplied, 상기 하우징의 최하단 측부에 형성되어, 연료가스가 공급되는 연료가스 주입구를 더 포함하되,Further comprising a fuel gas inlet formed at the lowest side of the housing to supply fuel gas, 상기 공기 주입구 및 상기 연료가스 주입구는 상기 버너의 하부에 위치하는 것을 특징으로 하는 이중관 구조를 가지는 연료 개질장치.A fuel reforming device having a double-pipe structure, characterized in that the air inlet and the fuel gas inlet are located at the bottom of the burner.
PCT/KR2023/021001 2023-11-27 2023-12-19 Fuel reforming apparatus having double pipe structure Pending WO2025116113A1 (en)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
KR20230166900 2023-11-27
KR10-2023-0166900 2023-11-27
KR1020230185515A KR20250079813A (en) 2023-11-27 2023-12-19 Apparatus for reforming fuel with dual pipe structure
KR10-2023-0185515 2023-12-19

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WO2025116113A1 true WO2025116113A1 (en) 2025-06-05

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007091584A (en) * 2005-09-27 2007-04-12 Samsung Sdi Co Ltd Fuel reformer
JP2007308328A (en) * 2006-05-18 2007-11-29 Honda Motor Co Ltd Fuel cell reformer
KR20120047545A (en) * 2010-11-04 2012-05-14 삼성에스디아이 주식회사 Reformer
KR20190025381A (en) * 2017-09-01 2019-03-11 엘지전자 주식회사 Fuel reforming divice
KR20210157097A (en) * 2020-06-19 2021-12-28 주식회사 파나시아 Steam Hydrocarbon Reformer

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007091584A (en) * 2005-09-27 2007-04-12 Samsung Sdi Co Ltd Fuel reformer
JP2007308328A (en) * 2006-05-18 2007-11-29 Honda Motor Co Ltd Fuel cell reformer
KR20120047545A (en) * 2010-11-04 2012-05-14 삼성에스디아이 주식회사 Reformer
KR20190025381A (en) * 2017-09-01 2019-03-11 엘지전자 주식회사 Fuel reforming divice
KR20210157097A (en) * 2020-06-19 2021-12-28 주식회사 파나시아 Steam Hydrocarbon Reformer

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