JPS59222514A - Treating installation for waste gas from converter - Google Patents
Treating installation for waste gas from converterInfo
- Publication number
- JPS59222514A JPS59222514A JP58096503A JP9650383A JPS59222514A JP S59222514 A JPS59222514 A JP S59222514A JP 58096503 A JP58096503 A JP 58096503A JP 9650383 A JP9650383 A JP 9650383A JP S59222514 A JPS59222514 A JP S59222514A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- converter
- mouth
- gaseous
- skirt
- 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.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
- C21C5/28—Manufacture of steel in the converter
- C21C5/38—Removal of waste gases or dust
- C21C5/40—Offtakes or separating apparatus for converter waste gases or dust
-
- 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
- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/40—Capture or disposal of greenhouse gases of CO2
-
- 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
- Y02P10/00—Technologies related to metal processing
- Y02P10/10—Reduction of greenhouse gas [GHG] emissions
- Y02P10/122—Reduction of greenhouse gas [GHG] emissions by capturing or storing CO2
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Treating Waste Gases (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は、転炉の非燃焼式排ガス処理装置の改良に関す
るものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement of a non-combustion type exhaust gas treatment device for a converter.
従来から繰業中、転炉の発注ガスは第1図に見る如く殆
んど燃焼させずに冷却、集じんしている。Conventionally, during operation, the gas ordered for the converter is cooled and dust-collected without being combusted, as shown in Figure 1.
即ち、図にあって、1は転炉本体で、2はスカート、3
、4は回収ガス(排ガス)の冷却器で、回収ガスを例え
ば1000℃程度に冷却する。5は一次集じん機、6は
二次集じん機で、共に通常ベンチュリースクラバーが採
用される。7は誘引送風機、8は三方切替弁で排ガスを
回収しない場合は8a−閉、8b−開、回収する場合は
8a開、8b閉となる。又9はバイパス弁で8bが閉か
ら開指令で作動しない場合緊急に開となる。猟時に閉。That is, in the figure, 1 is the converter main body, 2 is the skirt, and 3 is the converter body.
, 4 is a cooler for recovered gas (exhaust gas), which cools the recovered gas to, for example, about 1000°C. 5 is a primary dust collector, 6 is a secondary dust collector, and venturi scrubbers are usually used for both. 7 is an induced blower, 8 is a three-way switching valve, and when exhaust gas is not collected, 8a is closed and 8b is open, and when exhaust gas is collected, 8a is open and 8b is closed. Further, 9 is a bypass valve which is opened in an emergency if 8b is not activated by a command to open from close. Closed when hunting.
10は燃焼放散塔で転炉吹錬の初期、及び末期に排ガス
を燃焼放散する。11は水封逆止弁でガス回収中に開と
なる。12は水封弁で非常時(たとえは転炉休止時)に
ガス回収ホルダー13との縁を切るため水封されるが通
常時は開となっている。Reference numeral 10 denotes a combustion diffusion tower that combusts and diffuses exhaust gas at the beginning and end of converter blowing. Reference numeral 11 is a water seal check valve that is opened during gas recovery. Reference numeral 12 is a water seal valve which is water sealed in order to disconnect from the gas recovery holder 13 in an emergency (for example, when the converter is shut down), but is normally open.
上記構成にあって炉口とスカート部2には機械的シール
が困難なためシールしておらす、空気過剰係数λ=0.
1となるよう操業を行なっているか、転炉発生ガス中に
は空気が混入するため、回収ガスの主成分は(CO+C
O2+N2)となっている。In the above configuration, the furnace mouth and skirt part 2 are sealed because it is difficult to mechanically seal them, and the excess air coefficient λ=0.
1, or because air is mixed in the gas generated from the converter, the main component of the recovered gas is (CO + C
O2+N2).
従来、この回収ガスに、その侭燃料ガスとして回収利用
されているが、最近、これらガスの品質向上、化学原料
としての再利用が話題にのぼり出した。この場合、回収
ガスは先述した如くN2ガスが混在しているため、CO
分の抽出が難つかしく、従って抽出、分離装散が複雑か
つ高価な設備とならざるを得なかった。Conventionally, this recovered gas has been recovered and used as fuel gas, but recently, the improvement of the quality of these gases and their reuse as chemical raw materials have become a hot topic. In this case, as mentioned above, the recovered gas contains N2 gas, so CO
It is difficult to extract the fraction, and therefore extraction, separation and dispersion have to be complicated and expensive equipment.
そこで、本発明は炉口をCO2ガスで完全にシールして
発生ガス中に空気の侵入即ちN2の混入を防きCO/C
O2の分離、抽出を容易にし、COの品質向上更には、
CO2の再利用を図らんとするものでありその要旨とす
るところは
1.転炉発生ガスを燃焼させずに冷却、集じん後COガ
スとして回収する装置に於て、転炉炉口部とスカート部
分に、CO2によるシール構造を形成すると共に、上記
COガス回収経路の末尾にCO/CO2分離、抽出装置
を設けたことを特徴とする転炉の排ガス処理設備。Therefore, the present invention completely seals the furnace mouth with CO2 gas to prevent air from entering the generated gas, that is, to prevent N2 from entering the CO/C
Facilitates the separation and extraction of O2, improves the quality of CO, and
It aims to reuse CO2, and its main points are 1. In a device that recovers CO gas after cooling and collecting dust without burning the gas generated in a converter, a seal structure using CO2 is formed at the mouth and skirt of the converter, and at the end of the CO gas recovery path. Converter exhaust gas treatment equipment characterized by being equipped with a CO/CO2 separation and extraction device.
2.転炉発生ガスを燃焼させずに冷却、集じん後COガ
スとして回収する装置に於て、転炉炉口部とスカート部
分に、CO2によるシール構造を形成すると共に、上記
COガス回収経路の末尾にCO/CO2分離、抽出装置
を設け、更に該分離、抽出装置から上記炉口部のシール
構造及び/又はランス等のパージ部分へCO2の供給経
路を形成したことを特徴とする転炉の排ガス処理設備で
ある。2. In a device that recovers CO gas after cooling and collecting dust without burning the gas generated in a converter, a seal structure using CO2 is formed at the mouth and skirt of the converter, and at the end of the CO gas recovery path. A converter exhaust gas characterized in that a CO/CO2 separation and extraction device is provided in the converter, and a CO2 supply path is formed from the separation and extraction device to a seal structure at the furnace mouth and/or a purge portion such as a lance. This is processing equipment.
次に第2図、第3図に示す一実施例を基にして本発明を
詳細に説明する(図にあって従来と同構造の部分の説明
は省略する)。図に示す如く、ガス回収ホルダー13の
後流にCO/CO2分離、抽出装置14を配置し、又、
転炉炉体1の炉口とスカート2間には、CO2ガスによ
る炉口シールが形成されている。第3図にその実施例を
示す。スカート2下部には、炉口に面してラビリンスシ
ール20が設りられ、又、この部分には、CO2ガスを
供給するためのノズル部23が設けられている。21は
該ノズル23部に連通しているヘッダー管で、これらノ
ズル部とへッダー管は、スカート2の昇降に追従出来る
ように伸縮管22が設けられ該伸縮管22にはCO2供
給管16が連接されている。Next, the present invention will be explained in detail based on an embodiment shown in FIGS. 2 and 3 (description of parts in the figures having the same structure as the conventional one will be omitted). As shown in the figure, a CO/CO2 separation and extraction device 14 is placed downstream of the gas recovery holder 13, and
A furnace mouth seal made of CO2 gas is formed between the furnace mouth of the converter furnace body 1 and the skirt 2. An example is shown in FIG. A labyrinth seal 20 is provided at the bottom of the skirt 2 facing the furnace mouth, and a nozzle portion 23 for supplying CO2 gas is provided in this portion. Reference numeral 21 denotes a header pipe communicating with the nozzle section 23. These nozzle sections and the header pipe are provided with a telescopic pipe 22 so that they can follow the rise and fall of the skirt 2, and the CO2 supply pipe 16 is connected to the telescopic pipe 22. connected.
本発明は、上記構成に見る如くCO2パージしてN2の
混入を防いでいるため、CO/CO2の分離が容易なた
め、その分離、抽出装置14を系内に設けることが可能
になったのである。しかして発生ガスは一旦、回収ガス
のホルダー13に貯蔵され、一部は従来と同じくその侭
燃料として利用され、他はCO/CO2分離、抽出装置
14へ送給し、ここでCO/CO2を分離し、COはC
Oガスライン18を介し、例えばC1化学原料として利
用される。As seen in the above configuration, the present invention purges CO2 to prevent the incorporation of N2, so it is easy to separate CO/CO2, and it is now possible to install the separation and extraction device 14 in the system. be. The generated gas is temporarily stored in the recovered gas holder 13, and part of it is used as a fuel as before, while the other part is sent to the CO/CO2 separation and extraction device 14, where the CO/CO2 is extracted. separated, CO is C
It is used, for example, as a C1 chemical raw material through the O gas line 18.
CO2は、再び炉口部のシール又は、ライン15を介し
、例えばランス挿入口3′等のパージシール用のガスと
して利用される。The CO2 is used again as a gas for sealing the furnace mouth or for purge sealing, for example, the lance insertion port 3' via the line 15.
以上の如く、本発明によれは、COの品質が向上し、カ
ロリーアップ又は、他の資源としての利用が可能になる
等の効果を有し、更には回収ガスを全く燃焼させないた
め排ガス処理設備が小さくなる等のメリット有し又、本
発明にあっては、本設備によって回収したCO2をシー
ル、パージ用の不活性ガス媒体として再利用が可能なた
め、そのための設備及び運転費も不要になる等、実用的
価値は大である。As described above, the present invention has effects such as improving the quality of CO, increasing its calories, and making it possible to use it as other resources.Furthermore, since the recovered gas is not combusted at all, the exhaust gas treatment equipment In addition, with the present invention, the CO2 recovered by this equipment can be reused as an inert gas medium for sealing and purging, so the equipment and operating costs for this are unnecessary. It has great practical value.
第1図は従来の転炉排ガス処理設備の構造説明図、
第2図は本発明実施例設備の詐明図、
第3図は、第2図に於けるシール構造の実施例説明図で
ある。
1:転炉 2:スカート
3、4:冷却器 5:一次集じん機
6:二次集じん機 7:誘引送風機
8:三方弁 9:バイパス弁
10:放散塔 1l:ガス回収弁
12:水封弁 13:回収ガスホルダー14:CO/C
O2分離、抽出装置
15:CO2ガスライン
16:炉口CO2ガスシールライン
17:各部パージ、シールライン
18:COガスライン
19:炉口シール構造部
20:ラビリンスシール
21:CO2ガスヘッダー管
22:伸縮管。Fig. 1 is an explanatory diagram of the structure of conventional converter exhaust gas treatment equipment, Fig. 2 is a simplified diagram of the equipment according to the present invention, and Fig. 3 is an explanatory diagram of an embodiment of the seal structure in Fig. 2. . 1: Converter 2: Skirt 3, 4: Cooler 5: Primary dust collector 6: Secondary dust collector 7: Induced fan 8: Three-way valve 9: Bypass valve 10: Stripping tower 1l: Gas recovery valve 12: Water Valve seal 13: Recovery gas holder 14: CO/C
O2 separation and extraction device 15: CO2 gas line 16: Furnace CO2 gas seal line 17: Purge and seal line 18: CO gas line 19: Furnace seal structure 20: Labyrinth seal 21: CO2 gas header pipe 22: Expandable tube.
Claims (1)
スとして回収する装置において、転炉炉口部とスカート
部分に、CO2によるシール構造を形成すると共に、上
記COガス回収経路の末尾にCO/CO2分離、抽出装
置を設けたことを特徴とする転炉の排ガス処理設備。 2 転炉発生ガスを燃焼させずに冷却、集じん後COガ
スとして回収する装置において、転炉炉口部とスカート
部分に、CO2によるシール構造を形成すると共に、上
記COガス回収経路の末尾にCO/CO2分離、抽出装
置を設け、更に該分離、抽出装置から上記炉口部のシー
ル構造及び/又はランス等のパージ部分へCO2の供給
経路を形成したことを特徴とする転炉の排ガス処理設備
。[Claims] 1. In an apparatus for cooling the gas generated in a converter without burning it, collecting it as CO gas after collecting dust, a sealing structure using CO2 is formed at the mouth and skirt of the converter, and the CO gas is recovered as CO gas. A converter exhaust gas treatment facility characterized by having a CO/CO2 separation and extraction device installed at the end of a gas recovery path. 2. In a device that recovers CO gas after cooling and collecting dust without burning the gas generated in a converter, a sealing structure using CO2 is formed at the mouth and skirt of the converter, and a seal structure is formed at the end of the CO gas recovery path. Exhaust gas treatment for a converter, characterized in that a CO/CO2 separation and extraction device is provided, and a CO2 supply path is formed from the separation and extraction device to a seal structure at the furnace mouth and/or a purge portion such as a lance. Facility.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58096503A JPS59222514A (en) | 1983-05-31 | 1983-05-31 | Treating installation for waste gas from converter |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58096503A JPS59222514A (en) | 1983-05-31 | 1983-05-31 | Treating installation for waste gas from converter |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS59222514A true JPS59222514A (en) | 1984-12-14 |
Family
ID=14166907
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58096503A Pending JPS59222514A (en) | 1983-05-31 | 1983-05-31 | Treating installation for waste gas from converter |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59222514A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105400965A (en) * | 2015-11-18 | 2016-03-16 | 铜陵有色设计研究院 | Flue gas collecting device for copper smelting of converter process |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS562392A (en) * | 1979-06-20 | 1981-01-12 | Nippon Steel Corp | Purification of gas formed from converter |
-
1983
- 1983-05-31 JP JP58096503A patent/JPS59222514A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS562392A (en) * | 1979-06-20 | 1981-01-12 | Nippon Steel Corp | Purification of gas formed from converter |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105400965A (en) * | 2015-11-18 | 2016-03-16 | 铜陵有色设计研究院 | Flue gas collecting device for copper smelting of converter process |
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