JPS5811712A - Recovery device for sensible heat of converter waste gas - Google Patents
Recovery device for sensible heat of converter waste gasInfo
- Publication number
- JPS5811712A JPS5811712A JP11142281A JP11142281A JPS5811712A JP S5811712 A JPS5811712 A JP S5811712A JP 11142281 A JP11142281 A JP 11142281A JP 11142281 A JP11142281 A JP 11142281A JP S5811712 A JPS5811712 A JP S5811712A
- Authority
- JP
- Japan
- Prior art keywords
- waste gas
- converter
- dust
- gas
- sensible heat
- 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
- 239000002912 waste gas Substances 0.000 title claims abstract description 9
- 238000011084 recovery Methods 0.000 title description 8
- 239000000428 dust Substances 0.000 claims abstract description 36
- 239000007789 gas Substances 0.000 claims abstract description 16
- 238000009434 installation Methods 0.000 claims description 2
- 238000010521 absorption reaction Methods 0.000 claims 1
- 238000007670 refining Methods 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 5
- 238000000034 method Methods 0.000 abstract description 3
- 238000010586 diagram Methods 0.000 description 4
- 239000007921 spray Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000012789 harvest method Methods 0.000 description 1
- 230000002452 interceptive effect Effects 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Abstract
Description
【発明の詳細な説明】
現在、転炉の炉口より排出葛れる転炉廃ガスの温度は非
燃焼ガスｗ！Ｉ収方式の場合で約１ｓｏｏ℃にもなって
いる。本発−はこの転炉廃ＩＸＯ顕熱を効率良く回収す
る装置を提供することを■的とする。[Detailed Description of the Invention] Currently, the temperature of the converter waste gas discharged from the converter mouth is that of non-combustible gas! In the case of the I-harvest method, the temperature is about 1 soo°C. The purpose of this project is to provide an apparatus for efficiently recovering this converter waste IXO sensible heat.
従来の顕熱回収装置を第１図によ）説明するａ転炉ｌよ
り排出され友釣１６００℃の高温のガスから輻射式の熱
交換器２にｌ、ｔ ２００℃〜１０００℃程度迄熱回収
している。その後はスプレー水などＫよる湿式の集塵装
置３を設置するととＫよシガス温度を６０℃程度迄下げ
ると共にガス中のダストの除去を行ってい為。A conventional sensible heat recovery device is explained (see Figure 1).A Heat is recovered from the high-temperature gas discharged from the converter l and at a temperature of 1,600℃ to a radiation type heat exchanger 2 to a temperature of about 200℃ to 1,000℃. are doing. After that, if a wet type dust collector 3 using K such as spray water is installed, the K gas temperature will be lowered to about 60°C and the dust in the gas will be removed.
従って、ガスの顕熱は大部分がスプレー水に持ち去られ
、有効に熱回釈することは出来なかったそれは次の理由
によるためで゛ある。Therefore, most of the sensible heat of the gas was carried away by the spray water, and the heat could not be effectively converted for the following reasons.
転炉ガスを非燃焼で回収した場合、ガス中には１？・Ｏ
を主成分とするダストが約１２ Ｏｆ／Ｎ−の濃度で含
れることは曳く知られている事実である。その丸めに、
中低温度のガスよシ熱回収するのに有効である対流式の
熱交換器を使用すると、そのダストが熱交換器の伝熱管
ＫＪｌｌ積し、正常な使用が妨げられる。よって対流式
によ為熱交換器の使用は困難で６つ九。When converter gas is recovered without combustion, 1?・O
It is a well-known fact that dust containing as the main component is present at a concentration of about 12 Of/N-. In that round,
When a convection heat exchanger, which is effective in recovering heat from medium-low temperature gas, is used, the dust accumulates in the heat exchanger tubes, interfering with normal use. Therefore, it is difficult to use a convection type heat exchanger.
本発明者らは以上の問題点を解決するために対流式の熱
交換器の上流側に乾式の集塵装置を設置することで、対
流式熱交換器の設置を可能とし九本発明を第３図によシ
詳細に説明する。In order to solve the above problems, the present inventors installed a dry type dust collector on the upstream side of the convection type heat exchanger, thereby making it possible to install the convection type heat exchanger. This will be explained in detail with reference to FIG.
第２図は本発明による転炉ガス非燃焼ガス回収方式にお
いて、顕熱を回収する方式の１例を示す装置概要図であ
る。FIG. 2 is a schematic diagram of an apparatus showing an example of a system for recovering sensible heat in the converter gas non-combustion gas recovery system according to the present invention.
００を主成分とする転炉ガスは転炉１の一口より発生し
、１１ｓ燃焼して約１５００℃になる。転炉上部に設置
され九輻射式の熱交換器ｔＫよりガスの顕熱を回収し、
′ｊ！スａｍが１！００℃〜１０００℃になつ先後に乾
式による集塵装置４に導く。The converter gas containing 00 as the main component is generated from the mouth of the converter 1, burns for 11 seconds, and reaches a temperature of about 1500°C. The sensible heat of the gas is recovered from the nine radiant heat exchanger tK installed at the top of the converter.
'j! After the temperature reaches 1,00°C to 1,000°C, the dust is introduced into a dry type dust collector 4.
乾式による集塵装置の設置理−は次の様であも１つには
対流式の熱交換器の便用に問題ない様にダストを除去す
るためである。The installation procedure for the dry type dust collector is as follows.One of the reasons is to remove dust so that there is no problem in using the convection type heat exchanger.
１９には湿式による集塵装置は転炉ガスの温度を低下せ
しめるために顕熱を有効に利用で１１′＆へよって乾式
を使用する。In 19, a wet type dust collector effectively utilizes sensible heat to lower the temperature of the converter gas, and in 11' and 11', a dry type dust collector is used.
１つＫＦｉ湿式の集塵装置であると集塵装置によ〉捕集
しきれなかつえ飛散微小ダストが湿潤する丸め、後の対
流式Ｏ熱交換ＳＳで増積し易い。If the KFi wet type dust collector is used, the scattered microscopic dust that cannot be completely collected by the dust collector becomes wet and is likely to accumulate during the subsequent convection type O heat exchange SS.
以上の層内によ〉設置す為集塵機は乾式であらねばなら
ない。Since the dust collector is installed within the above layers, it must be a dry type.
図には衝央反転式による集塵装置を示し九がナイターン
による方式もより有効でＴｏ為。The figure shows a dust collector using the center-inversion type, and the number 9 indicates that the night-turn type is also more effective.
補集したダストの系外へＯ排出部は水封式のダスト排出
装置ＳＫよ為ことＫより転炉ガスの外部しかる後ガス中
の／ストの大半が除去されダスト１１１度が五〇ｙＮ１
１／以下になっ先後に、対流式の熱交換器６に導き熱回
収を行う。The collected dust is discharged outside the system by a water seal type dust discharge device SK.Thereafter, most of the dust in the gas is removed and the dust is 111 degrees 50yN1.
After the temperature becomes less than 1/2, the heat is introduced into a convection heat exchanger 6 for heat recovery.
以上の装置によ妙転炉ずスのＪＩＩ熱の大半を効率よく
回収する。The above device efficiently recovers most of the JII heat from the converter.
顕熱を十分に回収され温度が３００℃以下になった２転
炉廃ガスは環境汚染ならびに燃料としての使用上問題な
き様にダスト談縦を５（ｋｄ／ Ｎ−以下にするために
２次集塵装置７へと導かれる。The waste gas from the second converter reactor, whose temperature has dropped to below 300°C after sufficient sensible heat recovery, is sent to the secondary converter in order to reduce the dust content to below 5 (kd/N-) to avoid environmental pollution and use as a fuel. The dust is guided to the dust collector 7.
本方弐による装置をｉｓｏ≠−の転炉に設置しての効果
を以下に示す。The effect of installing the device by Honkata Ni in a converter with iso≠- is shown below.
熱回収量に関しては１ｓｏｏ’ｃより３００ｔ？、迄転
炉ガスの顕熱回収が可能とな）、それは溶鋼〒ＯＮあ九
シ約４ Ｘ １ｖ−もの熱量となる。これは従来法に比
較し３〜４倍の熱量である。Regarding the amount of heat recovery, is it 300t from 1soo'c? , it is possible to recover the sensible heat of the converter gas up to 1000 kW), which results in a calorific value of approximately 4 x 1 v- of molten steel. This is 3 to 4 times the amount of heat compared to the conventional method.
又集塵を乾式方法で実施することＫよシ約３００１／ｂ
ｒＯ集塵水を減することが出来る。Also, dust collection should be carried out using a dry method.
rO dust collection water can be reduced.
第１図は従来の顕熱回収方法を示す装管概ｌ！為ｇｉ図
は本発明顕熱回収装置の一実施例を示す概要図である。
１・・・・・・転炉、 ２・・・・・・輻射
式熱交換義３・・・・・・湿式集塵装置、 ４−・・・
・乾式集塵装置、５・・・・・・ダスト排出装置、６・
・・・・・対流式熱交換飄７・・・・・・２次集塵装置
、 ８・・・・・・吸引ファン、９・・・・・・直通
煙突。
弁ＩＭFigure 1 shows a schematic diagram of the conventional sensible heat recovery method. The gi diagram is a schematic diagram showing an embodiment of the sensible heat recovery device of the present invention. 1... Converter, 2... Radiant heat exchange 3... Wet type dust collector, 4-...
・Dry type dust collector, 5...Dust discharge device, 6.
...Convection heat exchanger 7...Secondary dust collector, 8...Suction fan, 9...Direct chimney. Valve IM
Claims (1)
せることなく回収するガス処理装置において、転炉廃ガ
ス通路中に乾式による集塵装置を設置せしめ、その下流
に対流式の熱交換装置を設置せしめたことを特徴とする
転炉Ｈｅスの類熱剛収装置(1) In a gas processing device that recovers waste gas generated during converter refining work without burning it, a dry dust collector is installed in the converter waste gas passage, and a convection heat exchange device is installed downstream of the dry dust collector. A similar heat absorption device for converter Hess, characterized by the installation of
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11142281A JPS5811712A (en) | 1981-07-16 | 1981-07-16 | Recovery device for sensible heat of converter waste gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11142281A JPS5811712A (en) | 1981-07-16 | 1981-07-16 | Recovery device for sensible heat of converter waste gas |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS5811712A true JPS5811712A (en) | 1983-01-22 |
Family
ID=14560770
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11142281A Pending JPS5811712A (en) | 1981-07-16 | 1981-07-16 | Recovery device for sensible heat of converter waste gas |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5811712A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59125962U (en) * | 1983-02-15 | 1984-08-24 | 新日本製鐵株式会社 | Converter exhaust gas treatment equipment |
| CN105890392A (en) * | 2016-06-15 | 2016-08-24 | 湖北金炉节能股份有限公司 | Direct dust collecting device for returned materials of counter-flow heat-supply calcining and drying kiln |
-
1981
- 1981-07-16 JP JP11142281A patent/JPS5811712A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59125962U (en) * | 1983-02-15 | 1984-08-24 | 新日本製鐵株式会社 | Converter exhaust gas treatment equipment |
| CN105890392A (en) * | 2016-06-15 | 2016-08-24 | 湖北金炉节能股份有限公司 | Direct dust collecting device for returned materials of counter-flow heat-supply calcining and drying kiln |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105937765B (en) | A kind of the burning quenching apparatus and method of processing high viscosity strong corrosive salt bearing liquid wastes | |
| JPH10253011A (en) | Combustion apparatus | |
| JPS5811712A (en) | Recovery device for sensible heat of converter waste gas | |
| WO2021082755A1 (en) | Dust removal device for coke dry quenching, and method for increasing steam yield of coke dry quenching boiler | |
| CN107058673B (en) | A kind of converter gas waste heat safety recovery system and method | |
| CN202719620U (en) | Incineration disposal system for fluoric liquid waste and exhaust gas | |
| CN108384583B (en) | System for purifying and utilizing pyrolysis gas of solid waste | |
| CN110452724A (en) | A kind of clean coking process and system | |
| CN208414347U (en) | A kind of purification of solid waste pyrolysis gas and the system of utilizing | |
| CN205042277U (en) | Processing apparatus of thick copper fire refining flue gas | |
| CN108085062A (en) | A kind of total heat recovery coal gasifier device | |
| JPS5822691B2 (en) | Exhaust gas sampling filtration device | |
| CN209475892U (en) | A kind of dust removing treatment system for gas burner | |
| CN208995361U (en) | A kind of pyrolysis plant flue gas heat recovery system | |
| CN103484597B (en) | Dust-removing and heat-recovering system for furnace gas of steel converter and processing method therefor | |
| CN106268127A (en) | V2o5reduction kiln reduction exhaust gas recovery system and recovery process | |
| JP3514044B2 (en) | Coke dry fire extinguishing equipment | |
| CN104263413B (en) | Method for realizing zero emission of dioxin during preparation of fuel gas with household garbage and device for implementing method | |
| CN214528840U (en) | Dry quenching coke powder resourceful treatment device | |
| CN212930001U (en) | Solid waste is with burning exhaust treatment device | |
| CN115031253A (en) | Gas boiler system for cleaning and efficiently recycling heat energy | |
| CN208414333U (en) | A kind of pyrolysis gas Recovery Purifying and reutilization system | |
| CN101862580B (en) | Novel high-efficiency dedusting and desulphurization integrated system process for coke-tamping, coaling and coke-discharging ground station | |
| CN106594780A (en) | High-sodium coal heating removing furnace and coal-fired power plant integrating device and method thereof | |
| CN115614763A (en) | Dry type recovery system and method for waste heat of slag of liquid slag-discharging boiler |