JPH1130491A - Honeycomb heat storage structure - Google Patents
Honeycomb heat storage structureInfo
- Publication number
- JPH1130491A JPH1130491A JP9184949A JP18494997A JPH1130491A JP H1130491 A JPH1130491 A JP H1130491A JP 9184949 A JP9184949 A JP 9184949A JP 18494997 A JP18494997 A JP 18494997A JP H1130491 A JPH1130491 A JP H1130491A
- Authority
- JP
- Japan
- Prior art keywords
- honeycomb
- honeycomb structure
- temperature side
- heat storage
- porosity
- 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.)
- Granted
Links
- 238000005338 heat storage Methods 0.000 title claims abstract description 39
- 239000007789 gas Substances 0.000 claims abstract description 39
- 239000002918 waste heat Substances 0.000 claims abstract description 10
- 239000002994 raw material Substances 0.000 claims abstract 2
- 238000010304 firing Methods 0.000 claims description 15
- 239000000463 material Substances 0.000 claims description 15
- 229910052878 cordierite Inorganic materials 0.000 claims description 4
- JSKIRARMQDRGJZ-UHFFFAOYSA-N dimagnesium dioxido-bis[(1-oxido-3-oxo-2,4,6,8,9-pentaoxa-1,3-disila-5,7-dialuminabicyclo[3.3.1]nonan-7-yl)oxy]silane Chemical compound [Mg++].[Mg++].[O-][Si]([O-])(O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2)O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2 JSKIRARMQDRGJZ-UHFFFAOYSA-N 0.000 claims description 4
- KZHJGOXRZJKJNY-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Si]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O KZHJGOXRZJKJNY-UHFFFAOYSA-N 0.000 claims description 4
- 229910044991 metal oxide Inorganic materials 0.000 claims description 4
- 150000004706 metal oxides Chemical class 0.000 claims description 4
- 229910052863 mullite Inorganic materials 0.000 claims description 4
- 239000002912 waste gas Substances 0.000 abstract 4
- 238000002485 combustion reaction Methods 0.000 description 17
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 10
- 230000035939 shock Effects 0.000 description 7
- 229910000505 Al2TiO5 Inorganic materials 0.000 description 6
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 6
- AABBHSMFGKYLKE-SNAWJCMRSA-N propan-2-yl (e)-but-2-enoate Chemical compound C\C=C\C(=O)OC(C)C AABBHSMFGKYLKE-SNAWJCMRSA-N 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 239000000446 fuel Substances 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 4
- 238000005245 sintering Methods 0.000 description 4
- 239000011232 storage material Substances 0.000 description 4
- 239000000919 ceramic Substances 0.000 description 3
- 238000005336 cracking Methods 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000032683 aging Effects 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 150000002736 metal compounds Chemical class 0.000 description 2
- 230000002093 peripheral effect Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- -1 alumina Chemical class 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 210000004027 cell Anatomy 0.000 description 1
- 210000002421 cell wall Anatomy 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/14—Thermal energy storage
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P80/00—Climate change mitigation technologies for sector-wide applications
- Y02P80/10—Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
- Y02P80/15—On-site combined power, heat or cool generation or distribution, e.g. combined heat and power [CHP] supply
Landscapes
- Air Supply (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、複数のハニカム構
造体を積み重ねてなり、貫通孔から構成される流路に排
ガスと被加熱ガスとを交互に通過させて排ガス中の廃熱
を回収するハニカム状蓄熱体に関し、特に高温の排ガス
に対して好適に使用できるハニカム状蓄熱体に関するも
のである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a stack of a plurality of honeycomb structures, and the exhaust gas and the gas to be heated are alternately passed through a flow path composed of through holes to recover waste heat in the exhaust gas. The present invention relates to a honeycomb-shaped heat storage element, and more particularly to a honeycomb-shaped heat storage element that can be suitably used for high-temperature exhaust gas.
【0002】[0002]
【従来の技術】従来から、鉄鋼、アルミ、ガラス等の溶
融及び加熱加工等に用いる一般産業用の燃焼加熱炉にお
いて、エネルギー効率を改善するために、排ガス中の廃
熱を回収し燃焼用空気を予め加熱する方法が行われてい
る。これに用いる蓄熱体として、従来は、例えば特開昭
58−26036号公報に記載の如くセラミックボー
ル、サドル、ペレット等が使用されていたが、排ガスあ
るいは燃焼用空気等が蓄熱体を通過する際圧力損失が高
く、また、容積当たりの熱交換面積が小さいため、蓄熱
体容積を大きくする必要があった。2. Description of the Related Art Conventionally, in a general industrial combustion heating furnace used for melting and heating of steel, aluminum, glass, etc., in order to improve energy efficiency, waste heat in exhaust gas is recovered and air for combustion is recovered. Is preliminarily heated. Conventionally, ceramic balls, saddles, pellets and the like have been used as described in JP-A-58-26036, for example, when exhaust gas or combustion air passes through the heat storage. Since the pressure loss is high and the heat exchange area per volume is small, it is necessary to increase the volume of the heat storage body.
【0003】これを改善するために、近年は蓄熱体とし
てハニカム構造体を用いる事が、例えば特開平4−25
1190号公報に記載されているように行われている。
ハニカム構造体では排ガス等の通過における圧力損失が
低く、容積当たりの熱交換面積も大きいことから、ハニ
カム構造体は非常に効率的な熱交換を行うことができ
る。しかしながら、これらのハニカム構造体にも以下の
ような問題点があった。すなわち、ハニカム構造体は非
常に薄いセル壁から構成されているため、従来使用され
ていたセラミックボール等と比較すると強度、熱耐久性
等に問題があった。そのため、衝撃や異常高温ガスの接
触等によってハニカム構造体が破損し蓄熱体として機能
しなくなる場合が発生し、最悪の場合、システムの停止
につながる問題があった。In order to improve this, in recent years, it has been proposed to use a honeycomb structure as a heat storage body.
This is performed as described in Japanese Patent No. 1190.
Since the pressure loss in passing the exhaust gas and the like is low in the honeycomb structure and the heat exchange area per volume is large, the honeycomb structure can perform very efficient heat exchange. However, these honeycomb structures also have the following problems. That is, since the honeycomb structure is composed of very thin cell walls, there are problems in strength, heat durability, and the like, as compared with conventionally used ceramic balls and the like. For this reason, the honeycomb structure may be damaged by a shock or contact with an abnormally high-temperature gas or the like, and may not function as a heat storage body. In the worst case, there is a problem that the system stops.
【0004】[0004]
【発明が解決しようとする課題】上述したこれらの問題
を解消するために、本出願人は特願平7−342634
号においてアルミニウムチタネート製ハニカム構造体を
使用した蓄熱体を提案した。アルミニウムチタネートは
耐熱性に優れる材料であることが知られている。しか
し、長期間の使用ではアルミニウムチタネートは分解す
る傾向があり、また、非常に高価な材料である。そのた
め、アルミニウムチタネート製ハニカム構造体を使用す
ることで熱効率を改善しても、これらアルミニウムチタ
ネート製ハニカム構造体を使用すると、従来のセラミッ
クボール等に対するコストメリットが同等もしくは若干
しか望めない問題があった。従って、ランニングコスト
を含めたコストメリットが有効に発揮できる蓄熱体の開
発が必要であった。In order to solve the above-mentioned problems, the present applicant has filed a Japanese Patent Application No. 7-342634.
Proposed a heat storage body using a honeycomb structure made of aluminum titanate. It is known that aluminum titanate is a material having excellent heat resistance. However, over long periods of use, aluminum titanate tends to decompose and is a very expensive material. Therefore, even if the thermal efficiency is improved by using the honeycomb structure made of aluminum titanate, the use of these honeycomb structures made of aluminum titanate has a problem that the cost merit over the conventional ceramic balls or the like can be expected to be equal or only slightly. . Therefore, it has been necessary to develop a heat storage body that can effectively exhibit cost advantages including running costs.
【0005】本発明の目的は上述した課題を解消して、
高温の排ガスに対しても破壊せず効率良く熱交換を行う
ことができ、しかもランニングコストを含めたコストメ
リットが有効に発揮できるハニカム状蓄熱体を提供しよ
うとするものである。An object of the present invention is to solve the above-mentioned problems,
An object of the present invention is to provide a honeycomb-shaped heat storage element that can efficiently perform heat exchange without breaking even high-temperature exhaust gas and that can effectively exhibit cost advantages including running costs.
【0006】[0006]
【課題を解決するための手段】本発明のハニカム状蓄熱
体は、複数のハニカム構造体を積み重ねてなり、貫通孔
から構成される流路に排ガスと被加熱ガスとを交互に通
過させて排ガス中の廃熱を回収するハニカム状蓄熱体に
おいて、少なくとも高温の排ガスに接する高温側のハニ
カム構造体の気孔率が、それ以外の低温側のハニカム構
造体の気孔率よりも低く、前記高温側のハニカム構造体
と低温側のハニカム構造体とが同一素材からなることを
特徴とするものである。According to the present invention, there is provided a honeycomb regenerator in which a plurality of honeycomb structures are stacked, and the exhaust gas and the gas to be heated are alternately passed through a flow path composed of through holes. In the honeycomb-shaped regenerator for recovering waste heat therein, at least the porosity of the honeycomb structure on the high-temperature side in contact with the high-temperature exhaust gas is lower than the porosity of the honeycomb structure on the other low-temperature side, and The honeycomb structure and the honeycomb structure on the low temperature side are made of the same material.
【0007】本発明における実施の形態を説明する前
に、上記構成の技術的作用について以下に説明する。ハ
ニカム構造体を蓄熱体として使用する場合の問題点は、
上述したように、強度、耐熱性による破壊及び高コスト
である。耐熱性を改善するために、材料的に実際の使用
温度に耐え得る材料を使用することは当業者として当然
である。例えば、従来から知られているアルミナを使用
した場合、アルミナの耐熱温度は十分に実使用に耐え得
るものであるが、アルミナの熱膨張が高く耐熱衝撃に非
常に弱い材料であることが当業者に広く知られている。Before describing the embodiments of the present invention, the technical operation of the above configuration will be described below. The problem when using the honeycomb structure as a heat storage is
As described above, it is destroyed due to strength and heat resistance, and is expensive. It is a matter of course for those skilled in the art to use materials capable of withstanding the actual use temperature in order to improve heat resistance. For example, when conventionally known alumina is used, although the heat resistance temperature of alumina can sufficiently withstand actual use, it is known to those skilled in the art that alumina has a high thermal expansion and is very weak against thermal shock. Widely known to.
【0008】ハニカム構造体を積み重ねることで組み合
わせてハニカム状蓄熱体とする場合、ハニカム構造体に
変形等があると、その部位で積み重ねた上下のハニカム
構造体の外周壁間に隙間が発生し、ハニカム構造体中を
通過する排ガスや燃焼用空気の流速が速くなり、また、
これらのガスが熱交換されずにハニカム状蓄熱体を通過
するため、ハニカム状蓄熱体に熱衝撃を発生する要因と
なっていた。本発明では、強度における問題をクリアす
るために、少なくとも高温の排ガスに接する高温側のハ
ニカム構造体として、気孔率がその他の低温側のハニカ
ム構造体よりも低く、強度に強いハニカム構造体で同一
組成からなるハニカム構造体を用いる。When honeycomb structures are combined to form a honeycomb-shaped regenerator, if the honeycomb structures are deformed or the like, a gap is generated between the outer peripheral walls of the upper and lower honeycomb structures stacked at that portion, The flow velocity of exhaust gas and combustion air passing through the honeycomb structure increases,
Since these gases pass through the honeycomb-shaped regenerator without heat exchange, they cause a thermal shock to the honeycomb-shaped regenerator. In the present invention, in order to clear the problem of strength, at least the high-temperature side honeycomb structure in contact with the high-temperature exhaust gas has a porosity lower than that of the other low-temperature side honeycomb structures, and is the same as the high-strength honeycomb structure. A honeycomb structure having a composition is used.
【0009】また、一般的に気孔率を低くするために
は、ハニカム構造体の焼成温度を高くして収縮させるこ
とが最も容易な方法であるが、収縮率が大きいためにハ
ニカム構造体が変形することが多々発生する。このよう
に変形したハニカム構造体を蓄熱体全てに使用すると、
先に記載したように隙間が生じて高温排ガスあるいは燃
焼用空気が熱交換されずに通過する。そのため、ハニカ
ム構造体に熱衝撃が発生し、ハニカム構造体にクラック
や割れを生じさせる。In general, in order to lower the porosity, it is easiest to shrink the honeycomb structure by increasing the firing temperature. However, since the shrinkage is large, the honeycomb structure is deformed. It often happens. When the honeycomb structure deformed in this way is used for all the heat storage bodies,
As described above, a gap is generated and high-temperature exhaust gas or combustion air passes through without heat exchange. Therefore, a thermal shock is generated in the honeycomb structure, and cracks and cracks are generated in the honeycomb structure.
【0010】よって、本発明では、低温側の耐熱特性へ
の要求が小さい部位のハニカム構造体には、焼成温度が
低く気孔率が高い、寸法精度に優れたハニカム構造体を
使用する。そうすることで、積み重ねてハニカム状蓄熱
体を構成した場合でも、上下のハニカム構造体の外周壁
間に隙間を生じさせず、クラックの問題を解決するだけ
でなくハニカム構造体の製造コストをも安価にすること
ができる。Therefore, in the present invention, a honeycomb structure having a low sintering temperature, a high porosity, and excellent dimensional accuracy is used for a portion of the honeycomb structure having a low requirement for heat resistance on the low temperature side. By doing so, even when the honeycomb-shaped heat accumulators are formed by stacking, no gap is formed between the outer peripheral walls of the upper and lower honeycomb structures, not only solving the problem of cracks but also reducing the manufacturing cost of the honeycomb structures. It can be cheap.
【0011】上記本発明の構成を実施するには、アルミ
ナ、ジルコニア等の単一金属酸化物を使用することが好
適である。すなわち、単一金属酸化物は焼成温度によっ
て容易に気孔率を変更することが可能である。これに対
し、複合金属化合物等を使用すると、焼成温度によって
は分解、異物質生成等が発生するため焼成温度のみによ
る気孔率変更が難しくなり、結果として製造コストが高
くなる。ここで、材料を選択するにあたり、使用される
排ガス温度に対して融点が高く軟化し難い材料であれ
ば、上記技術を使用することでクラック等の問題は解決
するため、従来から公知のいずれの材料も使用すること
ができる。In order to carry out the constitution of the present invention, it is preferable to use a single metal oxide such as alumina and zirconia. That is, the porosity of the single metal oxide can be easily changed depending on the firing temperature. On the other hand, when a composite metal compound or the like is used, decomposition, generation of foreign substances, and the like occur depending on the sintering temperature, so that it is difficult to change the porosity only by the sintering temperature. Here, in selecting the material, if the material has a high melting point with respect to the temperature of the exhaust gas to be used and is not easily softened, the problem such as cracks can be solved by using the above technology, and any conventionally known material can be used. Materials can also be used.
【0012】また、本発明では、さらに好適な例とし
て、高温側のハニカム構造体の開口率を低温側のハニカ
ム構造体の開口率よりも大きくする。これにより、高温
排ガスから廃熱を回収する際において吸温速度が緩やか
になり、高温に使用されるハニカム構造体の耐久特性を
一層向上させることが可能となる。Further, in the present invention, as a more preferable example, the opening ratio of the honeycomb structure on the high temperature side is made larger than the opening ratio of the honeycomb structure on the low temperature side. Thereby, when recovering waste heat from the high-temperature exhaust gas, the temperature absorption rate becomes slow, and the durability characteristics of the honeycomb structure used at a high temperature can be further improved.
【0013】[0013]
【発明の実施の形態】図1は本発明のハニカム状蓄熱体
の一例の構成を示す図である。図1に示す例において、
ハニカム状蓄熱体1は、直方体形状のハニカム構造体2
を、一方向に貫通孔3から構成される流路が揃うよう複
数個積み重ねて(ここでは2段に積み重ねて)構成され
ている。図1において、図中上方が排ガスに接する高温
側のハニカム構造体2であり、図中下方がそれ以外の低
温側のハニカム構造体2である。本発明の特徴は、上記
構成のハニカム状蓄熱体1において、高温側のハニカム
構造体2の気孔率を、低温側のハニカム構造体2の気孔
率よりも低く構成するとともに、高温側のハニカム構造
体2と低温側のハニカム構造体2とを同一素材で形成し
た点である。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is a diagram showing a configuration of an example of a honeycomb heat storage body of the present invention. In the example shown in FIG.
The honeycomb-shaped regenerator 1 has a rectangular parallelepiped honeycomb structure 2.
Are stacked (here, stacked in two stages) so that the flow paths constituted by the through holes 3 are aligned in one direction. In FIG. 1, the upper part in the figure is the honeycomb structure 2 on the high temperature side in contact with the exhaust gas, and the lower part in the figure is the other honeycomb structure 2 on the low temperature side. A feature of the present invention is that, in the honeycomb-shaped regenerator 1 having the above-described configuration, the porosity of the honeycomb structure 2 on the high-temperature side is lower than the porosity of the honeycomb structure 2 on the low-temperature side, and the honeycomb structure on the high-temperature side. The point is that the body 2 and the honeycomb structure 2 on the low temperature side are formed of the same material.
【0014】気孔率を変えたハニカム構造体2を得るた
めには、上述したように収縮率を小さく保ちハニカム構
造体2の変形を防止する観点から、焼成温度を変えるこ
とにより気孔率を変化させることが好ましい。また、高
温側のハニカム構造体2と低温側のハニカム構造体2の
材質としては、アルミナ、ジルコニア等の従来から蓄熱
体用の材料として知られているいずれの材料をも使用す
ることができるが、アルミナ、ジルコニア等の単一金属
酸化物を使用することが、焼成温度を変えることで容易
に気孔率を変更できるため好ましい。これに対し、複合
金属化合物等を使用すると、焼成温度によっては分解、
異物質生成等が発生するため焼成温度のみによる気孔率
変更が難しくなり、結果として製造コストが高くなる。In order to obtain the honeycomb structure 2 having a changed porosity, the porosity is changed by changing the firing temperature from the viewpoint of keeping the contraction rate small and preventing the deformation of the honeycomb structure 2 as described above. Is preferred. As the material of the honeycomb structure 2 on the high-temperature side and the honeycomb structure 2 on the low-temperature side, any material conventionally known as a material for a heat storage material such as alumina and zirconia can be used. It is preferable to use a single metal oxide such as alumina, zirconia, or the like because the porosity can be easily changed by changing the firing temperature. In contrast, when a composite metal compound or the like is used, decomposition and decomposition may occur depending on the firing temperature.
Since the generation of foreign substances and the like occurs, it is difficult to change the porosity only by the sintering temperature, and as a result, the production cost is increased.
【0015】図2は本発明のハニカム状蓄熱体の他の例
の構成を示す図である。図2に示す例において、ハニカ
ム状蓄熱体11は、図1に示す構成の高温側のハニカム
構造体2と低温側のハニカム構造体2とからなるハニカ
ム状蓄熱体1において、低温側のハニカム構造体の被加
熱ガスと接する面上にコージェライト、ムライト等から
なるハニカム構造体12からなる層を設けて構成されて
いる。図2に示す例では、図1に示す例と同様の効果を
得ることができるのに加えて、図1に示す例と比較して
コージェライト、ムライト等を使用できる分だけ安価に
ハニカム状蓄熱体11を作製することができる。また、
コージェライト、ムライト等からなるハニカム構造体1
2は温度の低い箇所にのみ設けられているため、高温の
排ガスと接触することによる熱衝撃の影響を受ける可能
性の少ないため、好ましい例となる。FIG. 2 is a diagram showing the configuration of another example of the honeycomb heat storage body of the present invention. In the example shown in FIG. 2, the honeycomb-shaped heat storage body 11 is composed of the honeycomb structure 2 on the high-temperature side and the honeycomb structure 2 on the low-temperature side having the configuration shown in FIG. 1. On the surface of the body in contact with the gas to be heated, a layer made of a honeycomb structure 12 made of cordierite, mullite or the like is provided. In the example shown in FIG. 2, the same effect as the example shown in FIG. 1 can be obtained, and in addition to the use of cordierite, mullite, etc., compared to the example shown in FIG. The body 11 can be made. Also,
Honeycomb structure 1 made of cordierite, mullite, etc.
2 is a preferable example because it is provided only in a low-temperature place, and is less likely to be affected by a thermal shock due to contact with high-temperature exhaust gas.
【0016】なお、図1および図2に示す例では、高温
側のハニカム構造体2と低温側のハニカム構造体2との
セル開口率については特に言及しなかったが、いずれの
場合も、高温側のハニカム構造体2の開口率を低温側の
ハニカム構造体2の開口率よりも大きくすると、高温排
ガスから廃熱を回収する際において吸温速度が緩やかに
なり、高温に使用されるハニカム構造体の耐久特性を一
層向上させることが可能となるため好ましい。In the examples shown in FIGS. 1 and 2, the cell opening ratio between the honeycomb structure 2 on the high temperature side and the honeycomb structure 2 on the low temperature side is not particularly mentioned. When the opening ratio of the honeycomb structure 2 on the lower side is made larger than the opening ratio of the honeycomb structure 2 on the lower side, the temperature absorption rate becomes slower when recovering waste heat from the high-temperature exhaust gas, and the honeycomb structure used at a high temperature This is preferable because the durability characteristics of the body can be further improved.
【0017】図3は本発明のハニカム状蓄熱体を使用し
た熱交換体を燃焼加熱炉の燃焼室に設置した例を示す図
である。図3に示す例において、21は燃焼室、22−
1、22−2は図1または図2に示す構造のハニカム状
蓄熱体、23−1、23−2はハニカム状蓄熱体22−
1、22−2から構成される熱交換体、24−1、24
−2は熱交換体23−1、23−2に設けた燃料投入口
である。図3に示す例において、2個の熱交換体23−
1、23−2を設けたのは、一方が高温の排ガスを流す
ことにより蓄熱を行っているとき、同時に他方が低温の
被加熱ガスを加熱できるよう構成して、熱交換を効率的
に行うためである。FIG. 3 is a view showing an example in which a heat exchanger using the honeycomb-shaped regenerator of the present invention is installed in a combustion chamber of a combustion heating furnace. In the example shown in FIG. 3, 21 is a combustion chamber, 22-
Reference numerals 1 and 22-2 denote honeycomb-shaped heat storage bodies having the structure shown in FIG. 1 or FIG. 2, and 23-1 and 23-2 denote honeycomb-shaped heat storage bodies 22-.
1, heat exchangers composed of 22-2, 24-1, 24
-2 is a fuel inlet provided in the heat exchangers 23-1 and 23-2. In the example shown in FIG. 3, two heat exchangers 23-
1, 23-2 is provided so that when one is storing heat by flowing high-temperature exhaust gas, the other can simultaneously heat the low-temperature gas to be heated, and heat exchange is efficiently performed. That's why.
【0018】図3に示す例において、片側のハニカム状
蓄熱体22−1の下方より燃焼用空気が進入する。ハニ
カム状蓄熱体22−1を通過した後に、燃料投入口24
−1から供給された燃料と混合され、燃焼室21内で点
火される。燃焼された排ガスは他方のハニカム状蓄熱体
22−2の上部より進入し、廃熱はハニカム状蓄熱体2
2−2に蓄熱され、低温となった排ガスは外部へ放出さ
れる。次に、燃焼用空気の進入方向が切り替えられ、先
程廃熱を回収した側のハニカム状蓄熱体22−2の下部
より燃焼用空気が進入する。この際、熱交換が行われ、
燃焼用空気は予熱されハニカム状蓄熱体22−2の上部
で燃料投入口24−2から供給された燃料と混合され、
燃焼室21内で点火される。排ガスは他方のハニカム状
蓄熱体22−1を通って排出されるが、この際、先程同
様にハニカム状蓄熱体22−1に廃熱が回収される。In the example shown in FIG. 3, combustion air enters from below one side of the honeycomb regenerator 22-1. After passing through the honeycomb-shaped regenerator 22-1, the fuel inlet 24
-1 and is ignited in the combustion chamber 21. The burned exhaust gas enters from the upper part of the other honeycomb-shaped heat storage body 22-2, and the waste heat is discharged from the honeycomb-shaped heat storage body 2-2.
Exhaust gas that has been stored at 2-2 and has become low temperature is discharged to the outside. Next, the entry direction of the combustion air is switched, and the combustion air enters from the lower part of the honeycomb-shaped heat storage body 22-2 on the side where the waste heat has been recovered earlier. At this time, heat exchange is performed,
The combustion air is preheated and mixed with the fuel supplied from the fuel inlet 24-2 at the upper part of the honeycomb-shaped regenerator 22-2,
It is ignited in the combustion chamber 21. The exhaust gas is discharged through the other honeycomb-shaped regenerator 22-1. At this time, waste heat is recovered by the honeycomb-shaped regenerator 22-1 as described above.
【0019】[0019]
【実施例】以下、実際の例について説明する。以下の表
1に示す形状および特性を有するアルミナからなるハニ
カム構造体A〜Dを準備し、高温側の蓄熱体Aと低温側
の蓄熱体Bとを以下の表2に示すように上記アルミナハ
ニカム構造体A〜Dから選択して、図1に示す形状のハ
ニカム状蓄熱体(試験No.1〜16)を作製した。次
に、得られた各ハニカム状蓄熱体を実験装置に組み込
み、所定の温度で1000時間保持するエージング試験
を実施した。エージング試験終了後、各蓄熱体の外観お
よび寸法収縮を調査した。また、各ハニカム状蓄熱体の
焼成エネルギー比および熱交換面積比を求めた。結果を
表2に示す。An actual example will be described below. Honeycomb structures A to D made of alumina having the shapes and characteristics shown in Table 1 below are prepared, and the high temperature side heat storage material A and the low temperature side heat storage material B are mixed with the above alumina honeycomb as shown in Table 2 below. Honeycomb regenerators (test Nos. 1 to 16) having the shape shown in FIG. 1 were prepared by selecting from structures A to D. Next, each of the obtained honeycomb-shaped regenerators was incorporated into an experimental apparatus, and an aging test was performed in which the honeycomb-shaped regenerator was maintained at a predetermined temperature for 1000 hours. After the aging test, the appearance and dimensional shrinkage of each heat storage body were examined. Further, the firing energy ratio and the heat exchange area ratio of each honeycomb-shaped regenerator were determined. Table 2 shows the results.
【0020】表2の結果において、蓄熱体AおよびBの
外観は、欠陥が全く存在しない例を◎、若干欠陥が存在
するが実使用に支障がない例を○、クラックが発生した
例を△、割れが発生した例を×として示した。蓄熱体A
およびBの寸法収縮は、焼成前後の各蓄熱体の寸法から
求めた。また、各ハニカム状蓄熱体の焼成エネルギー比
は、焼成に一番エネルギーを必要としないアルミナハニ
カム構造体Dを電気炉で焼成するのに必要なエネルギー
を基準として、各ハニカム状蓄熱体を電気炉で焼成する
のに必要なエネルギーとの比として求めた。さらに、各
ハニカム状蓄熱体の熱交換面積比は、幾何学的比表面積
から求めた貫通孔のガスと接触する部分の面積から求め
た。In the results shown in Table 2, the appearance of the heat storage bodies A and B is ◎ in the case where no defect is present, ○ in the case where the defect is slightly present but does not hinder the actual use, and Δ in the case where the crack is generated. And an example in which cracks occurred is indicated by x. Thermal storage A
And the dimensional shrinkage of B were determined from the dimensions of each heat storage body before and after firing. The firing energy ratio of each honeycomb-shaped regenerator is determined based on the energy required for firing the alumina honeycomb structure D, which requires the least energy for firing, in an electric furnace. And the ratio to the energy required for firing. Further, the heat exchange area ratio of each honeycomb-shaped regenerator was determined from the area of the portion of the through hole contacting the gas determined from the geometric specific surface area.
【0021】[0021]
【表1】 [Table 1]
【0022】[0022]
【表2】 [Table 2]
【0023】表1および表2の結果から明らかなよう
に、本発明例のハニカム状蓄熱体(試験No.2、4、
10、12)では、高温側(蓄熱体A)、低温側(蓄熱
体B)ともにハニカム構造体にはクラックや割れの発生
の問題がなかった。一方、高温側も低温側も全て同一の
気孔率が低いハニカム構造体(アルミナハニカム構造体
A、D)を使用した比較例のハニカム状蓄熱体(試験N
o.1、11)では、ハニカム構造体にクラックや割れ
が発生していた。これは、低温側に使用したハニカム構
造体を組み合わせる際に変形が大きく、ハニカム構造体
間に隙間が生じており、低温の焼成用空気が熱交換され
ずに上部まで進入し、熱衝撃によってクラックが発生し
たものと考えられる。また、低温側に使用したハニカム
構造体にも若干のクラックが発生しているが、これは高
温の排ガスが上記の隙間を通過し熱交換されずに低温部
まで進入することで、熱衝撃が発生したことによりクラ
ックが生じたものと考えられる。As is clear from the results of Tables 1 and 2, the honeycomb-shaped regenerator of the present invention example (Test Nos. 2, 4,
In 10 and 12), there was no problem of cracking or cracking in the honeycomb structure on both the high temperature side (heat storage body A) and the low temperature side (heat storage body B). On the other hand, the honeycomb-shaped heat storage material of the comparative example using the same honeycomb structure having low porosity (alumina honeycomb structures A and D) on both the high temperature side and the low temperature side (Test N)
o. In 1 and 11), cracks and cracks occurred in the honeycomb structure. This is because when the honeycomb structures used on the low temperature side are combined, deformation is large, gaps are formed between the honeycomb structures, and the low-temperature firing air enters the upper part without heat exchange and cracks due to thermal shock. Is considered to have occurred. Some cracks also occurred in the honeycomb structure used on the low-temperature side, but the high-temperature exhaust gas passed through the gap and entered the low-temperature portion without heat exchange, causing thermal shock. It is considered that a crack was caused by the occurrence.
【0024】さらに、高温側に気孔率が高いハニカム構
造体を使用した比較例のハニカム状蓄熱体(試験No.
5〜8、13〜16)では、高温排ガスによる収縮が大
きく、これによって割れが発生していた。この場合は、
下方の低温側に気孔率が高いハニカム構造体を使用しよ
うと気孔率の低いハニカム構造体を使用しようと、いず
れの場合も、上部の高温側のハニカム構造体が収縮して
隙間が開くため、高温排ガスあるいは低温燃焼用空気が
隙間から進入して、先程同様にクラックが生じたものと
考えられる。また、下部の低温側ハニカム構造体の収縮
も大きくなり、上記クラックの発生を助長する結果とな
った。Further, a honeycomb-shaped heat storage body of a comparative example using a honeycomb structure having a high porosity on the high temperature side (test No. 2).
5-8 and 13-16), the shrinkage due to the high-temperature exhaust gas was large, which caused cracking. in this case,
Regardless of whether a honeycomb structure with a high porosity is used on the lower low-temperature side or a honeycomb structure with a low porosity is used, the gap is opened because the honeycomb structure on the upper high-temperature side shrinks. It is probable that high-temperature exhaust gas or low-temperature combustion air entered through the gap and cracks were generated in the same manner as above. Further, the shrinkage of the lower-side low-temperature-side honeycomb structure also increased, which resulted in promoting the generation of the cracks.
【0025】一方、上部高温側に気孔率が低いハニカム
構造体を使用し、下部低温側に気孔率が高いハニカム構
造体を使用した本発明例のハニカム状蓄熱体では、上部
および下部のハニカム構造体ともに収縮が小さく、クラ
ックや割れも発生していなかった。また、本発明例のう
ち高温側のハニカム構造体に開口率が大きいものを使用
した本発明例のハニカム状蓄熱体(試験No.4)は、
さらに耐久性が向上していた。On the other hand, in the honeycomb heat storage body of the present invention in which a honeycomb structure having a low porosity is used on the upper high temperature side and a honeycomb structure having a high porosity is used on the lower low temperature side, the upper and lower honeycomb structures are used. Both bodies showed little shrinkage and no cracks or cracks occurred. Further, among the present invention examples, the honeycomb-shaped regenerator (test No. 4) of the present invention example using a high-temperature-side honeycomb structure having a large opening ratio was used.
Further, the durability was improved.
【0026】本発明は上述した実施例にのみ限定される
ものでなく、幾多の変形、変更が可能である。例えば、
上述した実施例では、高温の排ガスと接する高温側のハ
ニカム構造体を一層のみ設けたが、一層に限定されない
ことはいうまでもない。例えば、一層の高さが低いよう
な場合は、二層以上の気孔率の低いハニカム構造体から
高温側のハニカム構造体を構成しても良い。The present invention is not limited to the above-described embodiment, but can be variously modified and changed. For example,
In the embodiment described above, only one high-temperature-side honeycomb structure in contact with high-temperature exhaust gas is provided, but it is needless to say that the present invention is not limited to one layer. For example, when the height of one layer is low, a honeycomb structure on the high temperature side may be formed from a honeycomb structure having two or more layers and a low porosity.
【0027】[0027]
【発明の効果】以上の説明から明らかなように、本発明
によれば、高温側のハニカム構造体の気孔率を、低温側
のハニカム構造体の気孔率よりも低くするとともに、両
者を同一素材から構成してるため、高温の排ガスに対し
ても破壊せず効率よく熱交換を行うことができるハニカ
ム状蓄熱体を得ることができる。また、アルミニウムチ
タネートのような高価な材料を使用する必要がなく、ま
たその場合気孔率を焼成温度を変えることで制御できる
ため、低コストで上記ハニカム状蓄熱体を得ることがで
きる。As is apparent from the above description, according to the present invention, the porosity of the honeycomb structure on the high-temperature side is made lower than the porosity of the honeycomb structure on the low-temperature side, and both are made of the same material. Therefore, it is possible to obtain a honeycomb-shaped regenerator capable of efficiently exchanging heat without breaking even high-temperature exhaust gas. In addition, it is not necessary to use an expensive material such as aluminum titanate, and in that case, the porosity can be controlled by changing the firing temperature, so that the honeycomb-shaped heat storage body can be obtained at low cost.
【図1】本発明のハニカム状蓄熱体の一例の構成を示す
図である。FIG. 1 is a diagram showing a configuration of an example of a honeycomb heat storage body of the present invention.
【図2】本発明のハニカム状蓄熱体の他の例の構成を示
す図である。FIG. 2 is a diagram showing a configuration of another example of the honeycomb heat storage body of the present invention.
【図3】本発明のハニカム状蓄熱体を使用した熱交換体
を燃焼加熱炉の燃焼室に設置した例を示図である。FIG. 3 is a diagram showing an example in which a heat exchanger using the honeycomb-shaped regenerator of the present invention is installed in a combustion chamber of a combustion heating furnace.
1、11、22−1、22−2 ハニカム状蓄熱体、
2、12、 ハニカム構造体、3 貫通孔、23−1、
23−2 熱交換体、24−1、24−2 燃料投入口1, 11, 22-1, 22-2 honeycomb-shaped regenerator,
2, 12, honeycomb structure, 3 through-hole, 23-1,
23-2 heat exchanger, 24-1, 24-2 fuel inlet
Claims (5)
貫通孔から構成される流路に排ガスと被加熱ガスとを交
互に通過させて排ガス中の廃熱を回収するハニカム状蓄
熱体において、少なくとも高温の排ガスに接する高温側
のハニカム構造体の気孔率が、それ以外の低温側のハニ
カム構造体の気孔率よりも低く、前記高温側のハニカム
構造体と低温側のハニカム構造体とが同一素材からなる
ことを特徴とするハニカム状蓄熱体。1. A plurality of honeycomb structures are stacked,
The porosity of the honeycomb structure on the high-temperature side at least in contact with the high-temperature exhaust gas in the honeycomb-shaped regenerator for recovering waste heat in the exhaust gas by alternately passing the exhaust gas and the gas to be heated through the flow path composed of the through-holes However, the porosity of the other honeycomb structure on the low temperature side is lower than that of the other honeycomb structure, and the honeycomb structure on the high temperature side and the honeycomb structure on the low temperature side are made of the same material.
と接する面上にコージェライトまたはムライトからなる
ハニカム構造体からなる層を設けた請求項1記載のハニ
カム状蓄熱体。2. The honeycomb regenerator according to claim 1, wherein a layer made of a honeycomb structure made of cordierite or mullite is provided on a surface of the honeycomb structure on the low temperature side in contact with the gas to be heated.
それ以外の低温側のハニカム構造体の開口率よりも大き
い請求項1または2記載のハニカム状蓄熱体。3. An opening ratio of the high-temperature-side honeycomb structure is as follows:
The honeycomb-shaped heat storage body according to claim 1 or 2, wherein the opening ratio of the other honeycomb structure on the low temperature side is larger than that of the honeycomb structure.
それ以外の低温側のハニカム構造体の気孔率とを、同一
原料系からなる焼成前のハニカム構造体の焼成温度を変
更することで制御する請求項2または3記載のハニカム
状蓄熱体。4. The porosity of the honeycomb structure on the high temperature side;
The honeycomb heat storage body according to claim 2 or 3, wherein the porosity of the other honeycomb structure on the low temperature side is controlled by changing the firing temperature of the honeycomb structure made of the same raw material before firing.
化物である請求項1〜4のいずれか1項に記載のハニカ
ム状蓄熱体。5. The honeycomb heat storage body according to claim 1, wherein a main component of the honeycomb structure is a single metal oxide.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18494997A JP3694150B2 (en) | 1997-07-10 | 1997-07-10 | Honeycomb heat storage |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18494997A JP3694150B2 (en) | 1997-07-10 | 1997-07-10 | Honeycomb heat storage |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH1130491A true JPH1130491A (en) | 1999-02-02 |
| JP3694150B2 JP3694150B2 (en) | 2005-09-14 |
Family
ID=16162182
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP18494997A Expired - Fee Related JP3694150B2 (en) | 1997-07-10 | 1997-07-10 | Honeycomb heat storage |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3694150B2 (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2002023113A1 (en) * | 2000-09-13 | 2002-03-21 | Nkk Corporation | Regenerative heat reservoir for combustion burner |
| WO2002026655A1 (en) * | 2000-09-26 | 2002-04-04 | Ngk Insulators, Ltd. | Alumina honeycomb structure, method for manufacture of the same, and heat-storing honeycomb structure using the same |
| JP2003021482A (en) * | 2001-07-03 | 2003-01-24 | Kobayashi Pharmaceut Co Ltd | Heat reservoir and warm pad having the same |
| WO2003083397A1 (en) * | 2002-03-28 | 2003-10-09 | Ngk Insulators, Ltd. | Honeycomb heat reservoir, heat storage burner using the heat reservoir, heating furnace, and heating method |
| WO2016032095A1 (en) * | 2014-08-27 | 2016-03-03 | 부산대학교 산학협력단 | Counter-flow heat exchanger and heat exchanger assembly comprising same |
-
1997
- 1997-07-10 JP JP18494997A patent/JP3694150B2/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2002023113A1 (en) * | 2000-09-13 | 2002-03-21 | Nkk Corporation | Regenerative heat reservoir for combustion burner |
| US6547555B2 (en) | 2000-09-13 | 2003-04-15 | Nkk Corporation | Regenerative heat sensor reservoir for combustion burner |
| WO2002026655A1 (en) * | 2000-09-26 | 2002-04-04 | Ngk Insulators, Ltd. | Alumina honeycomb structure, method for manufacture of the same, and heat-storing honeycomb structure using the same |
| JP2003021482A (en) * | 2001-07-03 | 2003-01-24 | Kobayashi Pharmaceut Co Ltd | Heat reservoir and warm pad having the same |
| WO2003083397A1 (en) * | 2002-03-28 | 2003-10-09 | Ngk Insulators, Ltd. | Honeycomb heat reservoir, heat storage burner using the heat reservoir, heating furnace, and heating method |
| WO2016032095A1 (en) * | 2014-08-27 | 2016-03-03 | 부산대학교 산학협력단 | Counter-flow heat exchanger and heat exchanger assembly comprising same |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3694150B2 (en) | 2005-09-14 |
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