JPS6252201B2 - - Google Patents

Info

Publication number
JPS6252201B2
JPS6252201B2 JP53116573A JP11657378A JPS6252201B2 JP S6252201 B2 JPS6252201 B2 JP S6252201B2 JP 53116573 A JP53116573 A JP 53116573A JP 11657378 A JP11657378 A JP 11657378A JP S6252201 B2 JPS6252201 B2 JP S6252201B2
Authority
JP
Japan
Prior art keywords
heat transfer
heating furnace
flow rate
burner
transfer tube
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.)
Expired
Application number
JP53116573A
Other languages
Japanese (ja)
Other versions
JPS5543342A (en
Inventor
Mitsuo Imamura
Eiji Yamaguchi
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Power Ltd
Original Assignee
Babcock Hitachi KK
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 Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP11657378A priority Critical patent/JPS5543342A/en
Publication of JPS5543342A publication Critical patent/JPS5543342A/en
Publication of JPS6252201B2 publication Critical patent/JPS6252201B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明は、加熱炉に係り、特に炉内に設置され
た伝熱管内を流れる流体の温度調節装置に関す
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a heating furnace, and more particularly to a temperature control device for a fluid flowing through heat transfer tubes installed in the furnace.

加熱炉において、複数の流体の温度調節が必要
な場合、一つの流体温度は燃焼装置における燃焼
容量を増減させることで調節できるが、他の流体
温度の調節は燃焼容量の増減では不可能である。
このような場合の温度調節として、従来は第1図
に示すような手段がとられていた。
When it is necessary to adjust the temperature of multiple fluids in a heating furnace, the temperature of one fluid can be adjusted by increasing or decreasing the combustion capacity in the combustion device, but the temperature of other fluids cannot be adjusted by increasing or decreasing the combustion capacity. .
In order to control the temperature in such a case, the conventional method shown in FIG. 1 has been taken.

すなわち、加熱炉本体1の下方に燃料配管2を
接続したバーナ3が設置され、上方にはダンパ4
を内装した排気筒5が形成されている。炉内の上
側には伝熱管6が下側には伝熱管7がそれぞれ配
管されており、それぞれの伝熱管6,7内を流れ
る流体は、バーナ3の燃焼によつて加熱されたの
ち炉外に取出される。
That is, a burner 3 to which a fuel pipe 2 is connected is installed below the heating furnace main body 1, and a damper 4 is installed above.
An exhaust pipe 5 is formed in which the exhaust pipe 5 is equipped. Heat exchanger tubes 6 and 7 are installed at the upper and lower sides of the furnace, respectively, and the fluid flowing through each of the heat exchanger tubes 6 and 7 is heated by combustion in the burner 3 and then flows outside the furnace. is taken out.

バーナ3側に配設された伝熱管7を流れる流体
は、その出口温度を検出して、燃料配管2に付設
された燃料調節弁8で燃焼容量を調節することに
よつて温度調節される。一方、バーナ3より離れ
た所に配管されている伝熱管6を通して流れる流
体は、バイパス配管9に付設された流体調節弁1
0を操作し、バイパス配管9を流れる未加熱の流
体を、炉内を通つて加熱された高温流体に混合し
て流体の温度調整を行なつていた。
The temperature of the fluid flowing through the heat transfer tube 7 disposed on the burner 3 side is adjusted by detecting its outlet temperature and adjusting the combustion capacity with a fuel control valve 8 attached to the fuel pipe 2. On the other hand, the fluid flowing through the heat transfer tube 6 which is piped away from the burner 3 is controlled by the fluid control valve 1 attached to the bypass pipe 9.
0, the unheated fluid flowing through the bypass pipe 9 was mixed with the high-temperature fluid heated through the furnace to adjust the temperature of the fluid.

ところがこのような手段では、バイパス管9を
流れる流体と炉内を通つて出て来た流体とではか
なりの温度差があるため、伝熱管6のバイパス管
9と接合している部分に局部的な熱衝撃や熱応力
が生じ、そのため伝熱管6の耐用寿命が短かかつ
たり、また伝熱管6の損傷によつて事故を招来す
ることがある。更に上記のものでは構造が複雑
で、メンテナンス上からも問題があつた。
However, with such means, there is a considerable temperature difference between the fluid flowing through the bypass pipe 9 and the fluid coming out through the furnace, so there is a local temperature difference in the part of the heat transfer tube 6 that joins the bypass pipe 9. A thermal shock or thermal stress occurs, which may shorten the useful life of the heat exchanger tubes 6 or cause an accident due to damage to the heat exchanger tubes 6. Furthermore, the above-mentioned structure was complicated and caused problems in terms of maintenance.

本発明の目的は、上記した従来技術の欠点を除
去し、流体の温度調節が容易で、しかも調節可能
な温度範囲が拡張でき、伝熱管に損傷などを生じ
ない加熱炉の流体温度調節装置を提供するにあ
る。
An object of the present invention is to provide a fluid temperature control device for a heating furnace that eliminates the above-mentioned drawbacks of the prior art, allows easy fluid temperature control, expands the adjustable temperature range, and does not cause damage to heat transfer tubes. It is on offer.

この目的を達成するため、本発明は、加熱炉本
体と、その加熱炉本体の所定位置に設置されたバ
ーナと、加熱炉本体に連通した排気筒と、加熱炉
本体内の前記バーナから離れた個所に配置されバ
ーナ火炎からのふく射熱をほぼ遮蔽して炉壁との
間に対流伝熱部を区画形成する例えば筒状のふく
射熱遮蔽体と、その対流伝熱部を流れる燃焼ガス
の流量を調整するガス量調整手段と、前記バーナ
からのふく射熱によつて加熱される燃焼ガス流れ
方向上流側の第1の伝熱管と、前記対流伝熱部に
配置され対流伝熱によつて加熱される燃焼ガス流
れ方向下流側の第2の伝熱管とを備える。
To achieve this objective, the present invention provides a heating furnace body, a burner installed at a predetermined position in the heating furnace body, an exhaust pipe communicating with the heating furnace body, and a burner located in the heating furnace body away from the burner. For example, a cylindrical radiation heat shield is placed at a location to block most of the radiant heat from the burner flame and form a convection heat transfer section between it and the furnace wall, and the flow rate of combustion gas flowing through the convection heat transfer section is adjusted. a first heat transfer tube on the upstream side in the flow direction of the combustion gas heated by radiated heat from the burner; and a combustion tube disposed in the convection heat transfer section and heated by convection heat transfer. and a second heat transfer tube on the downstream side in the gas flow direction.

そして、前記ガス流量調整手段によつて対流伝
熱部のガス流量を調整することにより、前記第2
の伝熱管内を流れる流体温度を前記第1の伝熱管
とは別に調整できるように構成されていることを
特徴とするものである。
Then, by adjusting the gas flow rate of the convection heat transfer section by the gas flow rate adjustment means, the second
The heat exchanger tube is characterized in that the temperature of the fluid flowing inside the heat exchanger tube can be adjusted separately from that of the first heat exchanger tube.

以下、本発明の実施例を第2図とともに説明す
る。
Embodiments of the present invention will be described below with reference to FIG.

伝熱管7は従来と同様にバーナ3の近くに設置
され、伝熱管7を流れる流体は、その出口温度を
検出して、燃料配管2に付設された燃料調節弁8
で燃焼容量を調節することによつて温度調節され
る。バーナ3から出る燃焼ガスの流路でバーナ3
から離れた箇所(図面ではバーナ3の上方)に、
流量調整筒体11が設置されている。流量調整筒
体11は両端に開口12,12を有し、一方の開
口12にダンパなどからなる流量可変部13が設
けられ、流量可変部13によつて筒内14を通過
する燃焼ガスの量が調整できる。流量調整筒体1
1は加熱炉本体1の炉壁15から所定の間隔をお
いて固定されており、流量調整筒体11と炉壁1
5の間にバーナ3からの火炎ふく射熱17をほぼ
遮蔽して対流伝熱部16が区画形成されて、この
対流伝熱部16に伝熱管6が流量調整筒体11を
取り囲むように巻装配置されている。従つて伝熱
管6は流量調整筒体11と並列に配置され、また
流量調整筒体11及び対流伝熱部16は共に排気
筒5に連通している。
The heat transfer tube 7 is installed near the burner 3 as in the conventional case, and the outlet temperature of the fluid flowing through the heat transfer tube 7 is detected and the fuel control valve 8 attached to the fuel pipe 2 is operated.
The temperature is regulated by adjusting the combustion capacity. Burner 3 in the flow path of combustion gas coming out of burner 3
(above burner 3 in the drawing),
A flow rate adjusting cylinder 11 is installed. The flow rate adjusting cylinder 11 has openings 12, 12 at both ends, and a flow rate variable part 13 consisting of a damper or the like is provided in one of the openings 12, and the flow rate variable part 13 controls the amount of combustion gas passing through the cylinder interior 14. can be adjusted. Flow rate adjustment cylinder 1
1 is fixed at a predetermined distance from the furnace wall 15 of the heating furnace body 1, and connects the flow rate adjusting cylinder 11 and the furnace wall 1.
5, a convection heat transfer section 16 is formed by substantially shielding the flame radiation heat 17 from the burner 3, and a heat transfer tube 6 is wound around the convection heat transfer section 16 so as to surround the flow rate adjusting cylinder 11. has been done. Therefore, the heat transfer tube 6 is arranged in parallel with the flow rate adjustment cylinder 11, and both the flow rate adjustment cylinder 11 and the convection heat transfer section 16 communicate with the exhaust pipe 5.

伝熱管6を流れる流体の温度調節は、その出口
温度を検出して、流量調整筒体11により間接的
に対流伝熱部16を流れる燃焼ガスの流量を調節
することによつて行なわれる。すなわち、流量調
整筒体11の流量可変部13を開くと筒内14を
流れる燃焼ガス量が増え、それによつて対流伝熱
部16を流れる燃焼ガス量が減少し、対流伝熱割
合が減少して伝熱管6を流れる流体の温度は下が
る。流体の温度を上げる場合は、流量調整筒体1
1の流量可変部13を閉じて、対流伝熱部16を
流れる燃焼ガス量を増してやれば、対流伝熱割合
が増大して流体の温度は上昇する。このように流
量調整筒体11で燃焼ガスの流量を可変すること
によつて、伝熱管6を流れる流体の温度調節がで
きる。
The temperature of the fluid flowing through the heat transfer tube 6 is adjusted by detecting its outlet temperature and indirectly adjusting the flow rate of the combustion gas flowing through the convection heat transfer section 16 using the flow rate adjustment cylinder 11. That is, when the flow rate variable portion 13 of the flow rate adjustment cylinder 11 is opened, the amount of combustion gas flowing through the cylinder interior 14 increases, thereby reducing the amount of combustion gas flowing through the convection heat transfer portion 16, and the convection heat transfer rate decreases. As a result, the temperature of the fluid flowing through the heat transfer tubes 6 decreases. When increasing the temperature of the fluid, use the flow rate adjustment cylinder 1
If the flow rate variable section 13 of No. 1 is closed and the amount of combustion gas flowing through the convection heat transfer section 16 is increased, the convection heat transfer rate will increase and the temperature of the fluid will rise. By varying the flow rate of the combustion gas with the flow rate adjusting cylinder 11 in this way, the temperature of the fluid flowing through the heat transfer tubes 6 can be adjusted.

本発明は、丸型炉や角型炉などに適用でき、第
2図に示すような螺旋型の伝熱管だけでなく、く
し型の伝熱管、または上記の二つを組合わせた伝
熱管を用いることもできる。
The present invention can be applied to round-shaped furnaces, square-shaped furnaces, etc., and can be applied not only to spiral-shaped heat exchanger tubes as shown in Fig. 2, but also to comb-shaped heat exchanger tubes or heat exchanger tubes that are a combination of the above two. It can also be used.

上記したように本発明は、雰囲気温度が極めて
高く伝熱効率の良い火炉内に伝熱管を配置した加
熱炉に係るもので、この種の加熱炉においてバー
ナ近くに配置されている伝熱管は、バーナへの燃
料供給量を調整することによつて流体温度の調整
が容易にできる。しかしバーナから離れた個所に
配置されている伝熱管は、バーナへの燃料供給量
をコントロールしても直接に細かい流体温度の調
整は不可能である。
As described above, the present invention relates to a heating furnace in which heat transfer tubes are placed in a furnace where the ambient temperature is extremely high and heat transfer efficiency is high.In this type of heating furnace, the heat transfer tubes placed near the burner are By adjusting the amount of fuel supplied to the fluid, the fluid temperature can be easily adjusted. However, if the heat transfer tube is located far from the burner, it is impossible to directly finely adjust the fluid temperature even if the amount of fuel supplied to the burner is controlled.

そのため従来は、第1図に示すような構成で伝
熱管6の温度調整を行なつていたが、前述のよう
に種々の技術的問題点を有していた。
Conventionally, therefore, the temperature of the heat exchanger tubes 6 has been adjusted using a configuration as shown in FIG. 1, but this has had various technical problems as described above.

そこで本発明は、加熱炉本体内のバーナから離
れた位置にバーナからのふく射熱を遮蔽して炉壁
との間に温度調整が容易な対流伝熱部を区画形成
するふく射熱遮蔽体を配置し、その対流伝熱部に
第2の伝熱管を設けるとともに、該対流伝熱部を
流れる燃焼ガスの流量を調整するガス流量調整手
段を設け、そのガス流量を調整することによつて
第2の伝熱管内を流れる流体の温度を調整するも
のである。
Therefore, the present invention disposes a radiant heat shield at a position away from the burner in the heating furnace main body, which blocks radiant heat from the burner and forms a convection heat transfer section between the furnace wall and the furnace wall, where the temperature can be easily adjusted. A second heat transfer tube is provided in the convection heat transfer section, and a gas flow rate adjusting means for adjusting the flow rate of combustion gas flowing through the convection heat transfer section is provided, and the second heat transfer is achieved by adjusting the gas flow rate. It adjusts the temperature of the fluid flowing inside the heat tube.

従つて高温の燃焼ガスから効率良く伝熱がで
き、しかも細かい温度調整が容易に、かつ確実に
でき、しかも温度調節範囲が拡張される。また炉
内で温度調節できるから、従来のように伝熱管に
熱衝撃や熱応力を与えることがなく、伝熱管の耐
用寿命が延長できる。しかも構造が簡単であり、
メンテナスが容易である。
Therefore, heat can be efficiently transferred from the high-temperature combustion gas, fine temperature adjustment can be easily and reliably performed, and the temperature adjustment range can be expanded. Furthermore, since the temperature can be adjusted within the furnace, there is no need to apply thermal shock or thermal stress to the heat exchanger tubes as in conventional methods, and the service life of the heat exchanger tubes can be extended. Moreover, the structure is simple,
Easy to maintain.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は従来の加熱炉の切断正面図、第2図は
本発明の実施例に係る加熱炉の切断正面図であ
る。 1……加熱炉本体、3……バーナ、6,7……
伝熱管、11……流量調整筒体、12……開口、
13……流量可変部、14……筒内、16……対
流伝熱部、17……火炎ふく射熱。
FIG. 1 is a cutaway front view of a conventional heating furnace, and FIG. 2 is a cutaway front view of a heating furnace according to an embodiment of the present invention. 1... Heating furnace body, 3... Burner, 6, 7...
Heat exchanger tube, 11...Flow rate adjustment cylinder, 12...Opening,
13...Flow rate variable section, 14...Cylinder interior, 16...Convection heat transfer section, 17...Flame radiation heat.

Claims (1)

【特許請求の範囲】 1 加熱炉本体と、その加熱炉本体の所定位置に
設置されたバーナと、加熱炉本体に連通した排気
筒と、加熱炉本体内の前記バーナから離れた個所
に配置されバーナ火炎からのふく射熱をほぼ遮蔽
して炉壁との間に対流伝熱部を区画形成するふく
射熱遮蔽体と、その対流伝熱部を流れる燃焼ガス
の流量を調整するガス流量調整手段と、前記バー
ナからの火炎ふく射熱によつて加熱される燃焼ガ
ス流れ方向上流側の第1の伝熱管と、前記対流伝
熱部に配置され対流伝熱によつて加熱される燃焼
ガス流れ方向下流側の第2の伝熱管とを備え、 前記ガス流量調整手段によつて対流伝熱部のガ
ス流量を調整することにより、前記第2の伝熱管
内を流れる流体温度を前記第1の伝熱管とは別に
調整できるように構成されていることを特徴とす
る加熱炉。 2 特許請求の範囲第1項記載において、前記ふ
く射熱遮蔽体が両端にそれぞれ開口を有する筒体
からなり、そのふく射熱遮蔽体内に前記ガス流量
調整手段が設けられていることを特徴とする加熱
炉。 3 特許請求の範囲第1項記載において、前記ふ
く射熱遮蔽体が加熱炉本体に固定され、そのふく
射熱遮蔽体の周囲に前記第2の伝熱管が巻装支持
されていることを特徴とする加熱炉。 4 特許請求の範囲第1項記載において、前記バ
ーナに接続される燃料配管に燃料供給量調整手段
が付設され、前記第1の伝熱管内を流れる流体温
度が燃料供給量によつて調整されるように構成さ
れていることを特徴とする加熱炉。
[Scope of Claims] 1. A heating furnace body, a burner installed at a predetermined position in the heating furnace body, an exhaust pipe communicating with the heating furnace body, and a part located away from the burner in the heating furnace body. a radiant heat shield that substantially shields radiant heat from the burner flame and defines a convection heat transfer section between it and the furnace wall; a gas flow rate adjustment means that adjusts the flow rate of combustion gas flowing through the convection heat transfer section; A first heat transfer tube on the upstream side in the flow direction of the combustion gas heated by flame radiation heat from the burner, and a first heat transfer tube on the downstream side in the flow direction of the combustion gas disposed in the convection heat transfer section and heated by convective heat transfer. and a second heat transfer tube, and by adjusting the gas flow rate of the convection heat transfer section by the gas flow rate adjusting means, the temperature of the fluid flowing in the second heat transfer tube is set separately from that of the first heat transfer tube. A heating furnace configured to be adjustable. 2. The heating furnace according to claim 1, wherein the radiation heat shield is made of a cylinder having openings at both ends, and the gas flow rate adjusting means is provided within the radiation heat shield. 3. The heating furnace according to claim 1, wherein the radiation heat shield is fixed to a heating furnace main body, and the second heat transfer tube is wrapped and supported around the radiation heat shield. . 4. In claim 1, a fuel supply amount adjusting means is attached to the fuel pipe connected to the burner, and the temperature of the fluid flowing in the first heat transfer tube is adjusted by the fuel supply amount. A heating furnace characterized by being configured as follows.
JP11657378A 1978-09-25 1978-09-25 Heating furnace Granted JPS5543342A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11657378A JPS5543342A (en) 1978-09-25 1978-09-25 Heating furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11657378A JPS5543342A (en) 1978-09-25 1978-09-25 Heating furnace

Publications (2)

Publication Number Publication Date
JPS5543342A JPS5543342A (en) 1980-03-27
JPS6252201B2 true JPS6252201B2 (en) 1987-11-04

Family

ID=14690447

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11657378A Granted JPS5543342A (en) 1978-09-25 1978-09-25 Heating furnace

Country Status (1)

Country Link
JP (1) JPS5543342A (en)

Also Published As

Publication number Publication date
JPS5543342A (en) 1980-03-27

Similar Documents

Publication Publication Date Title
US6308702B1 (en) Compact high-efficiency air heater
WO1997011856A2 (en) Vehicle heater independent of the engine
JPH07208701A (en) Temperature controller for inlet gas of denitrating device for boiler
GB1527204A (en) Preheating combustion air
US4460121A (en) Thermally controlled vent damper
US1940355A (en) Furnace control
US4474229A (en) Air preheater
JPS6252201B2 (en)
US4326897A (en) Post weld heat treatment of shell and tube heat exchangers and apparatus
JP3190939B2 (en) Steam generator
US4781575A (en) Temperature compensator for pressure operated fuel regulator
JPH05203378A (en) Protector of heat pipe air heater
US4041908A (en) Super heater
US4631022A (en) Heat recuperator with compensator for pressure operated fuel regulator
JPS6116573Y2 (en)
JPS6026298Y2 (en) Heat exchanger
JPS62208564A (en) Fuel reformer of fuel cell power generating plant
JPS6011284B2 (en) Heat transfer control device for tube heating furnace
US3730166A (en) Apparatus for heating water by means of an oilburner
JPS5938684Y2 (en) instant water heater
GB1241606A (en) Improvements in or relating to a heater for fluids
BE1004412A7 (en) Water heater
JPS6249118A (en) Air preheating system
JPS61213416A (en) Gas burning apparatus
SU811050A1 (en) Blast furnace air-duct apparatus