JPS5970703A - Humidification device for blasting to blast furnace - Google Patents
Humidification device for blasting to blast furnaceInfo
- Publication number
- JPS5970703A JPS5970703A JP18078482A JP18078482A JPS5970703A JP S5970703 A JPS5970703 A JP S5970703A JP 18078482 A JP18078482 A JP 18078482A JP 18078482 A JP18078482 A JP 18078482A JP S5970703 A JPS5970703 A JP S5970703A
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- Japan
- Prior art keywords
- water
- steam
- nozzle
- air
- amount
- 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.)
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B9/00—Stoves for heating the blast in blast furnaces
- C21B9/16—Cooling or drying the hot-blast
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Nozzles (AREA)
Abstract
Description
【発明の詳細な説明】 本発明は高炉送風の加湿装置に関するものである。[Detailed description of the invention] The present invention relates to a humidifying device for blast furnace air.
高炉操業を安定させるために、高炉への送風を加湿して
高炉の羽口前理論燃焼温度を調節すると共に羽ロ水素人
量?Il−調節することは知られている。In order to stabilize blast furnace operation, the blast furnace air is humidified to adjust the theoretical combustion temperature before the tuyere of the blast furnace, and the amount of hydrogen in the blast furnace is adjusted. It is known that Il-regulates.
この送風への加湿の具体的方法としては、送風機と熱風
炉間の送風本管内の冷風中に水蒸気ヶ吹込むことによっ
て加湿する水蒸気加湿法、送風機と熱風炉間の送風本管
内の冷風中に水噴霧ノズルから常温水’k”]&し、微
細な水粒子にして吹込むことにより・送風機の断熱圧縮
によって昇温した冷風の顕熱で上記微細な水粒子を気化
せしめて水蒸気となし加湿する水噴霧加湿法がある。Specific methods for humidifying this air include the steam humidification method, which humidifies the cold air in the main air pipe between the blower and the hot air stove, and the steam humidification method, which humidifies the cold air in the main air pipe between the blower and the hot air stove. By blowing room-temperature water 'k''& into fine water particles from the water spray nozzle, the sensible heat of the cool air heated by the adiabatic compression of the blower vaporizes the fine water particles and turns them into water vapor, resulting in humidification. There is a water spray humidification method.
この水噴霧加湿法は、送風機で昇温された冷風の顕熱を
利用して微細水粒子を水蒸気となし加湿するものである
から、水蒸気加湿法で必要な水蒸気が節約でき水蒸気を
得るためのエネルギーが節約できると共に、熱風炉前の
冷風の温度が低下して熱風炉の熱効率を向上させ省エネ
ルギー効果ケ得ることができる利点がある。This water spray humidification method uses the sensible heat of cold air heated by a blower to turn fine water particles into water vapor and humidify it. Therefore, the water vapor required by the water vapor humidification method can be saved, and the water vapor required for obtaining water vapor can be saved. This has the advantage that not only can energy be saved, but the temperature of the cold air in front of the hot-blast stove is lowered, improving the thermal efficiency of the hot-blast stove and achieving an energy-saving effect.
本発明者は前記水噴霧加湿法について検討し、次の検討
結果を得た。The present inventor studied the water spray humidification method and obtained the following results.
(1)水9t、m加湿法における水噴霧蒸発加侵可能量
は冷風温度によって左右され、例えば小型の高炉では、
送風圧力が低くて冷風温度が低く噴霧水量會多く6する
ことができず、熱風炉前の冷風湿分(高炉送風湿分)を
高炉の安定操業に必要な目標値にできない。上記目標値
に対して水噴霧蒸発加湿可能量で不足する湿分け、水蒸
気加湿法による水蒸気吹込みで対処し危ければならない
。(1) The amount of water that can be evaporated and penetrated by water spray in the 9t/m water humidification method depends on the temperature of the cold air. For example, in a small blast furnace,
The blast pressure is low, the cold air temperature is low, and it is not possible to increase the amount of spray water, making it impossible to bring the cold air moisture in front of the hot blast furnace (blast furnace blast moisture) to the target value required for stable operation of the blast furnace. If the amount of moisture that can be humidified by water spray evaporation is insufficient for the above-mentioned target value, it must be dealt with by blowing in steam using the steam humidification method.
例えば、高炉送風目標湿分2 B、 5 ’/ fir
r? +大気湿分’7.2 f/ /Nm3+送風量1
7501JmF/min。For example, target blast furnace humidity 2B, 5'/fir
r? + Atmospheric humidity '7.2 f/ /Nm3 + Air flow rate 1
7501JmF/min.
送風圧力L 6 Kg/ crl +冷風温度120℃
のとき水噴霧加湿可能量は11.5もバーであり、不足
加湿量9.8 ? /Nn?は水蒸気加湿法による水蒸
気吹込量となる。Blow pressure L 6 Kg/crl + cold air temperature 120℃
, the possible water spray humidification amount is 11.5 bars, and the insufficient humidification amount is 9.8? /Nn? is the amount of steam blown by the steam humidification method.
(2) 水噴霧ノズルによって常温水を噴霧して微細
水粒子とし、これ’1loo〜250℃の冷風顕熱で蒸
発加湿する際には蒸発性を良くするため水滴径葡100
μ以下程度にする必要がある。(2) Water at room temperature is sprayed with a water spray nozzle to form fine water particles, and when humidifying by evaporation with cold wind sensible heat at 1loo~250°C, the water droplet diameter is 100 to improve evaporability.
It needs to be about μ or less.
(3)水噴霧ノズルとして例えば水圧のみで水を霧化さ
せる水噴霧ノズル(以下−流体ノズルと略す)【採用す
る場合、上記微細水滴を発生させる一流体ノズルは、ノ
ズル1個当りの水量が少なく、例えば水蒸気加湿法で加
湿していた量10〜20グ/Nmを噴霧するには・数十
〜数百個のノズルが必要であり、水噴霧ノズルの保守点
検が煩雑となる。(3) As a water spray nozzle, for example, a water spray nozzle that atomizes water using only water pressure (hereinafter referred to as a fluid nozzle) [When adopted, the fluid nozzle that generates the fine water droplets described above has a water volume per nozzle. In order to spray a small amount of water, for example 10 to 20 g/Nm, which is the amount humidified by the steam humidification method, tens to hundreds of nozzles are required, and maintenance and inspection of the water spray nozzles becomes complicated.
一方、水噴霧ノズルとして、例えば水を気体圧力で霧化
させる水噴霧ノズル(以下二流体ノズルと略す)を採用
する場合、1個のノズルで多量の水を微細水滴にして噴
射でき、例えば気体として10〜20 Kg / cr
Aの圧縮空気を使用すると、上記水蒸気加湿法で加湿し
ていた量10〜202β背を噴霧するのに数個のノズル
で十分であり、水噴霧ノズルの保守点検が極めて容易と
なる。しかしなから二流体ノズルでは、霧化媒体として
1O−20h/caの圧縮空気を必要とし、このような
圧縮空気を得るために別途空気圧縮機全必要とし圧縮機
運転費が必要となり、水蒸気加湿法による水蒸気製造エ
ネルギー節約効果を減少してしまう。On the other hand, when a water spray nozzle that atomizes water using gas pressure (hereinafter referred to as a two-fluid nozzle) is used as a water spray nozzle, it is possible to spray a large amount of water into fine water droplets with one nozzle. As 10-20 Kg/cr
When compressed air A is used, a few nozzles are sufficient to spray the amount of 10 to 202β that was humidified by the water vapor humidification method, and maintenance and inspection of the water spray nozzles becomes extremely easy. However, the two-fluid nozzle requires compressed air of 10-20h/ca as the atomization medium, and to obtain such compressed air, a separate air compressor is required, which requires compressor operating costs, and requires steam humidification. This reduces the energy saving effect of the steam production method.
(4)前記(1)の如く高炉送風目標湿分に対して水噴
霧蒸発加湿可能量が不足する場合・送風湿分補足用の水
蒸気を前記(2)の二流体ノズルにおける水の霧化媒体
として有効活用することによって、上記空気圧縮機並び
に圧縮機運転費を要せずに、安価に高炉送風目標湿分に
加湿できる。(4) When the amount of water spray evaporation and humidification is insufficient for the blast furnace blast target target humidity as in (1) above, the water vapor for supplementing the blast furnace moisture is used as the water atomization medium in the two-fluid nozzle in (2) above. By effectively utilizing the air as a fuel, it is possible to humidify the blast furnace air to the target humidity at low cost without requiring the air compressor or the operating cost of the compressor.
更に高炉送風目標湿分に対して水噴霧蒸発加湿可能量が
不足する場合、−流体ノズルによる水噴霧で上記加湿可
能量まで加湿すると共に上記不足分を水蒸気吹込管によ
る水蒸気吹込量で補う加湿方式も考えられが、この加湿
方式に比較して前記送風湿分補足用の水蒸気を二流体ノ
ズルの水霧化媒体として有効活用する加湿方式は、上記
水噴霧蒸発加湿可能量まで加湿するのに必要なノズル数
を太幅に減少してノズルの保守点検が極めて容易となる
。Furthermore, if the amount of water spray evaporation that can be humidified is insufficient with respect to the target blast furnace blast humidity, - a humidification method in which water spray from a fluid nozzle is used to humidify up to the above possible humidification amount, and the shortage is compensated for by the amount of steam blown through a steam blowing pipe. However, compared to this humidification method, a humidification method that effectively utilizes the water vapor for moisture supplementation by air as a water atomization medium of a two-fluid nozzle is necessary to humidify to the amount that can be humidified by water spray evaporation. This greatly reduces the number of nozzles, making maintenance and inspection of the nozzles extremely easy.
本発明は前記検討結果にもとづきなされたもので・本発
明の要旨は送風機と熱風炉間の送風本管内に、水を水蒸
気で霧化する水噴霧ノズルを内設したことを特徴とする
高炉送風の加湿装置にある。The present invention has been made based on the above-mentioned study results.The gist of the present invention is to provide a blast furnace blower characterized by a water spray nozzle for atomizing water into steam being installed in the main blower pipe between the blower and the hot blast furnace. in the humidifier.
以下、本発明の高炉送風の加湿装置の一実施例を図面に
より説明する。DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the blast furnace air humidification device of the present invention will be described below with reference to the drawings.
叱1図においてlは送風機と熱風炉間の送風本管で、2
は送風本管l内に内設した二流体ノズルである。第2図
は二流体ノズル2の断面斜視図で2aはノズルの水通路
、2bはノズルの水霧化媒体通路、2cは通路2aから
通路2bへ水金供給する供給孔、2dはノズル2先の水
噴霧孔を示す。In Figure 1, l is the main air pipe between the blower and the hot air stove, and 2
is a two-fluid nozzle installed inside the blower main pipe l. FIG. 2 is a cross-sectional perspective view of the two-fluid nozzle 2, where 2a is a water passage of the nozzle, 2b is a water atomizing medium passage of the nozzle, 2c is a supply hole for supplying water and gold from passage 2a to passage 2b, and 2d is a tip of the nozzle 2. water spray holes are shown.
第1図において3及び4は二流体ノズル2の水通路2a
及び水霧化媒体通路2bに接続した水供給系及び水蒸気
供給系である。水供給系3は、水配管5に加圧ポンプ6
を配置すると共にこのポンプ6の吐出側の水配管に流量
検出器7.流量調節弁8′fr:配置してなる。また水
蒸気供給系4は、水蒸覧配管9に流量検出器10.流量
調節弁11を配置してなる。ユ2は送風圧力、冷風温度
から決まる蒸発可能な上限噴霧水量紮目標値として設定
されて・流量検出器7の実測値が目標値となるように流
量調節弁8を制御する水流量調節計、13は目標送風湿
分、大気湿分、上記上限噴霧水量から決まる水噴霧蒸発
加湿量から、目標送風湿分に加湿するに必要な水蒸気流
量を算出する水蒸気流電演算器、14は上記水蒸気流量
に流量検出器lOの実測値がなるように流量調節弁11
を制御する水蒸気量調節計である。In FIG. 1, 3 and 4 are water passages 2a of the two-fluid nozzle 2.
and a water supply system and a water vapor supply system connected to the water atomization medium passage 2b. The water supply system 3 includes a water pipe 5 and a pressure pump 6.
and a flow rate detector 7 on the water piping on the discharge side of the pump 6. Flow control valve 8'fr: arranged. In addition, the water vapor supply system 4 includes a water vapor detection pipe 9 and a flow rate detector 10. A flow control valve 11 is arranged. U 2 is a water flow rate controller that is set as a target value for the upper limit amount of spray water that can be evaporated and determined from the blowing pressure and cold air temperature, and controls the flow rate control valve 8 so that the actual value of the flow rate detector 7 becomes the target value; 13 is a water vapor current calculator that calculates the water vapor flow rate necessary to humidify the target air humidity from the water spray evaporation humidification amount determined from the target air humidity, atmospheric humidity, and the above-mentioned upper limit spray water amount; 14 is the water vapor flow rate mentioned above; The flow rate control valve 11 is adjusted so that the actual measured value of the flow rate detector lO becomes
This is a water vapor amount controller that controls the amount of water vapor.
以上の様に構成した高炉送風の加湿装置によると、加圧
ポンプ6によって昇圧された水は検出器7、調節計12
.調節弁8からなる制御系で上記上限噴ぜ水量に一定制
御され、二流体ノズル2へ供給される。一方水膳化用水
蒸気は、演算器13で演算された〔(目標送風湿分)−
(大気湿分)−(上限噴霧水量から決る上限水噴霧蒸発
加湿量)〕になるように。検出器10.調節計14.調
節弁11よシなる制御系で制御されて二流体ノズル2へ
供給される。According to the blast furnace air humidification device configured as described above, the water pressurized by the pressurizing pump 6 is transferred to the detector 7 and the controller 12.
.. The amount of water jetted is controlled to be constant at the upper limit amount by a control system including a regulating valve 8, and is supplied to the two-fluid nozzle 2. On the other hand, the water vapor for serving water is calculated by the calculator 13 [(target air humidity) -
(Atmospheric moisture) - (Upper limit water spray evaporation humidification amount determined from upper limit spray water amount)]. Detector 10. Controller 14. It is controlled by a control system such as a control valve 11 and supplied to the two-fluid nozzle 2.
そして二流体ノズル2へ供給された水は、同様に供給さ
れた水蒸気によって微細水滴となって、送風本管2内の
冷風中に吹込まれ、微細水滴が冷風顕熱で蒸発し水蒸気
となり、上記霧化用水蒸気とともに冷風を目標送風湿分
まで加湿する。The water supplied to the two-fluid nozzle 2 is turned into fine water droplets by the similarly supplied water vapor, and blown into the cold air in the blast main pipe 2, and the fine water droplets are evaporated by the sensible heat of the cold air and become water vapor. Humidifies cold air with atomizing water vapor to the target air humidity.
なお水供給系已に自動水流量制御系を構成せずに流量調
節弁8の弁開度を一定に手動設定して、二流体ノズル2
へ水供給することもできる。この場合、弁8の開度が一
定でも目標送風湿分、大気湿分が変化して必要水蒸気量
が変化すると、ノズル2から冷風中への噴霧氷量が変化
するのでこのような水量変化を考慮して、上記変化があ
ってもノズル2からの冷風中への噴霧水量が上記上限噴
霧水量を越えないように弁8の開度設定するととが、本
管l内にドレン発生しないようにする上で必要である。In addition, without configuring an automatic water flow rate control system in the water supply system, the valve opening degree of the flow rate adjustment valve 8 is manually set to a constant value, and the two-fluid nozzle 2
It is also possible to supply water to In this case, even if the opening degree of the valve 8 is constant, if the target air humidity and atmospheric humidity change and the required amount of water vapor changes, the amount of misted ice sprayed from the nozzle 2 into the cold air will change. Taking into account the above changes, the opening of the valve 8 is set so that the amount of water sprayed into the cold air from the nozzle 2 does not exceed the upper limit amount of water sprayed, and in order to prevent drainage from occurring in the main pipe 1. It is necessary to do so.
なお二流体ノズル2は、目標送風湿分制御のために使用
される霧化用蒸気量と噴霧氷量との比較範囲で、好まし
くは低い霧化用蒸気圧力、噴霧水圧で水を蒸発性の良好
な100μ以下の水滴にすることができる性能のものを
選定する。In addition, the two-fluid nozzle 2 is designed to evaporate water at preferably low atomization steam pressure and spray water pressure within the comparison range of the atomization steam amount and spray ice amount used for target air humidity control. Select one that has the ability to form water droplets with a size of 100 μm or less.
例えば冷風温度120℃、送風圧力1.6に9/ cr
l +送風量1750 N?7Z’/min 、大気湿
分7−2 Si’ /Nm3゜目標送風湿分28.5
ii’ /N77z’ 、必要加湿量21.3ji’/
N iであり、水噴霧蒸発可能加湿量(最大水噴霧加湿
蓋J 11.5 y 7N77z、水蒸気加湿量9.8
S’/Nm8の場合(霧化用蒸気量/噴霧水量〕≧0
.1で、噴霧水圧6.8 /(y / tst + f
it化用蓋用蒸気圧力6OKg / crrtテ100
μ以下の水滴にする性能の二流体ノズルを使用する。For example, when the cold air temperature is 120℃ and the blowing pressure is 1.6, it is 9/cr.
l + Air flow rate 1750 N? 7Z'/min, atmospheric humidity 7-2 Si'/Nm3゜Target air humidity 28.5
ii'/N77z', required humidification amount 21.3ji'/
N i, water spray evaporable humidification amount (maximum water spray humidification lid J 11.5 y 7N77z, water vapor humidification amount 9.8
In the case of S'/Nm8 (atomization steam amount/spray water amount) ≧0
.. 1, spray water pressure 6.8 / (y / tst + f
Steam pressure for IT lid 6OKg/crrtte 100
Use a two-fluid nozzle capable of producing water droplets smaller than μ.
この二訛体ノズル1個当りの噴霧氷量は21t/ pi
nと極めて多く送風量1750N771/騎、水噴務加
湿量11.5 r /N?7Z” k加湿するために送
風本管2内に内設するノズル数は1個ですむ。なお噴霧
水圧10Kg/m2で100μ以下の水滴をうる一流体
ノズルでは80個のノズルを内設する必要がある。The amount of sprayed ice per two-piece nozzle is 21t/pi.
Extremely large air flow rate: 1750N771/Ki, water jet humidification amount: 11.5 r/N? 7Z"k Only one nozzle is required to be installed inside the main air pipe 2 for humidification.In addition, for a single fluid nozzle that produces water droplets of 100μ or less at a spray water pressure of 10Kg/m2, 80 nozzles need to be installed inside. There is.
以上述べた様に本発明の高炉送風の加湿装置によれば、
高炉送風目標湿分に対して水噴霧蒸発加湿可能量が不足
し、水蒸気で補足する場合、送風湿分補足用の水蒸気を
二流体ノズルにおける水の霧化媒体として有効活用して
、水噴霧ノズルとして二流体ノズルを採用する際に必要
な空気圧縮機並びに圧縮機運転費を要せずに、安価に高
炉送風を目標湿分に加湿できる。また、本発明装置は水
噴餠ノズルとして二流体ノズルを採用するものであるか
ら、水噴霧蒸発加湿可能量まで加湿するのに一流体ノズ
ルを採用する場合に比較して、必要なノズル数を大幅に
減少してノズルの保守点検葡容易にすることができる。As described above, according to the blast furnace air humidification device of the present invention,
When the amount of moisture that can be evaporated and humidified by water spray evaporation is insufficient for the blast furnace blast target target humidity and water vapor is used to supplement the moisture content, the water vapor for supplementing the blast furnace moisture can be effectively used as a water atomization medium in the two-fluid nozzle. Blast furnace air can be humidified to the target humidity at low cost without requiring an air compressor or compressor operating costs that are required when adopting a two-fluid nozzle. Furthermore, since the device of the present invention uses a two-fluid nozzle as the water spray nozzle, the number of nozzles required can be reduced compared to the case where a single-fluid nozzle is used to humidify to the amount that can be humidified by water spray evaporation. Maintenance and inspection of the nozzle can be greatly reduced and facilitated.
第1図は、本発明の高炉送風の加湿装置の−実流側の説
明図、第2図は二流体ノズルの断面斜視図である。
1・・・・・・送風本管
2・・・ ・・・二流体ノズル
3・・・・・・水供給系
4・・・・・・水蒸気供給系
5・・・・・・水配管
9・・・ ・・・水蒸気配管
出 願 人 妨日本製鐵株式会社FIG. 1 is an explanatory diagram of the actual flow side of the blast furnace air humidification device of the present invention, and FIG. 2 is a cross-sectional perspective view of a two-fluid nozzle. 1...Blower main pipe 2...Two-fluid nozzle 3...Water supply system 4...Steam supply system 5...Water piping 9 ... ...Steam piping application person: Nippon Steel Corporation
Claims (1)
る水噴霧ノズルを内設したことを特徴とする高炉送風の
加湿装置。A humidifying device for blowing air from a blast furnace, characterized in that a water spray nozzle that atomizes water into steam is installed in the main air pipe between the blower and the hot blast furnace.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18078482A JPS5970703A (en) | 1982-10-15 | 1982-10-15 | Humidification device for blasting to blast furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18078482A JPS5970703A (en) | 1982-10-15 | 1982-10-15 | Humidification device for blasting to blast furnace |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5970703A true JPS5970703A (en) | 1984-04-21 |
Family
ID=16089262
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP18078482A Pending JPS5970703A (en) | 1982-10-15 | 1982-10-15 | Humidification device for blasting to blast furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5970703A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106423609A (en) * | 2016-11-04 | 2017-02-22 | 赫曼(南京)机械技术工程有限公司 | Super atomizing and dust-falling device |
JP2018133169A (en) * | 2017-02-14 | 2018-08-23 | 東京瓦斯株式会社 | Fuel cell system |
CN113471487A (en) * | 2021-06-30 | 2021-10-01 | 潍柴动力股份有限公司 | Hydrogen fuel cell humidifying system and humidifying method |
-
1982
- 1982-10-15 JP JP18078482A patent/JPS5970703A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106423609A (en) * | 2016-11-04 | 2017-02-22 | 赫曼(南京)机械技术工程有限公司 | Super atomizing and dust-falling device |
JP2018133169A (en) * | 2017-02-14 | 2018-08-23 | 東京瓦斯株式会社 | Fuel cell system |
CN113471487A (en) * | 2021-06-30 | 2021-10-01 | 潍柴动力股份有限公司 | Hydrogen fuel cell humidifying system and humidifying method |
CN113471487B (en) * | 2021-06-30 | 2022-07-15 | 潍柴动力股份有限公司 | Hydrogen fuel cell humidifying system and humidifying method |
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