KR20190002786U - Reformer installed matal net and net corrugating machine therfor - Google Patents

Reformer installed matal net and net corrugating machine therfor Download PDF

Info

Publication number
KR20190002786U
KR20190002786U KR2020190004389U KR20190004389U KR20190002786U KR 20190002786 U KR20190002786 U KR 20190002786U KR 2020190004389 U KR2020190004389 U KR 2020190004389U KR 20190004389 U KR20190004389 U KR 20190004389U KR 20190002786 U KR20190002786 U KR 20190002786U
Authority
KR
South Korea
Prior art keywords
mesh network
reformer
net
metal mesh
wall
Prior art date
Application number
KR2020190004389U
Other languages
Korean (ko)
Other versions
KR200493244Y1 (en
Inventor
이형섭
최용호
최구현
권철
윤주영
Original Assignee
(주) 보림테크
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by (주) 보림테크 filed Critical (주) 보림테크
Priority to KR2020190004389U priority Critical patent/KR200493244Y1/en
Publication of KR20190002786U publication Critical patent/KR20190002786U/en
Application granted granted Critical
Publication of KR200493244Y1 publication Critical patent/KR200493244Y1/en

Links

Images

Classifications

    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/06—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
    • C01B3/12—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with carbon monoxide
    • C01B3/14—Handling of heat and steam
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/06—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
    • C01B3/12—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with carbon monoxide
    • C01B3/16—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with carbon monoxide using catalysts
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02—Processes for making hydrogen or synthesis gas
    • C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
    • C01B2203/0227—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
    • C01B2203/0233—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step the reforming step being a steam reforming step
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02—Processes for making hydrogen or synthesis gas
    • C01B2203/0283—Processes for making hydrogen or synthesis gas containing a CO-shift step, i.e. a water gas shift step
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/06—Integration with other chemical processes
    • C01B2203/066—Integration with other chemical processes with fuel cells
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/08—Methods of heating or cooling
    • C01B2203/0805—Methods of heating the process for making hydrogen or synthesis gas
    • C01B2203/0811—Methods of heating the process for making hydrogen or synthesis gas by combustion of fuel
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/16—Controlling the process
    • C01B2203/1614—Controlling the temperature
    • C01B2203/1623—Adjusting the temperature

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Fuel Cell (AREA)

Abstract

본 고안은 가스분산용 메시망이 내부에 형성되는 개질기 및 이 메시망을 절곡하는 절곡기에 관한 것으로, 더욱 상세하게는 개질기 내부로 유입되는 가스를 내부에서 잘 분산되도록 유도하면서 동시에 열분산을 원활하게 하기 위해서 절곡되는 금속재 메시망을 포함하는 개질기와, 이러한 금속재 메시망을 연속적으로 절곡할 수 있도록 하는 메시망 절곡기에 관한 것이다.
본 고안에 의하면 개질기 내부의 내벽과 내벽사이에 절곡된 금속재 메시망이 형성되므로 유입된 가스가 메시망에 의해서 분산이 이루어지면서 이송되므로 열의 전달은 물론 반응이 원활이 일어나고, 버너로부터 전달되는 열이 금속재 메시망에 의해서 전도로 다음 내벽까지 빠르게 전달되어 촉매제의 분위기 온도가 빠르게 보상되어 적정온도를 유지할 수 있어서 반응이 원활해지며, 제공되는 절단기에 의해서 금속재 메시망을 쉽게 접을 수 있어서 작업의 효율이 좋은 등의 효과가 발생한다The present invention relates to a reformer in which a gas dispersing mesh network is formed therein and a bending machine for bending the mesh network, and more particularly, induces a gas flowing into the reformer to be dispersed well in the inside and smoothly dissipates heat at the same time. The present invention relates to a reformer including a metal mesh network that is bent to make a metal mesh network, and a mesh network bending machine for continuously bending the metal mesh network.
According to the present invention, a metal mesh network bent between the inner wall and the inner wall of the reformer is formed, so that the incoming gas is transported while being dispersed by the mesh network, so that not only heat transfer but also reaction occurs smoothly, and heat transmitted from the burner The metal mesh net is quickly transferred to the next inner wall of the conduction path to quickly compensate the atmosphere temperature of the catalyst to maintain the proper temperature, thereby facilitating the reaction, and the metal mesh net can be easily folded by the cutter provided so that the work efficiency is improved. Good back effects occur

Description

가스분산용 메시망이 내부에 형성되는 개질기 및 이 메시망을 절곡하는 절곡기 {REFORMER INSTALLED MATAL NET AND NET CORRUGATING MACHINE THERFOR}A reformer in which a gas dispersion mesh network is formed inside and a bending machine for bending the mesh network {REFORMER INSTALLED MATAL NET AND NET CORRUGATING MACHINE THERFOR}

본 고안은 가스분산용 메시망이 내부에 형성되는 개질기 및 이 메시망을 절곡하는 절곡기에 관한 것으로, 더욱 상세하게는 개질기 내부로 유입되는 가스를 내부에서 잘 분산되도록 유도하면서 동시에 열분산을 원활하게 하기 위해서 절곡되는 금속재 메시망을 포함하는 개질기와, 이러한 금속재 메시망을 연속적으로 절곡할 수 있도록 하는 메시망 절곡기에 관한 것이다.The present invention relates to a reformer in which a gas dispersing mesh network is formed therein and a bending machine for bending the mesh network, and more particularly, induces a gas flowing into the reformer to be dispersed well in the inside and smoothly dissipates heat at the same time. The present invention relates to a reformer including a metal mesh network that is bent to make a metal mesh network, and a mesh network bending machine for continuously bending the metal mesh network.

연료전지에 사용되고 있는 연료개질기는 버너의 열을 이용하여 반응기에서 연료를 개질시켜 수소, 일산화탄소, 이산화탄소 등과 같은 생성물 가스를 얻고, 이 생성물 가스는 시프트 컨버터(shift converter) 등을 통과하면서 연료전지스택(stack)에서 필요한 수소가스를 얻게 된다.The fuel reformer used in the fuel cell reforms the fuel in the reactor by using the heat of the burner to obtain a product gas such as hydrogen, carbon monoxide, carbon dioxide, etc., and the product gas passes through a shift converter and the like. the required hydrogen gas in the stack).

종래의 연료개질기에 사용되던 버너튜브는 주로 반응기 외부에서 열을 공급한 후 다시 외부로 빠져나가도록 설계되어 있다. 따라서 종래의 버너튜브로는 열을 충분히 공급하지 못하고 바이-패스(by-pass)하는 열 매체가 많게 되어, 결과적으로 연료의 소모량을 증가시켜 왔다. The burner tube used in the conventional fuel reformer is mainly designed to exit after supplying heat from the outside of the reactor. Therefore, a conventional burner tube has a large amount of heat medium which does not supply enough heat and bypasses it, resulting in increased fuel consumption.

도1의 도시된 연료개질기는 종래의 연료전지용 연료개질기를 대표한다.The fuel reformer shown in FIG. 1 represents a conventional fuel reformer for a fuel cell.

상기 연료개질기는 촉매층(3)을 갖는 반응기(2)가 개질기 내부에 위치하고, 버너(1)의 열공급 영역이 반응기(2) 외부에 위치되기 때문에 열손실이 크도록 설계되어 있다. 버너(1) 내부로 공기입구(11)를 통하여 공기가 유입되고, 버너연료입구(12)를 통하여 버너연료가 유입된다. The fuel reformer is designed so that the heat loss is large because the reactor 2 having the catalyst layer 3 is located inside the reformer and the heat supply region of the burner 1 is located outside the reactor 2. Air is introduced into the burner 1 through the air inlet 11, and burner fuel is introduced through the burner fuel inlet 12.

상기 버너(1)에서 연료가 연소되어 반응기(2)를 가열시킨 후 버너 배기가스출구(13)를 통하여 배기가스가 배출된다. 반응기(2)에서는 반응연료가 반응연료입구(15)를 통하여 내부로 주입되고 촉매층(3)에서 개질반응 후 반응연료출구(14)를 통하여 배출된다.Fuel is combusted in the burner 1 to heat the reactor 2, and then exhaust gas is discharged through the burner exhaust gas outlet 13. In the reactor 2, the reaction fuel is injected into the reactor through the reaction fuel inlet 15 and discharged through the reaction fuel outlet 14 after the reforming reaction in the catalyst layer 3.

상기 반응연료출구(14)로 배출된 생성가스는 시프트 컨버터(도시되지 않음)로 유입되어 일산화탄소가 스팀과 함께 반응하여 이산화탄소와 연료전지스택에 필요한 수소가스를 발생시킨다. The generated gas discharged to the reaction fuel outlet 14 flows into a shift converter (not shown), and carbon monoxide reacts with steam to generate carbon dioxide and hydrogen gas required for the fuel cell stack.

상기 반응기(2) 내부의 온도는 약 800℃∼ 900 ℃에 달하기 때문에, 버너(1)에 의하여 그 온도가 유지되도록 계속 가열하여야 한다. Since the temperature inside the reactor 2 reaches about 800 ° C. to 900 ° C., it must be continuously heated so that the temperature is maintained by the burner 1.

상기 촉매층은 반응기 상단과 하단의 스크린으로 고정되어 있으며 그 내용물이 귀금속 촉매와 이를 담지하고 있는 담체 또는 지지체로 이루어져 있는 것으로, 반응연료의 개질반응을 촉진시킨다.The catalyst layer is fixed to a screen at the top and bottom of the reactor, the contents of which are composed of a noble metal catalyst and a support or support carrying the same, and promotes the reforming reaction of the reaction fuel.

그러나, 종래의 개질기는 다음과 같은 문제점이 있었다.However, the conventional reformer has the following problems.

(1) 종래의 개질기의 내부에는 다수의 내벽들이 존재하고, 이러한 내벽들 사이로 가스가 이동되는데, 가스가 이동하는 속도가 높아서 열의 전달이 원활하지 못하여 촉매에 의한 반응이 전반적으로 일어나지 못한다. (1) In the conventional reformer, a plurality of inner walls exist, and gas is moved between these inner walls. The gas is moved at a high speed so that heat transfer is not smooth, and reaction by the catalyst does not occur overall.

(2) 개질기의 내부에 공간이 있어서 열전달이 원활하지 못하여 촉매에 열전달이 원활히 이루어지지 않는다.(2) Since there is a space inside the reformer, heat transfer is not smooth and heat transfer to the catalyst is not smooth.

상기한 문제점을 해결하기 위해서, 본 고안은 내벽과 내벽 사이에 절곡된 금속재 메시망이 형성되되, In order to solve the above problems, the present invention is formed a metal mesh network bent between the inner wall and the inner wall,

상기 메시망은 수직하게 설치되고, 수평방향으로는 지그재그로 절곡되어 포함되는 것을 특징으로 한다. The mesh network is installed vertically, it is characterized in that it is included bent in a zigzag in the horizontal direction.

상기 메시망을 연속적으로 절곡하기 위해서 절곡기가 제공되는데, 몸체가 형성되고, 상기 몸체의 상단에 대향하게 회전할 수 있도록 형성되는 한 쌍의 축이 형성되며, 상기 각 축에는 다수개의 날개판이 형성되고, 상기 각각의 축에서 회전하는 각 날개판은 서로 엇갈리게 삽입되면서 대향하게 회전하도록 형성되는 것을 특징으로 한다.A bending machine is provided to continuously bend the mesh network, and a body is formed, and a pair of shafts are formed to rotate to face the upper end of the body, and each wing plate is formed with a plurality of wing plates. Each blade is rotated on each of the shafts, characterized in that the blades are formed to rotate to face each other while being staggered with each other.

본 고안의 가스분산용 메시망이 내부에 형성되는 개질기 및 이 메시망을 절곡하는 절곡기에 의하면 다음과 같은 효과가 발생한다.According to the reformer in which the gas dispersion mesh network of the present invention is formed and the bending machine for bending the mesh network, the following effects occur.

(1) 개질기 내부의 내벽과 내벽사이에 절곡된 금속재 메시망이 형성되므로 유입된 가스가 메시망에 의해서 분산이 이루어지면서 이송되므로 열의 전달은 물론 반응이 원활이 일어난다. (1) Since the bent metal mesh network is formed between the inner wall and the inner wall of the reformer, the incoming gas is transported while being dispersed by the mesh network, so that the heat transfer and the reaction occur smoothly.

(2) 버너로부터 전달되는 열이 금속재 메시망에 의해서 전도의 방법으로 다음 내벽까지 빠르게 전달되어 촉매제의 분위기 온도가 빠르게 보상되어 적정온도를 유지할 수 있어서 반응이 원활해진다.(2) The heat transferred from the burner is quickly transferred to the next inner wall by the method of conduction by the metal mesh network, and the atmospheric temperature of the catalyst is quickly compensated, so that the reaction can be smoothly maintained.

(3) 제공되는 절단기에 의해서 금속재 메시망을 쉽게 접을 수 있어서 작업의 효율이 좋다.(3) The metal mesh net can be easily folded by the cutter provided, so the work efficiency is good.

도 1은 종래의 개질기의 개념도.
도 2는 본 고안의 바람직한 실시예로 형성된 메시망이 설치된 개질기의 평면개념도.
도 3은 본 고안의 바람직한 실시예로 형성된 개질기에 사용되는 메시망의 일부사시개념도.
도 4는 본 고안의 바람직한 실시예로 형성된 메시망을 형성하는 장치의 사시도.
도 5는 본 고안의 바람직한 실시예로 형성된 메시망을 형성하는 장치의 축과 날개판을 나타낸 측면도. 1 is a conceptual diagram of a conventional reformer.
Figure 2 is a plan view of the reformer is installed mesh mesh formed in a preferred embodiment of the present invention.
3 is a partial perspective view of the mesh network used in the reformer formed by the preferred embodiment of the present invention.
4 is a perspective view of an apparatus for forming a mesh network formed by a preferred embodiment of the present invention.
Figure 5 is a side view showing the shaft and wing plate of the apparatus for forming a mesh network formed by a preferred embodiment of the present invention.

본 고안은 내벽(5)과 내벽(5) 사이에 절곡된 금속재 메시망(10)이 형성되되, 상기 메시망(10)은 수직하게 설치되고, 수평방향으로는 지그재그로 절곡되어 포함된다.According to the present invention, a metal mesh network 10 bent between the inner wall 5 and the inner wall 5 is formed, and the mesh network 10 is vertically installed and is bent in a zigzag horizontal direction.

상기 메시망(10)은 금속재로 형성되고, 내부에 형성된 메시(mesh)는 공간면적이 10㎟~ 50㎟이 적당하고, 공간면적이 좁은 메시를 사용할 경우에는 가스의 유동에 방해를 주고, 너무 넓을 경우에는 가스의 유동에 주는 영향이 미비하다. The mesh network 10 is formed of a metal material, the mesh formed therein has a suitable space area of 10 mm 2 to 50 mm 2, and when a mesh having a narrow space area is used, it impedes the flow of gas. If large, the influence on the flow of gas is insignificant.

상기 메시망(10)은 절곡기에 의해서 절곡되어 수평방향으로 지그재그로 구성되어 가스가 유동할 때 하단으로 가면서 난류를 형성하여 전체적으로 고르게 분포될 수 있다.The mesh network 10 is bent by a bending machine and composed of zig-zags in a horizontal direction, and when the gas flows, the mesh network 10 forms a turbulent flow toward the bottom to be evenly distributed throughout.

만약, 내벽(5)과 내벽(5)의 공간이 충분하다면 절곡된 메시망(10)을 나란하게 다수개를 설치하면 가스의 분산에 유리하다.If the space between the inner wall 5 and the inner wall 5 is sufficient, it is advantageous to disperse the gas by providing a plurality of bent mesh networks 10 side by side.

상기 메시망(10)의 재질은 스텐레스 재질로 이루어지고, 권취되어 제공되고, 귄취된 상태의 메시망을 절곡기에 넣고 지그재그로 형성한 후에 내벽(5)과 내벽(5) 사이에 설치한다.The material of the mesh network 10 is made of stainless steel, is wound and provided, and is placed between the inner wall 5 and the inner wall 5 after the mesh net in the curled state is placed in a bending machine and formed in a zigzag.

상기 메시망을 연속적으로 절곡하기 위해서 절곡기가 제공되는데, 몸체(100)가 형성되고, 상기 몸체의 상단에 대향하게 회전할 수 있도록 형성되는 한 쌍의 축(150)이 형성되며, 상기 각 축에는 다수개의 날개판(170)이 형성되며, 상기 각각의 축에서 회전하는 각 날개판(170)은 서로 엇갈리게 삽입되면서 대향하게 회전하도록 형성된다.A bending machine is provided to continuously bend the mesh network, and a body 100 is formed, and a pair of shafts 150 are formed to rotate to face the upper end of the body, and each of the shafts A plurality of wing plates 170 are formed, and each wing plate 170 that rotates in each of the shafts is alternately inserted to rotate oppositely.

상기 날개판(170)은 각 축에 4개 ~ 6개가 방사형으로 형성되고, 서로 삽입되면서 회전할 수 있도록 일정각도로 틀어져서 고정된다. The wing plate 170 is formed in four to six radial in each axis, and is fixed by twisting at a predetermined angle to rotate while being inserted into each other.

상기 몸체(100)의 일측에는 메시망을 밀어넣는 받침대가 형성되고, 상기 받침대는 날개판(170)의 사이에 위치할 수 있도록 형성된다.One side of the body 100 is formed with a pedestal for pushing the mesh network, the pedestal is formed to be located between the wing plate 170.

본 고안에 의하면 개질기 내부의 내벽과 내벽사이에 절곡된 금속재 메시망이 형성되므로 유입된 가스가 메시망에 의해서 분산이 이루어지면서 이송되므로 열의 전달은 물론 반응이 원활이 일어나고, 버너로부터 전달되는 열이 금속재 메시망에 의해서 전도로 다음 내벽까지 빠르게 전달되어 촉매제의 분위기 온도가 빠르게 보상되어 적정온도를 유지할 수 있어서 반응이 원활해지며, 제공되는 절단기에 의해서 금속재 메시망을 쉽게 접을 수 있어서 작업의 효율이 좋은 등의 효과가 발생한다.According to the present invention, a metal mesh network bent between the inner wall and the inner wall of the reformer is formed, so that the incoming gas is transported while being dispersed by the mesh network, so that not only heat transfer but also reaction occurs smoothly, and heat transmitted from the burner The metal mesh net is quickly transferred to the next inner wall of the conduction path to quickly compensate the atmosphere temperature of the catalyst to maintain the proper temperature, thereby facilitating the reaction, and the metal mesh net can be easily folded by the cutter provided so that the work efficiency is improved. Good back effects occur.

본 고안은 첨부된 도면을 참조하여 바람직한 실시 예를 중심으로 기술되었지만 당업자라면 이러한 기재로부터 후술하는 특허청구범위에 의해 포괄되는 본 고안의 범주를 벗어남이 없이 다양한 변형이 가능하다는 것은 명백하다.Although the present invention has been described with reference to the accompanying drawings, it will be apparent to those skilled in the art that various modifications are possible without departing from the scope of the present invention, which is encompassed by the following claims.

5 : 내벽 10 : 메시망
100 : 몸체 150 : 축
170 : 날개판5: inner wall 10: mesh network
100: body 150: axis
170: wing plate

Claims (1)

내벽(5)과 내벽(5) 사이에 절곡된 금속재 메시망(10)이 형성되되, 상기 메시망(10)은 수직하게 설치되고, 수평방향으로는 지그재그로 절곡되어 포함되는 일반적인 개질기에 있어서,
상기 메시망은 스텐레스로 형성되고, 메시의 공간면적은 10㎟~ 50㎟이고, 상기 메시망이 적어도 2개가 형성되는 것을 특징으로 하는 가스분산용 메시망이 내부에 형성되는 개질기.In the general reformer including a metal mesh network (10) bent between the inner wall (5) and the inner wall (5) is formed, the mesh network (10) is installed vertically, bent in a zigzag in the horizontal direction,
The mesh network is formed of stainless steel, the space area of the mesh is 10mm2 ~ 50mm2, the reformer is formed inside the gas dispersion mesh network, characterized in that at least two mesh network is formed.
KR2020190004389U 2019-10-30 2019-10-30 Matal net corrugating machine therfor for reformer KR200493244Y1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR2020190004389U KR200493244Y1 (en) 2019-10-30 2019-10-30 Matal net corrugating machine therfor for reformer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR2020190004389U KR200493244Y1 (en) 2019-10-30 2019-10-30 Matal net corrugating machine therfor for reformer

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
KR1020180014904A Division KR20190095656A (en) 2018-02-07 2018-02-07 Reformer installed matal net and net corrugating machine therfor

Publications (2)

Publication Number Publication Date
KR20190002786U true KR20190002786U (en) 2019-11-06
KR200493244Y1 KR200493244Y1 (en) 2021-02-26

Family

ID=68531226

Family Applications (1)

Application Number Title Priority Date Filing Date
KR2020190004389U KR200493244Y1 (en) 2019-10-30 2019-10-30 Matal net corrugating machine therfor for reformer

Country Status (1)

Country Link
KR (1) KR200493244Y1 (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06192955A (en) * 1992-12-25 1994-07-12 Morimura Kosan Kk Production of wave-shaped net-like article
KR20120074401A (en) * 2010-12-28 2012-07-06 지에스칼텍스 주식회사 Fuel processor of fuel cell
JP6097384B2 (en) * 2013-03-25 2017-03-15 住友精密工業株式会社 Fuel reformer and fuel cell
KR101947571B1 (en) * 2017-12-30 2019-05-20 (주)보림테크 Reformer installed honeycom support at burner part

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06192955A (en) * 1992-12-25 1994-07-12 Morimura Kosan Kk Production of wave-shaped net-like article
KR20120074401A (en) * 2010-12-28 2012-07-06 지에스칼텍스 주식회사 Fuel processor of fuel cell
JP6097384B2 (en) * 2013-03-25 2017-03-15 住友精密工業株式会社 Fuel reformer and fuel cell
KR101947571B1 (en) * 2017-12-30 2019-05-20 (주)보림테크 Reformer installed honeycom support at burner part

Also Published As

Publication number Publication date
KR200493244Y1 (en) 2021-02-26

Similar Documents

Publication Publication Date Title
JP4068111B2 (en) Hydrogen generator and fuel cell system provided with the same
BRPI0810937B1 (en) HIGH AND THERMALLY INTEGRATED AND COMBINED STEAM REFORMER FOR THE PRODUCTION OF HYDROGEN FROM A FUEL SOURCE AND A STEAM REFORMER ASSEMBLY FOR USE IN A FUEL PROCESSING SYSTEM
KR102456288B1 (en) Scalable Heat Exchanger Reformer for Syngas Generation
JP4830591B2 (en) Circular mixing / distribution header
JP2001155756A (en) Vapor-reforming reactor for fuel cell
CN107667070A (en) Catalytic burner equipment
KR101947571B1 (en) Reformer installed honeycom support at burner part
US9279581B2 (en) Steam boiler for a steam reformer
KR20190002786U (en) Reformer installed matal net and net corrugating machine therfor
KR102315289B1 (en) Steam Reformer with Multi Reforming Reactor
KR20190095656A (en) Reformer installed matal net and net corrugating machine therfor
US8263274B2 (en) Steam reformer with recuperative heat exchanger
KR102184495B1 (en) 7 normal cubic meter per hour hydrogen production apparatus
JP5163147B2 (en) Heat exchanger and combined fuel reactor
JP4904867B2 (en) Fuel processor
JPS5826002A (en) Steam reforming method and reaction tube for steam reforming
US8999016B2 (en) Fuel processor and method for generating hydrogen rich gas
KR100429602B1 (en) Fuel Reformer for Fuel Cell
JP3306430B2 (en) Reformer
JPH04322739A (en) Fuel reformer for fuel cell
JP5643706B2 (en) Hydrogen-containing gas generator
KR101480085B1 (en) Fuel reformer having gas distributor for uniform gas flow formation
JP2002029705A (en) Reforming device
JP3555703B2 (en) Hollow cylindrical plate reformer
JP2004115320A (en) Reforming apparatus

Legal Events

Date Code Title Description
A201 Request for examination
E902 Notification of reason for refusal
E90F Notification of reason for final refusal
E701 Decision to grant or registration of patent right