JPS6048614B2 - Effective recovery method for blast furnace gas energy - Google Patents
Effective recovery method for blast furnace gas energyInfo
- Publication number
- JPS6048614B2 JPS6048614B2 JP1492678A JP1492678A JPS6048614B2 JP S6048614 B2 JPS6048614 B2 JP S6048614B2 JP 1492678 A JP1492678 A JP 1492678A JP 1492678 A JP1492678 A JP 1492678A JP S6048614 B2 JPS6048614 B2 JP S6048614B2
- Authority
- JP
- Japan
- Prior art keywords
- blast furnace
- exhaust gas
- gas
- expansion turbine
- turbine
- 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
Links
- 238000011084 recovery Methods 0.000 title claims description 29
- 238000000034 method Methods 0.000 title claims description 13
- 239000007789 gas Substances 0.000 claims description 72
- 239000000567 combustion gas Substances 0.000 claims description 6
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims 1
- 239000003546 flue gas Substances 0.000 claims 1
- 238000002485 combustion reaction Methods 0.000 description 21
- 238000010586 diagram Methods 0.000 description 5
- 230000005611 electricity Effects 0.000 description 4
- 241000234435 Lilium Species 0.000 description 3
- 239000000428 dust Substances 0.000 description 3
- 230000001105 regulatory effect Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000010248 power generation Methods 0.000 description 2
- 239000000571 coke Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Blast Furnaces (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Description
【発明の詳細な説明】
本発明は、高炉の炉頂ガスエネルギーを有効に回収する
方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for effectively recovering top gas energy of a blast furnace.
従来から実施されている高炉の炉頂ガスエネルギーを回
収する方法としては、たとえば、第1図に示すように、
高炉aからダストキヤツチヤを)さらにベンチユリスク
ラバーcを経てきた高炉ガスを膨張タービンeに導いて
発電する方法では、一・ −プ吉J日↓゛フに江ハ°ハ
日5−L、冷却されるため、高炉ガスの圧力のみによる
発電が主であり、したがつて、回収エネルギーも低かつ
た。As shown in Fig. 1, for example, a conventional method of recovering the top gas energy of a blast furnace is as follows.
In the method of generating electricity by guiding the blast furnace gas that has passed through the dust catcher (from the blast furnace a) and the bench lily scrubber c to the expansion turbine e, 1. Because it is cooled, power generation is mainly based on the pressure of the blast furnace gas, and therefore the energy recovered is low.
同様に第2図に示すように、一次ベンチユリスクラバー
cを出た高炉ガスの一部を燃焼器iにて燃焼させ、セプ
タム弁dおよび二次ベンチユリスクラバーfを経てきた
高炉ガスと、膨張タービンeに入る前で混合させ、これ
により高炉ガスの温度を高めて回収電力を高める方法で
は、膨張タービンeとベンチユリスクラバーれの間に燃
焼器iを特別に設置しなければならないうえ、燃焼させ
た高炉ガスの一部を混合するため、ガスホルダgに行く
高炉ガスのカロリーを低下させるので、燃焼器iで燃焼
できる量も限られ、第1図の方法よりは回収エネルギー
は高いというものの、高炉ガスの燃料価値低下等の欠点
があつた。また第3図のように、セプタム弁dの手前で
高圧の高炉ガスを抜きた七、熱風炉jで燃焼後、その排
ガスの一部を、膨張タービンeに入る前の高炉ガス本管
に導入して混合させ、高圧および高温ガスとノして回収
電力を高める方法があるが、第2図の方法と同様に、高
炉ガスカロリーを低め、しかもそのため、熱風炉排ガス
の全量は使用できないので、大部分は煙突にから捨てら
れる。さらに、この方法で、熱風炉jを経由してガスを
高炉ガス本5管に導入するためには、その間の圧力低下
を補償してやる必要があり、そのための昇圧設備および
運転に要する費用を無視するわけにはいかない。本発明
は、従来の炉頂圧回収用膨張タービンによるエネルギー
の回収に加えて、熱風炉排ガスのもつエネルギーの有効
利用を図ることができ、か 夕つ、ガスホルダーに行く
高炉ガスのカロリーを低下させないようにした高炉ガス
エネルギーの有効回収法を提供することを目的とするも
のてある。このため、本発明の構成は、炉頂圧回収用膨
張タービンを備えた高炉設備において、熱風炉の燃焼排
ガスラインに排ガスエネルギー回収用の膨張タービンを
設置するとともに該排ガスエネルギー回収用の膨張ター
ビンのラインには補助的にバイパス管およびバイパス弁
を設けておき、かつ、高炉から排出する炉頂ガスを高圧
のまま清浄化し、その一部を前記炉頂圧回収用膨張ター
ビンの手前の高圧部からとり、圧力降下最小にした状態
で前記熱風炉に導いて高圧下で燃焼させ、しかも、該燃
焼ガスのもつ高圧および高温のエネルギーを前記排ガス
エネルギー回収用の膨張タービンで回収し、該排ガスエ
ネルギー回収用の膨張タービンで膨張したのちの排ガス
を煙突に導くことを特徴としている。以下、本発明の一
実施例について、第4図を参照しながら説明する。Similarly, as shown in Fig. 2, part of the blast furnace gas that has exited the primary ventilary scrubber c is combusted in a combustor i, and the blast furnace gas that has passed through the septum valve d and the secondary ventilary scrubber f is combined with the expanded blast furnace gas. In the method of mixing the blast furnace gas before entering the turbine e, thereby raising the temperature of the blast furnace gas and increasing the recovered power, the combustor i must be specially installed between the expansion turbine e and the ventilary scrubber, and the combustion Since the calorie content of the blast furnace gas going to the gas holder g is reduced, the amount that can be burned in the combustor i is limited, and although the recovered energy is higher than the method shown in Figure 1, There were drawbacks such as a decline in the fuel value of blast furnace gas. In addition, as shown in Figure 3, the high-pressure blast furnace gas is removed before the septum valve d, and after combustion in the hot blast furnace j, a part of the exhaust gas is introduced into the blast furnace gas main pipe before entering the expansion turbine e. There is a method to increase the recovered power by mixing it with high-pressure and high-temperature gas, but like the method shown in Figure 2, it lowers the blast furnace gas calorie, and because of this, the entire amount of hot blast furnace exhaust gas cannot be used. Most of it is thrown down the chimney. Furthermore, in order to introduce gas into the 5 blast furnace gas main pipes via the hot stove j with this method, it is necessary to compensate for the pressure drop during that time, ignoring the cost of pressurizing equipment and operation. I can't afford it. In addition to recovering energy using the conventional expansion turbine for recovering furnace top pressure, the present invention makes it possible to effectively utilize the energy contained in the hot blast furnace exhaust gas, and at the same time reduce the calories of the blast furnace gas going to the gas holder. The purpose of this project is to provide an effective recovery method for blast furnace gas energy that does not cause waste. For this reason, the configuration of the present invention is such that, in blast furnace equipment equipped with an expansion turbine for top pressure recovery, an expansion turbine for exhaust gas energy recovery is installed in the combustion exhaust gas line of the hot blast furnace, and an expansion turbine for exhaust gas energy recovery is installed in the combustion exhaust gas line of the hot blast furnace. A bypass pipe and a bypass valve are auxiliary installed in the line, and the furnace top gas discharged from the blast furnace is purified at high pressure, and a part of it is sent from the high pressure section before the expansion turbine for recovering the furnace top pressure. The combustion gas is guided into the hot blast furnace with the pressure drop minimized and combusted under high pressure, and the high pressure and high temperature energy of the combustion gas is recovered by the exhaust gas energy recovery expansion turbine. The feature is that the exhaust gas is guided into the chimney after being expanded by an expansion turbine. An embodiment of the present invention will be described below with reference to FIG.
第4図において、1は高炉、2はダストキヤツチヤ、3
は一次ベンチユリスクラバー、は二次ベンチユリスクラ
バー、5は炉頂圧回収用膨張タービン、6はセプタム弁
、7は熱風炉燃焼用高炉ガスライン、8は熱風炉である
。In Figure 4, 1 is the blast furnace, 2 is the dust catcher, and 3 is the blast furnace.
5 is an expansion turbine for recovering furnace top pressure, 6 is a septum valve, 7 is a blast furnace gas line for hot blast combustion, and 8 is a hot blast furnace.
すなわち、熱風炉−燃焼用高炉ガスライン7を炉頂圧力
制御装置であるセプタム弁6の手前で接続する。一方、
熱風炉8の排ガスライン9の後に排ガスエネルギー回収
用の膨張タービン10が発電機16と同軸上に設置され
る。余剰エネルギーの利用法によつては熱3風炉8での
燃焼用空気圧縮機11を同軸上に設置することもできる
。排ガスライン9の前記タービン10の入口手前からバ
イパス管22およびバイパス弁13を補助的に設置して
、タービン10の起動および停止または非常時などに使
用する。前4t記タービン10を出た排ガスラインは前
記バイパス弁13の同ラインと合流後、煙突14に接続
される。また前記空気圧縮機11を該タービン10と同
軸上に設置するときは、該圧縮機11から燃焼用空気ラ
イン12をとおつて熱風炉8の燃焼用空気ライン20に
合流せしめ、必要に応じて切換弁19により燃焼用空気
の供給切換を行なう。なお15はガスホルダ、17は発
電機、18は遮断弁、21は調速弁である。第4図に示
すように構成された高炉ガスエネルギー回収装置におい
ては、従来のように、炉頂圧回収用膨張タービン5によ
つて発電機17が駆動され、発電することができること
は勿論であるクが、熱風炉8側に排ガスエネルギー回収
用の膨張タービン1?を設けてあるので、次のような作
用となる。That is, the hot blast furnace-combustion blast furnace gas line 7 is connected before the septum valve 6, which is the furnace top pressure control device. on the other hand,
After the exhaust gas line 9 of the hot blast stove 8, an expansion turbine 10 for exhaust gas energy recovery is installed coaxially with a generator 16. Depending on how the surplus energy is used, the air compressor 11 for combustion in the three-heat stove 8 may be installed coaxially. A bypass pipe 22 and a bypass valve 13 are auxiliary installed in the exhaust gas line 9 before the inlet of the turbine 10, and are used for starting and stopping the turbine 10, or in an emergency. The exhaust gas line exiting the turbine 10 from the previous four tons is connected to the chimney 14 after merging with the same line from the bypass valve 13 . When the air compressor 11 is installed coaxially with the turbine 10, the air compressor 11 is connected to the combustion air line 20 of the hot air stove 8 through the combustion air line 12, and switched as necessary. A valve 19 switches the supply of combustion air. Note that 15 is a gas holder, 17 is a generator, 18 is a cutoff valve, and 21 is a speed regulating valve. In the blast furnace gas energy recovery apparatus configured as shown in FIG. 4, it is of course possible to generate electricity by driving the generator 17 by the expansion turbine 5 for recovering furnace top pressure, as in the conventional case. Is there an expansion turbine 1 on the hot blast stove 8 side for exhaust gas energy recovery? Since it is provided, the following effect is obtained.
すなわち、該タービン10の停止時、熱風炉8で燃焼し
た後の排ガスは調速弁21および遮断弁18を閉じるこ
とにより、バイパス弁137を経て、さらに必要に応じ
、減圧弁を経て煙突14から排出される。該タービン駆
動時には、バイパス弁13を閉とし、遮断弁18および
調速弁21を開として、該タービン10を起動し、定常
回転後に発電機16から電力供給ラインに投入すること
で発電する。一方、熱風炉燃焼用高圧空気は、高炉ブロ
ワ(図示せず)の圧縮空気ラインからバイパスさせた燃
焼用空気ライン20からの空気を利用することもてきる
が、同図のように、排ガスエネルギー回収用タービン1
0が停止の時には上記高炉ブロワの圧縮空気を使用し、
該タービン10が定常運転に入つたら切換弁19を切換
えて、該タービン10に直結されて時駆動されている燃
焼用空気圧縮機11から燃焼用空気ライン12を経て、
圧縮空気を供給する方法もある。したがつて、第4図の
ようにすれば、排ガスエネルギー回収用の膨張タービン
10が運転に入つたのちは、炉頂圧回収タービン5と、
2基のタービンで同時発電することになる。したがつて
、本発明は、炉頂圧回収用膨張タービンを備えた高炉設
備において、熱風炉の燃焼排ガスラインに排ガスエネル
ギー回収用の膨張タービンを設置するとともに該排ガス
エネルギー回収用の膨張タービンのラインには補助的に
バイパス管およびバイパス弁を設けておき、かつ、高炉
から排出する炉頂ガスを高圧のまま清浄化し、その一部
を前記炉頂圧回収用膨張タービンの手前の高圧部からと
り、圧力降下最小にした状態で前記熱風炉に導いて高圧
下で燃焼させ、しかも、該燃焼ガスのもつ高圧および高
温のエネルギー回収用の膨張タービンで回収し、該排ガ
スエネルギー回収用の膨張タービンで膨張したのち排ガ
スを煙突に導く方法であるから、次の諸効果を奏する。That is, when the turbine 10 is stopped, the exhaust gas after being combusted in the hot air stove 8 is discharged from the chimney 14 through the bypass valve 137 and, if necessary, through the pressure reducing valve by closing the regulating valve 21 and the shutoff valve 18. be discharged. When the turbine is driven, the bypass valve 13 is closed, the cutoff valve 18 and the speed regulating valve 21 are opened, the turbine 10 is started, and after steady rotation, power is input from the generator 16 to the power supply line to generate electricity. On the other hand, the high-pressure air for combustion in a hot stove can be made by using air from the combustion air line 20 bypassed from the compressed air line of a blast furnace blower (not shown), but as shown in the figure, exhaust gas energy Recovery turbine 1
When 0 is stopped, compressed air from the blast furnace blower is used,
When the turbine 10 enters steady operation, the switching valve 19 is switched, and the combustion air is passed through the combustion air line 12 from the combustion air compressor 11 which is directly connected to the turbine 10 and is driven at the time.
Another method is to supply compressed air. Therefore, if the arrangement is as shown in FIG. 4, after the expansion turbine 10 for exhaust gas energy recovery starts operating, the furnace top pressure recovery turbine 5 and
Two turbines will generate electricity simultaneously. Therefore, the present invention provides blast furnace equipment equipped with an expansion turbine for top pressure recovery, in which an expansion turbine for exhaust gas energy recovery is installed in the combustion exhaust gas line of a hot blast furnace, and the line of the expansion turbine for exhaust gas energy recovery is installed. A bypass pipe and a bypass valve are auxiliary installed in the blast furnace, and the furnace top gas discharged from the blast furnace is cleaned at high pressure, and a part of it is taken from the high pressure section before the expansion turbine for recovering the furnace top pressure. , the combustion gas is guided into the hot blast furnace with a minimum pressure drop and combusted under high pressure, and the high pressure and high temperature energy of the combustion gas is recovered by an expansion turbine for energy recovery, and the exhaust gas is recovered by an expansion turbine for energy recovery. Since this method guides the exhaust gas into the chimney after it expands, it has the following effects.
第1に、従来、燃焼用空気の予熱あるいは燃料ガスの予
熱にしか利用されていなかつた熱風炉からの高温排ガス
を、その圧力を高めてその全量を直接、膨張タービンで
エネルギー回収することにより、熱風炉排ガスのもつエ
ネルギーをより有効に使用することができる。第2に、
従来の炉頂圧回収タービンと併用して運転することがで
きるので、従来、炉頂圧回収タービンのみで回収される
エネルギーより大きなエネルギーを回収することができ
る。第3に、熱風炉で燃焼して発電などに利用した高炉
排ガスは、従来の熱風炉排ガスの扱いと同様に煙突から
排出し、したがつて、燃焼させない高炉ガス中に混合し
ないため、ガスホルダに行く高炉ガスのカロリーを低め
ることがなく、またそのため、カロリー富化のために使
用するコークス炉発生ガスなどの高価なガスの使用量を
増加させる必要がない。第4に、排ガスエネルギー回収
用の膨張タービンの出口圧力は、タービン出口が煙突に
直結しているため、従来の炉頂圧回収タービンの出口圧
力より低くできるため、出力をよけいにとりだすことが
でき、かつ、出口圧力を低くしても、入口温度が高いの
で、出口ガスの凍結の心配はない。First, by increasing the pressure of high-temperature exhaust gas from a hot blast stove, which has traditionally been used only for preheating combustion air or preheating fuel gas, the entire amount is directly recovered as energy using an expansion turbine. The energy of the hot blast furnace exhaust gas can be used more effectively. Second,
Since it can be operated in conjunction with a conventional top pressure recovery turbine, it is possible to recover more energy than conventionally recovered by the top pressure recovery turbine alone. Thirdly, the blast furnace exhaust gas that is combusted in the hot blast furnace and used for power generation etc. is discharged from the chimney in the same way as conventional hot blast furnace exhaust gas is handled, and therefore it is not mixed with the blast furnace gas that is not combusted, so it is stored in the gas holder. There is no need to reduce the calorie content of the blast furnace gas, and therefore there is no need to increase the amount of expensive gas such as coke oven gas used for calorie enrichment. Fourth, because the turbine outlet is directly connected to the chimney, the outlet pressure of the expansion turbine for exhaust gas energy recovery can be lower than that of a conventional furnace top pressure recovery turbine, so more output can be extracted. Moreover, even if the outlet pressure is lowered, the inlet temperature is high, so there is no need to worry about freezing of the outlet gas.
【図面の簡単な説明】
第1図は従来の高炉ガスエネルギー回収方法の一例の説
明図、第2図は同じくもう1つの説明図、第3図は同じ
くさらにもう1つの説明図、第4図は本発明の一実施例
の説明図てある。
1 ・・・高炉、2・・・ダストキヤツチヤ、3・・・
一次ベンチユリスクラバー、4 ・・・二次ベンチユリ
スクラバー、5・・・炉頂圧回収用膨張タービン、6
・・・セプタム弁、7・・・熱風炉燃焼用高炉ガスライ
ン、8 ・・・熱風炉、9・・・排ガスライン、10・
・・排ガスエネルギー回収用の膨張タービン、11・・
・燃焼用空気圧縮機、12・・・燃焼用空気ライン、1
3・・・バイパス弁、14・・・煙突、15・・・ガス
ホルダ、16,17・・・発電機、18・・・遮断弁、
19・・・切換弁、20・・・燃焼用空気ライン、21
・・・調速弁、22・・・バイパス管。[Brief explanation of the drawings] Fig. 1 is an explanatory diagram of an example of a conventional blast furnace gas energy recovery method, Fig. 2 is another explanatory diagram, Fig. 3 is another explanatory diagram, and Fig. 4 is another explanatory diagram. 1 is an explanatory diagram of an embodiment of the present invention. 1...Blast furnace, 2...Dust catcher, 3...
Primary bench lily scrubber, 4...Secondary bench lily scrubber, 5...Furnace top pressure recovery expansion turbine, 6
...Septum valve, 7.Blast furnace gas line for hot blast furnace combustion, 8..Hot blast furnace, 9..Exhaust gas line, 10.
...Expansion turbine for exhaust gas energy recovery, 11...
・Combustion air compressor, 12... Combustion air line, 1
3... Bypass valve, 14... Chimney, 15... Gas holder, 16, 17... Generator, 18... Shutoff valve,
19...Switching valve, 20...Combustion air line, 21
...Governing valve, 22...Bypass pipe.
Claims (1)
て、熱風炉の燃焼排ガスウインに排ガスエネルギー回収
用の膨張タービンを設置するとともに該排ガスエネルギ
ー回収用の膨張タービンのラインには補助的にバイパス
管およびバイパス弁を設けておき、かつ、高炉から排出
する炉頂ガスを高圧のまま清浄化し、その一部を前記炉
頂圧回収用膨張タービンの手前の高圧部からとり、圧力
降下最小にした状態で前記熱風炉に導いて高圧下で燃焼
させ、しかも、該燃焼ガスのもつ高圧および高温のエネ
ルギーを前記排ガスエネルギー回収用の膨張タービンで
回収し、該排ガスエネルギー回収用の膨張タービンで膨
張したのち排ガスを煙突に導くことを特徴とする、高炉
ガスエネルギーの有効回収法。1 In blast furnace equipment equipped with an expansion turbine for top pressure recovery, an expansion turbine for exhaust gas energy recovery is installed in the flue gas win of the hot blast furnace, and an auxiliary bypass pipe is installed in the line of the expansion turbine for exhaust gas energy recovery. A state in which a bypass valve is provided, and the top gas discharged from the blast furnace is purified while remaining at high pressure, and a portion of it is taken from the high pressure section in front of the expansion turbine for recovering top pressure, thereby minimizing the pressure drop. The combustion gas is guided into the hot stove and burned under high pressure, and the high pressure and high temperature energy of the combustion gas is recovered by the expansion turbine for exhaust gas energy recovery, and after being expanded by the expansion turbine for exhaust gas energy recovery. An effective method for recovering blast furnace gas energy, which is characterized by guiding exhaust gas into the chimney.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1492678A JPS6048614B2 (en) | 1978-02-14 | 1978-02-14 | Effective recovery method for blast furnace gas energy |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1492678A JPS6048614B2 (en) | 1978-02-14 | 1978-02-14 | Effective recovery method for blast furnace gas energy |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS54108115A JPS54108115A (en) | 1979-08-24 |
| JPS6048614B2 true JPS6048614B2 (en) | 1985-10-28 |
Family
ID=11874559
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1492678A Expired JPS6048614B2 (en) | 1978-02-14 | 1978-02-14 | Effective recovery method for blast furnace gas energy |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6048614B2 (en) |
-
1978
- 1978-02-14 JP JP1492678A patent/JPS6048614B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS54108115A (en) | 1979-08-24 |
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