JPH0979525A - Heat storage material for regenerative burner - Google Patents
Heat storage material for regenerative burnerInfo
- Publication number
- JPH0979525A JPH0979525A JP23546495A JP23546495A JPH0979525A JP H0979525 A JPH0979525 A JP H0979525A JP 23546495 A JP23546495 A JP 23546495A JP 23546495 A JP23546495 A JP 23546495A JP H0979525 A JPH0979525 A JP H0979525A
- Authority
- JP
- Japan
- Prior art keywords
- heat storage
- exhaust gas
- storage body
- ceramic layer
- volume
- 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
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D17/00—Regenerative heat-exchange apparatus in which a stationary intermediate heat-transfer medium or body is contacted successively by each heat-exchange medium, e.g. using granular particles
- F28D17/02—Regenerative heat-exchange apparatus in which a stationary intermediate heat-transfer medium or body is contacted successively by each heat-exchange medium, e.g. using granular particles using rigid bodies, e.g. of porous material
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、蓄熱式バーナーの
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 heat storage body of a heat storage type burner.
【0002】[0002]
【従来の技術】鋳造後のスラブ(鋼片)、ビレット(条
鋼)、ブルーム等を加熱炉へ装入し、熱間圧延に好適な
温度に加熱するものであるが、このような加熱炉におい
ては、一般に予熱帯、加熱帯及び均熱帯から構成され、
スラブ等の被加熱材は、順次予熱帯、加熱帯及び均熱帯
を連続的に移動させて加熱するものであり、また加熱効
率を向上させるため、蓄熱式バーナーを加熱炉の被加熱
材進行方向両側に対向してバーナー群を配設し、一側の
バーナー群は蓄熱体を通して燃焼用空気を昇熱してバー
ナーへ供給して燃料を燃焼し、他側のバーナー群は燃焼
を停止して、蓄熱体を通して炉内の燃焼排ガスを排気し
排ガス中の熱エネルギーを蓄熱する。このように燃焼と
蓄熱を交互に行う、いわゆる蓄熱型交番燃焼によって連
続的に加熱することが特開平5−118764号公報、
特開平6−194054号公報に開示されている。この
ような蓄熱式バーナーに付設されている蓄熱体は、セラ
ミック製の塊状物で構成しているか、または小容積で大
容量蓄熱ができるメタル(金属製)担体で構成されてい
るのが通例である。2. Description of the Related Art A slab (steel slab), billet (bar steel), bloom, etc. after casting is charged into a heating furnace and heated to a temperature suitable for hot rolling. Is generally composed of pre-tropics, heating zones and soaking zones,
Materials to be heated such as slabs are heated by sequentially moving the pre-tropical zone, heating zone and soaking zone in order to improve the heating efficiency. The burner groups are arranged facing each other, the one side burner group heats the combustion air through the heat storage body and supplies it to the burner to burn the fuel, and the other side burner group stops the combustion. The combustion exhaust gas in the furnace is exhausted through the heat storage body to store heat energy in the exhaust gas. As described above, continuous heating is performed by so-called heat storage type alternating combustion in which combustion and heat storage are alternately performed.
It is disclosed in Japanese Patent Laid-Open No. 6-194054. The heat storage body attached to such a heat storage type burner is usually composed of a lump made of ceramics or a metal (metal) carrier capable of storing a large amount of heat in a small volume. is there.
【0003】[0003]
【発明が解決しようとする課題】上記のごとき鋼片等被
加熱材の加熱においては、被加熱材に付着している鉄
粉、酸化物粉、炉壁(煉瓦)粉等が蓄熱式バーナーの蓄
熱時における排ガス吸引に際し、排ガスとともに蓄熱体
を構成している金属製蓄熱体へ吸引され、金属製蓄熱体
に目詰りが発生して金属製蓄熱体(蓄熱体)の一部分に
排ガスが接触通過することができず、従って蓄熱体への
蓄熱量が低下し、蓄熱式バーナーの燃焼時に燃焼用空気
を十分に予熱することが困難になり、燃焼温度の低下を
燃料増加によって補うことから熱効率が低下して燃料原
単位を悪化することになる。また、蓄熱体の寿命が短命
になりコストが高くなる、しかも蓄熱体の取り替えによ
る加熱炉の停止により生産性が低下する。更に、蓄熱時
には高温排ガスに接触するため、耐久性の向上が要求さ
れている等の課題がある。本発明は、このような課題を
有利に解決するためなされたものであり、蓄熱体の目詰
りを確実に防止して、金属製蓄熱体の蓄熱機能を向上す
るとともに、高耐久性を有する蓄熱式バーナーの蓄熱体
を提供することを目的とするものである。In heating a material to be heated such as a steel piece as described above, iron powder, oxide powder, furnace wall (brick) powder, etc., adhering to the material to be heated is a regenerative burner. When exhaust gas is sucked during heat storage, it is sucked together with the exhaust gas by the metal heat storage body that constitutes the heat storage body, and clogging occurs in the metal heat storage body, causing the exhaust gas to pass through a portion of the metal heat storage body (heat storage body). Therefore, the amount of heat stored in the heat storage body decreases, and it becomes difficult to preheat combustion air sufficiently during combustion of the regenerative burner. It will decrease and worsen the fuel consumption rate. In addition, the life of the heat storage body becomes short and the cost becomes high, and the productivity is lowered due to the stop of the heating furnace due to the replacement of the heat storage body. Further, there is a problem that the durability is required to be improved because it contacts high temperature exhaust gas during heat storage. The present invention has been made in order to advantageously solve such a problem, reliably prevents clogging of the heat storage body, improves the heat storage function of the metal heat storage body, heat storage having high durability. The purpose of the present invention is to provide a heat storage body of a rotary burner.
【0004】[0004]
【課題を解決するための手段】本発明の特徴とするとこ
ろは、小容積金属製蓄熱体の排ガス入側に大容積粗粒セ
ラミック層を配設し、その上層に細粒セラミック層を配
設したことを特徴とする蓄熱式バーナーの蓄熱体であ
る。The feature of the present invention resides in that a large-volume coarse-grained ceramic layer is provided on the exhaust gas inlet side of a small-volume metal heat storage body, and a fine-grained ceramic layer is provided thereon. It is a heat storage body of a heat storage type burner characterized by doing.
【0005】[0005]
【発明の実施の形態】蓄熱式バーナーの蓄熱体は、前記
のごとく蓄熱時に加熱炉内の排ガスを吸引して排ガス顕
熱を蓄熱するものであり、ほぼ常時高温の排ガスに接触
していることから耐久性を向上することが要求されるも
のである。一方蓄熱体には、より高温排ガスの接触によ
り高効率で蓄熱することが試みられている。例えば加熱
炉の予熱炉に蓄熱式バーナーを配設し、蓄熱型交番燃焼
加熱を施す、加熱帯及び均熱帯には蓄熱帯を付設しない
通常バーナーを配設して操業するに際し、予熱帯の燃焼
側蓄熱式バーナーへ供給する燃焼用空気供給量を常時蓄
熱式バーナー容量の最大値近傍とし、燃焼負荷が減少し
たときは燃焼空気比を増加し、逆に燃焼負荷を増大した
ときは、燃焼空気比を減少して燃焼排ガス量を常時ほぼ
一定とする。一方蓄熱側蓄熱式バーナーの蓄熱体へ蓄熱
するための排ガス吸引量も蓄熱体の最大容量(蓄熱式バ
ーナーの最大容量)を吸引して蓄熱する。このように燃
焼負荷が減少したとき、燃焼空気比を増加して排ガス量
を増加することによって、燃焼側蓄熱式バーナーの燃焼
負荷が減少したときも燃焼負荷の増大(バーナー容量の
最大値近傍)時とほぼ同一にする。従って燃焼負荷が減
少したときは、燃焼空気比の増加によって増量した、排
ガスに加熱帯及び均熱帯からの流入した高温排ガスと混
合して蓄熱側蓄熱式バーナーへ吸引し、高効率で蓄熱す
ることを本発明者等が開発した。BEST MODE FOR CARRYING OUT THE INVENTION As described above, the heat storage body of the heat storage type burner sucks the exhaust gas in the heating furnace to store the sensible heat of the exhaust gas during the heat storage, and is always in contact with the high temperature exhaust gas. Therefore, it is required to improve durability. On the other hand, it has been attempted to store heat with high efficiency in a heat storage body by contacting higher temperature exhaust gas. For example, a regenerative burner is installed in the preheating furnace of the heating furnace to perform regenerative alternating combustion heating, and a normal burner that does not have a tropical heat storage is provided in the heating zone and the soaking zone. The amount of combustion air supplied to the side heat storage burner is set near the maximum value of the constant heat storage burner capacity, and the combustion air ratio is increased when the combustion load decreases, and conversely when the combustion load increases. The ratio is reduced so that the amount of combustion exhaust gas is almost constant at all times. On the other hand, the exhaust gas suction amount for storing heat to the heat storage body of the heat storage side heat storage type burner also sucks the maximum capacity of the heat storage body (maximum capacity of the heat storage type burner) to store heat. When the combustion load decreases in this way, the combustion air ratio is increased to increase the amount of exhaust gas, so that the combustion load increases even when the combustion load of the combustion side regenerative burner decreases (near the maximum burner capacity). Make it almost the same as time. Therefore, when the combustion load decreases, mix with the exhaust gas that has increased due to the increase in the combustion air ratio and the hot exhaust gas that has flowed in from the heating zone and the soaking zone, and suck it into the heat storage side regenerative burner to store heat with high efficiency. Were developed by the present inventors.
【0006】このような蓄熱式バーナーの蓄熱において
は、高温排ガスが直接金属製蓄熱体に接触通過すると、
金属製蓄熱体の耐熱限度を越え耐久性を低下させるおそ
れがあるので、本発明においては金属製蓄熱体の排ガス
入側に配設する大容積の粗粒セラミック層によって若干
排ガスの顕熱を抜熱した後、小容積で大容量蓄熱ができ
る金属製蓄熱体を通して大容量蓄熱をする。即ち、大容
積の粗粒セラミック層の機能としては、高温排ガスから
の金属製蓄熱体を保護するものである。この他、燃焼時
には、粗粒セラミック層に若干蓄熱した顕熱により、金
属製蓄熱体の蓄熱とともに、燃焼用空気の予熱に寄与さ
せるものである。In the heat storage of such a heat storage type burner, when the high temperature exhaust gas directly passes through the metal heat storage body,
Since there is a risk of exceeding the heat resistance limit of the metallic heat storage body and lowering the durability, in the present invention, the sensible heat of the exhaust gas is slightly removed by the large-volume coarse-grained ceramic layer arranged on the exhaust gas inlet side of the metal heat storage body. After heating, a large amount of heat is stored through a metal heat storage body that can store a large amount of heat in a small volume. That is, the function of the large-volume coarse-grained ceramic layer is to protect the metallic heat storage body from the high-temperature exhaust gas. In addition, at the time of combustion, the sensible heat slightly stored in the coarse-grained ceramic layer contributes to the heat storage of the metal heat storage body and the preheating of the combustion air.
【0007】次に、粗粒セラミック層の容積としては、
金属製蓄熱体容積より大容積とする、即ちセラミック
は、メタル(金属製蓄熱体)より熱伝導性が低く、かつ
蓄熱量も小さいので排ガス顕熱の抜熱量が小さいので、
金属製蓄熱体の耐熱温度を越えない温度に高温排ガスの
顕熱を抜熱するためには、金属製蓄熱体容積より粗粒セ
ラミック層を大容積に構成することが必要である。しか
して具体的には、前記のごとき粒径であれば、排ガス温
度によって若干異なるが金属製蓄熱体容積1:粗粒セラ
ミック層容積2〜3.5で確実に金属製蓄熱体を上記の
ごとく、高温排ガスから保護することができる。また、
蓄熱体を構成している金属製蓄熱体の排ガス入側に配設
する大容積粗粒セラミックの粒径としてはφ10〜φ2
0mmで十分である。Next, as the volume of the coarse grain ceramic layer,
The volume is larger than the volume of the metal heat storage body, that is, the ceramic has a lower thermal conductivity than the metal (metal heat storage body) and the heat storage amount is small, so that the sensible heat of the exhaust gas is removed little,
In order to remove the sensible heat of the high-temperature exhaust gas to a temperature that does not exceed the heat resistant temperature of the metal heat storage body, it is necessary to configure the coarse-grained ceramic layer to have a larger volume than the metal heat storage body volume. However, specifically, if the particle size is as described above, the metallic heat storage body volume 1: the coarse-grained ceramic layer volume 2 to 3.5 is surely used as the metal heat storage body as described above, though it slightly varies depending on the exhaust gas temperature. , Can be protected from high temperature exhaust gas. Also,
The particle size of the large-volume coarse-grained ceramics arranged on the exhaust gas inlet side of the metal heat storage body constituting the heat storage body is φ10 to φ2.
0 mm is sufficient.
【0008】このような大容積粗粒セラミック層の上層
に配設する細粒セラミックの粒径としては、粒径φ3〜
φ9mmが適当である。即ち、細粒セラミックの機能と
しては、排ガス中に含まれる鉄粉等のダストを捕捉する
ものであり、上記のごとき粒径で、層厚10〜100m
mで確実にダストを捕捉することができる。The particle size of the fine-grained ceramics arranged in the upper layer of such a large-volume coarse-grained ceramic layer is as follows:
φ9 mm is suitable. That is, the function of the fine-grained ceramics is to capture dust such as iron powder contained in the exhaust gas. With the above-mentioned grain size, the layer thickness is 10 to 100 m.
The dust can be reliably captured with m.
【0009】[0009]
【実施例】次に、本発明の実施例を図面により説明す
る。図1において、金属製蓄熱体1の排ガス入側Aに金
属製蓄熱体(メタル担体)1容積より、大容積の粗粒セ
ラミック層2を配設し、その上部に細粒セラミック層3
を配設して蓄熱体4を構成する。かくして燃焼時は、蓄
熱体4の排ガス出側Bから燃焼用空気を供給し、金属製
蓄熱体1及び粗粒セラミック層2から蓄熱した顕熱を抜
熱して予熱し、バーナー5先端部へ供給する、同時にバ
ーナー5へ燃料(コークス炉発生ガス等)を供給して燃
焼し、加熱炉6内を加熱して被加熱材(図示せず)を加
熱する。一方蓄熱時は、他方の蓄熱式バーナー(図示せ
ず)が同様に燃焼加熱する際に発生する高温排ガスを蓄
熱体4の排ガス入側Aから吸引して、排ガス中のダスト
を細粒セラミック層3で捕捉し、粗粒セラミック層2で
金属製蓄熱体1の耐熱温度未満に抜熱した後、金属製蓄
熱体1を通過させて金属製蓄熱体1で大容量蓄熱して排
気する。Embodiments of the present invention will now be described with reference to the drawings. In FIG. 1, on the exhaust gas inlet side A of the metal heat storage body 1, a coarse grain ceramic layer 2 having a volume larger than the volume of the metal heat storage body (metal carrier) 1 is arranged, and a fine grain ceramic layer 3 is provided on the upper side thereof.
Is arranged to form the heat storage body 4. Thus, at the time of combustion, combustion air is supplied from the exhaust gas outlet side B of the heat storage body 4, and the sensible heat stored from the metal heat storage body 1 and the coarse grain ceramic layer 2 is removed and preheated to be supplied to the tip of the burner 5. At the same time, fuel (gas generated in the coke oven, etc.) is supplied to the burner 5 and burned, and the inside of the heating furnace 6 is heated to heat a material to be heated (not shown). On the other hand, at the time of heat storage, the high temperature exhaust gas generated when the other heat storage type burner (not shown) is similarly burnt and heated is sucked from the exhaust gas inlet side A of the heat storage body 4 to remove dust in the exhaust gas into the fine grain ceramic layer. After being captured by 3, the coarse-grained ceramic layer 2 removes heat to a temperature lower than the heat resistant temperature of the metal heat storage body 1, the metal heat storage body 1 is allowed to pass through, and the metal heat storage body 1 stores a large amount of heat and exhausts the heat.
【0010】[0010]
【発明の効果】本発明によれば、排ガス中のダストを捕
捉して金属製蓄熱体の目詰りを防止し、金属製蓄熱体の
耐久性を維持することができ、かつ蓄熱体(金属製蓄熱
体)の熱効率も向上することができる。また金属製蓄熱
体の耐熱温度超の排ガスとの接触を防ぎ、金属製蓄熱体
の耐久性を向上しつつ高熱効率で蓄熱することができる
等の優れた効果が得られる。According to the present invention, the dust in the exhaust gas can be captured to prevent clogging of the metal regenerator, and the durability of the metal regenerator can be maintained. The thermal efficiency of the heat storage body) can also be improved. Further, it is possible to obtain excellent effects such as preventing contact of the metal heat storage body with exhaust gas having a temperature higher than the heat resistant temperature, and improving the durability of the metal heat storage body while storing heat with high thermal efficiency.
【図1】本発明の実施例を示す要部断面図である。FIG. 1 is a sectional view of an essential part showing an embodiment of the present invention.
1 金属製蓄熱体 2 粗粒セラミック層 3 細粒セラミック層 4 蓄熱体 1 Metal heat storage body 2 Coarse grain ceramic layer 3 Fine grain ceramic layer 4 Heat storage body
Claims (1)
積粗粒セラミック層を配設し、その上層に細粒セラミッ
ク層を配設したことを特徴とする蓄熱式バーナーの蓄熱
体。1. A regenerator for a regenerative burner, characterized in that a large volume coarse grain ceramic layer is disposed on the exhaust gas inlet side of a small volume metal regenerator, and a fine grain ceramic layer is disposed on top of it.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23546495A JP3340287B2 (en) | 1995-09-13 | 1995-09-13 | Thermal storage of thermal storage burner |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23546495A JP3340287B2 (en) | 1995-09-13 | 1995-09-13 | Thermal storage of thermal storage burner |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0979525A true JPH0979525A (en) | 1997-03-28 |
JP3340287B2 JP3340287B2 (en) | 2002-11-05 |
Family
ID=16986485
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP23546495A Expired - Fee Related JP3340287B2 (en) | 1995-09-13 | 1995-09-13 | Thermal storage of thermal storage burner |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3340287B2 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1126217A1 (en) * | 1999-09-01 | 2001-08-22 | Nkk Corporation | Heat treating plant, installation method for porous regenerative element, production method for heat treated substance, selection method for porous regenerative element, and spent porous regenerative element component member |
US7946844B2 (en) * | 2007-03-19 | 2011-05-24 | Ngk Insulators, Ltd. | Heat accumulating-type burner |
JPWO2016076035A1 (en) * | 2014-11-10 | 2017-08-17 | 日本碍子株式会社 | Container for storing heat storage material |
-
1995
- 1995-09-13 JP JP23546495A patent/JP3340287B2/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1126217A1 (en) * | 1999-09-01 | 2001-08-22 | Nkk Corporation | Heat treating plant, installation method for porous regenerative element, production method for heat treated substance, selection method for porous regenerative element, and spent porous regenerative element component member |
EP1126217A4 (en) * | 1999-09-01 | 2002-11-20 | Nippon Kokan Kk | Heat treating plant, installation method for porous regenerative element, production method for heat treated substance, selection method for porous regenerative element, and spent porous regenerative element component member |
KR100681575B1 (en) * | 1999-09-01 | 2007-02-09 | 제이에프이 엔지니어링 가부시키가이샤 | Heat treating plant, installation method for porous regenerative element, production method for heat treated substance, selection method for porous regenerative element, and spent porous regenerative element component member |
US7946844B2 (en) * | 2007-03-19 | 2011-05-24 | Ngk Insulators, Ltd. | Heat accumulating-type burner |
JPWO2016076035A1 (en) * | 2014-11-10 | 2017-08-17 | 日本碍子株式会社 | Container for storing heat storage material |
Also Published As
Publication number | Publication date |
---|---|
JP3340287B2 (en) | 2002-11-05 |
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