JPS5913652A - Cement manufacture and device utilizing blast furnace molten slag - Google Patents
Cement manufacture and device utilizing blast furnace molten slagInfo
- Publication number
- JPS5913652A JPS5913652A JP57123689A JP12368982A JPS5913652A JP S5913652 A JPS5913652 A JP S5913652A JP 57123689 A JP57123689 A JP 57123689A JP 12368982 A JP12368982 A JP 12368982A JP S5913652 A JPS5913652 A JP S5913652A
- Authority
- JP
- Japan
- Prior art keywords
- molten slag
- cement
- blast furnace
- furnace
- molten
- 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.)
- Granted
Links
- 239000002893 slag Substances 0.000 title claims description 93
- 239000004568 cement Substances 0.000 title claims description 53
- 238000004519 manufacturing process Methods 0.000 title claims description 29
- 238000001354 calcination Methods 0.000 claims description 25
- 239000002994 raw material Substances 0.000 claims description 24
- 238000010304 firing Methods 0.000 claims description 16
- 239000007921 spray Substances 0.000 claims description 13
- 238000005507 spraying Methods 0.000 claims description 9
- 239000000203 mixture Substances 0.000 claims description 6
- 238000000034 method Methods 0.000 claims description 5
- 238000009628 steelmaking Methods 0.000 claims description 4
- 239000003595 mist Substances 0.000 claims description 2
- 239000004575 stone Substances 0.000 claims 1
- 239000002245 particle Substances 0.000 description 6
- 238000010586 diagram Methods 0.000 description 4
- 239000000446 fuel Substances 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 235000019738 Limestone Nutrition 0.000 description 2
- 241000209094 Oryza Species 0.000 description 2
- 235000007164 Oryza sativa Nutrition 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 235000013339 cereals Nutrition 0.000 description 2
- 239000004927 clay Substances 0.000 description 2
- 230000004927 fusion Effects 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000006028 limestone Substances 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 235000009566 rice Nutrition 0.000 description 2
- 238000005245 sintering Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 241000257465 Echinoidea Species 0.000 description 1
- 241000237858 Gastropoda Species 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 235000020094 liqueur Nutrition 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000004071 soot Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
Classifications
-
- 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
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/10—Production of cement, e.g. improving or optimising the production methods; Cement grinding
Landscapes
- Curing Cements, Concrete, And Artificial Stone (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
本光明は、高炉スラグを一しメン1−の副原オ′31ど
して利用づるセメン1〜の製造方法J5よO・その装置
(ご関り−るものである。DETAILED DESCRIPTION OF THE INVENTION The present invention describes a method for producing cement 1~ using blast furnace slag as an auxiliary raw material for cement 1~ and its equipment (for those involved). be.
周知のように製鉄高炉からは、その運転に1′1′つ(
約1/loo″Cの高炉溶融スラブか4〕1出されてい
る。この高炉溶融スラブは、従来徐冷スラグ、急冷スラ
グ等どしく、例えばセメン1−製造の副原石等各号面で
利用されているが、その顕然の回収どなると一部で発電
等に利用されている他には、充分に有効利用されていな
いのが現状である。As is well known, a steelmaking blast furnace requires 1'1' for its operation.
A blast furnace molten slab of approximately 1/loo"C is produced. This blast furnace molten slab is conventionally used as slowly cooled slag, rapidly cooled slag, etc., and is used for various purposes such as secondary raw material for cement production. However, when it comes to actual recovery, it is currently not being utilized effectively enough other than in some areas for power generation and other purposes.
本発明は、上記事情に鑑みてなされたもの−(、製1ス
高炉の溶融スラグの有しCいる熱的−1ネル−1′−一
を有効利用C′さるしメン1〜の製造方法及び装置を提
II’りることを目的どJるものCある。The present invention has been made in view of the above-mentioned circumstances. There are also some devices that are designed to provide equipment.
本発明の高炉溶融スラグを利用づるセメン1への製造方
法は、製釦、高炉から制用され<)6炉溶融スラグを、
溶融スラグ移送路を通しくL!メン1〜製造設備に導さ
、前記高炉溶融スラグを同セメン1〜製造設猫の予熱工
程、仮焼工程または焼成工程で、セメン1〜原料(石灰
石、粘土等からなる)に足場的に噴霧し−(、前記溶融
スラグをセメント原オ′」ど混合し、しって前記溶融ス
ラグの顕熱を前記しメン1〜原籾に与えてセメント製造
工程にJ3ける予熱用熱、仮焼用熱J、たは焼成用熱の
一部としC有効利用づるようにしたことを特徴とりるも
のである。The method for manufacturing cement 1 using blast furnace molten slag of the present invention can be used from button making and blast furnaces.
L through the molten slag transfer path! The blast furnace molten slag is introduced into the cement 1 production equipment and sprayed onto the cement 1 raw materials (consisting of limestone, clay, etc.) in the preheating, calcination, or firing process of the production equipment. (The molten slag is mixed in a cement raw oven, and then the sensible heat of the molten slag is applied to the raw rice grains for preheating and calcination in the cement manufacturing process J3. It is characterized by the fact that heat J or C can be effectively used as part of the heat for firing.
2した本発明のしメン1〜製造”A !i′l°は、製
υ、1r:1炉の溶融スラグIJI出口どセメント製4
’+’i設置d11どの間に、溶融スラグ移送路を設(
〕ると共に、同溶融スラグ移jス路の一喘部に前記セメ
ン1へ製j冑設置拍の予熱器、仮焼炉または焼成炉の内
部もしくはこれら予熱器、仮焼炉または焼成炉にセメン
ト原)’j+を導入覆るためのダウ1〜内部へ、前記溶
融スー、ツクを足場的に噴霧するための噴B装置を設り
、しメント朋)’1と溶融スラグどを混合しで溶h1!
スングの右りる顕熱を予熱用熱、仮焼用熱または焼成用
熱の一部として有効利用(JるJ、−)にしたことを特
徴どりるものCある。2 of the present invention 1 ~ Manufacture ``A!
'+' i Installation d11 Set up a molten slag transfer path (
] At the same time, a preheater, a calcination furnace or a sintering furnace, or a cement is installed in a part of the molten slag transfer path to the cement 1. 1) Introducing ``j+'' A spray B device was installed to spray the molten soot and slag into the inside of Dow 1 to cover the interior. h1!
There is C, which is characterized by effectively utilizing the sensible heat of the heat as part of the heat for preheating, heat for calcination, or heat for firing (JruJ, -).
1ス干、本発明を図面を参照しく説明りる。First, the present invention will be explained with reference to the drawings.
第1図は、本発明のしメン1ル製j閂装首の一実施例を
示づ図である。この図中貿月1は、製鉄高炉、2にルメ
ン1〜製造設備である。FIG. 1 is a diagram showing an embodiment of the bar-neck made of one piece of steel according to the present invention. In this figure, trade number 1 is the steelmaking blast furnace, and number 2 is the manufacturing equipment.
まず、概略構成を説明りるど、^°S1力11は、通常
その運転時に定期的に高炉溶融スラグかIJI出され−
るらので、その上部に溶融スラグiJI fli IT
I 18を(R^えでいる。まIこ、レノン1〜製j貫
設(#++ 2は、す【クロン予熱器38〜・3c、分
離]j″イク]」ン1、仮焼炉5及び[]−タリーキル
ン6等をIWf+えた周知の構成よりなるものCある。First, to explain the general configuration, the S1 force 11 normally discharges molten blast furnace slag or IJI periodically during its operation.
Since it is Rura, there is molten slag on top of it.
I 18 is installed (R^). Also, Lennon 1~J penetration (#++ 2 is [Chron preheater 38~・3c, separation] j'')'n 1, Calcining furnace 5 and []- tally kiln 6, etc. are included in the well-known structure C.
イして、前記高炉10刊出口18と前記ロータリーキル
ン6の窯尻6aどの間には、溶融スラグ移送路8が設り
られ−Cいる。A molten slag transfer path 8 is provided between the outlet 18 of the blast furnace 10 and the bottom 6a of the rotary kiln 6.
この溶融スラグ移送路8は、その中間部に溶811スラ
グ貯留容器9を備えている。また、溶融スラブ移送路8
の1]−タリーキルン6側の端部には、溶融スラグをロ
ータリ−キルン6内部に噴霧づるI〔めの噴霧装置10
が設けられている。This molten slag transfer path 8 is equipped with a molten 811 slag storage container 9 at its intermediate portion. In addition, the molten slab transfer path 8
1] - At the end of the rotary kiln 6 side, there is a spray device 10 for spraying molten slag into the rotary kiln 6.
is provided.
前記溶融スラグ移送路8及び噴霧装置10について更に
詳しく説明する。前記溶融スラブ移送路8の中間部に設
【プられた溶融スラグ貯留容″a9は、例えば第2図に
承りように中空円柱状に形成されたちのC”あっ−C1
その壁部9aが耐火・断熱性の保温壁どなつCいる。こ
の溶融スラグ貯留容?!A9の上部には、高炉1の排出
l’l 1 a 7+1 +ら延びるり]1の移送管路
8aが接続されると共に、下部には、ロータリーキルン
6に延びる第2の移送管路8bと、余剰スラグを+Jl
出するための排出管路18どか接続されている。これら
第2の移jス管路ε3と排出管路18とには、ぞれぞれ
の色路を間開するためのダンパ19.20が設(プら4
1. ’(いる。;また、−溶融スラグ貯留容器9の側
壁土部に(、L、溶融スラグの貯留部を検出Jるための
レンリ2′1が設置′Jられでいる。ぞし−(、このレ
ンリ21の出力に基いてレヘル−:」ン1ヘローラ22
により1ノ1出管路18のダンパ20を間開し、溶融ス
ラグ貯留部器0内部の溶融スラグを所定f1に保つJ、
〕になつ(いる。The molten slag transfer path 8 and the spray device 10 will be explained in more detail. The molten slag storage capacity "a9" installed in the middle part of the molten slab transfer path 8 is, for example, a hollow cylinder shaped as shown in FIG.
The wall portion 9a is a fireproof and heat insulating wall. This molten slag storage capacity? ! A 1 transfer pipe 8a extending from the discharge port of the blast furnace 1 is connected to the upper part of A9, and a second transfer pipe 8b extending to the rotary kiln 6 is connected to the lower part. Extra slag +Jl
It is connected to a discharge pipe 18 for discharging the water. These second transfer pipe line ε3 and discharge pipe line 18 are provided with dampers 19 and 20 for spacing the respective color paths.
1. (There is.; Also, - on the side wall soil part of the molten slag storage container 9, a receptacle 2'1 for detecting the molten slag storage part is installed. Based on the output of this Renri 21,
The damper 20 of the 1-1 outlet pipe 18 is opened to maintain the molten slag inside the molten slag storage unit 0 at a predetermined value f1,
]Natsu (there.
この溶溶融スラグ貯留部器9ユ、同容器9内の高力J溶
融スラグの貯留バ)を調整し、しメン1〜製造設置l1
ii 2への高炉溶融スラグの供給14′!及0記度(
7)調整を行’7′にう機能を有りるbのである。Adjust the molten slag storage unit 9 and the storage bar for high-strength molten slag in the same container 9, and then
ii Supply of blast furnace molten slag to 2 14'! and 0 degrees (
7) There is a function to perform adjustment '7'.
また噴霧装置10どしては、1911えばり〕3図に承
りような装置が使用される。、この噴貨装置首10は、
その噴出口10aが先端部に向()(開さ、中間部に股
部1011か形成されるとJI、に、股部10 bに向
(〕て溶融スラグを導入づる第2の移送管路81)が接
続されCなるものである。また、この噴霧装置F’?
10の11@出1’110aと反対側には、給気管23
が接続されCいる3、この給気管23には、での一端部
に]ンプレッサ24に接続されると共に、中間部に熱交
換器25が介挿され−Cいる。熱交換器25には、前記
第1の移送管路8aの中間部で分岐された排出管路26
と前記溶融スラグ貯留容器9から延びる排出管路18と
が合流されたうえで接続され、高炉1から排出される溶
融スラグの初期流出分と溶融スラグ貯留部′I59の余
剰な溶FAl!スラグどが導入されるようになっている
。Further, as the spray device 10, a device as shown in Fig. 3 of the 1911 edition is used. , this ejection device neck 10 is,
When the spout 10a is opened toward the tip and a crotch section 1011 is formed in the middle section, a second transfer pipe is introduced into which the molten slag is introduced toward the crotch section 10b. 81) is connected to C. Also, this spray device F'?
11 of 10 @ On the opposite side from exit 1'110a, there is an air supply pipe 23
The air supply pipe 23 is connected to a compressor 24 at one end thereof, and a heat exchanger 25 is inserted in the middle thereof. The heat exchanger 25 includes a discharge pipe 26 branched at the middle of the first transfer pipe 8a.
and the discharge pipe 18 extending from the molten slag storage container 9 are merged and connected, and the initial outflow of molten slag discharged from the blast furnace 1 and the excess molten FAl in the molten slag storage part 'I59! Slugs are being introduced.
上記の構成のちとに、噴霧装置10には溶融スラグ貯留
容器9から溶融スラグが定量的に送られると共に、]ン
ブレッ4j24− tこより圧送され、熱交換器25で
高温溶融スラグと熱的に接触しCシ?温された空気か給
気管23を紅で供給される。そして噴出しl 10 ;
iからロータリ−キルン6内部に向(プて高温の溶融ス
ラブが空気を噴霧媒体どして噴霧されるJ、うになっ−
Cいる3、
しかし−(、」二記のセメント製造装置にa3いC1原
′Ai1投入装首2ε3から投入された石灰イj、シリ
カ分を含む粘土等のセメン1へ原料は、第1の4ノイク
[1ン予熱器3aど第2のリイク11ン子熱器31+ど
の間を連結するタクト29aに送り込、1れ、高i品の
気流中を搬送されC1;熱さft−:)つ第1のリーイ
クロン予熱器3aに導入される。この第1の→ノイク]
=1ン予熱器3aC高温気体と分離されたしメン1へ原
料は、同様にして第2、第J3のリイクUン子熱器3b
、3cを経てY熱され、仮焼)、7I!11に送り込ま
れる。仮焼炉5では一1重油、(j炭なとの燃料をバー
ノー5aににり燃焼させて、セメン1゛・原料の予熱と
仮焼とを行なう。仮焼後のセメン1へ原料は、分離1す
、イタ+1ン4に送られ、気休ど分冊され(Ll−タリ
ーキルン6の窯尻6Cに送り込J、れる。また、高)晶
気体(は、タリ1〜29J]−290を通しでリイクロ
ン予熱器3 a、・3Cにjス1うれ、セメント原お1
の予熱に使用される1゜
一方、高炉1から排出される溶融スラグのうち、ぞの初
期流出分は、温度が低いためJul出艙・路26を通し
、熱交換器25を経て徐6)ヤー1−り図示せり゛)等
l\送られる3、まIご1Q温の溶融スラグは、溶融ス
ラグ貯留容器9内部へ導かれる。この溶融スラグ貯留容
器9内部には、溶融スラグの一部が貯留されると共に、
所定量がダンパ19により宙吊されで噴霧装置10に送
られる。イしC1この11【1霧装置10から高温、高
圧の空気を噴霧媒体とし−Cロータリーーー1ルン6内
部のレシシト1京判に噴霧、混合される。噴霧装置10
から噴霧された溶融スラグは、前記セメント原料に混合
され、これにJ、り溶融スラグが有していた顕然はけメ
ン1へ原料に与えられ(焼成用熱の一部として利用され
る。また、上記溶融スラブは、ロータリーキルン6の入
口近傍′Cしメン1〜原お1層の上に散布されるが、ロ
ータリーキルン6人口では原料が粉状で′あり、かつし
メン1ル原オ′31層表面は、ロータリーキルン(3の
回転に伴って常に攪拌、更新されるため、噴霧された溶
融スラグのJ!Ifiによるスラグ粒子間の再融着が防
止される。ロータリ−キルン6内部′C沢合されたレシ
ン1−原オ′31と高炉スラグは、焼成され(セメント
クリカーを形成し、タリンカークーラ30に送られる。After the above configuration, the molten slag is quantitatively fed from the molten slag storage container 9 to the spraying device 10, and is also pressure fed from the boiler 4j24-t, and is brought into thermal contact with the high-temperature molten slag in the heat exchanger 25. Shi C Shi? Warmed air is supplied through the air supply pipe 23. and squirt l 10 ;
The high-temperature molten slab is sprayed from i to the inside of the rotary kiln 6 using air as an atomizing medium.
C3, but-(,') The raw materials for cement 1, such as lime and clay containing silica, which were input from the input neck 2ε3 into the cement manufacturing equipment described in 2, were The heat is sent to the tact 29a connecting between the 4-noise preheater 3a, the 2nd re-heater 31, and the 11-inch heater 31+which is transported through the airflow of the high-quality product C1; heat ft-:). It is introduced into the first Lee ICron preheater 3a. This first → Noik]
=1 N preheater 3aC The raw material is separated from the high temperature gas and sent to the second heater 1 in the same way as the second and J3 reheater 3b.
, 3c, heated to Y, and calcined), 7I! Sent to 11. In the calcining furnace 5, fuel such as 11 heavy oil (J) and charcoal is burned in the burnout 5a to preheat and calcinate the cement 1 raw material.After calcining, the raw material is transferred to the cement 1. Separation 1 is sent to Italy + 1 to 4, and divided into volumes (Ll - sent to the bottom 6C of Tally kiln 6. Also, high) crystal gas (Tari 1 to 29 J] -290 Through the Reikron preheater 3 a, 3C, j su 1, cement field o 1
On the other hand, the initial outflow of the molten slag discharged from the blast furnace 1 passes through the Jul outlet port/channel 26 and the heat exchanger 25 due to its low temperature. The molten slag at a temperature of 1Q is guided into the molten slag storage container 9. A part of the molten slag is stored inside this molten slag storage container 9, and
A predetermined amount is suspended by a damper 19 and sent to the spray device 10. High-temperature, high-pressure air is used as a spraying medium from the mist device 10 and is sprayed and mixed onto the 1 quintillion-sized receipt inside the rotary 6. Spray device 10
The molten slag sprayed from the molten slag is mixed with the cement raw material, and then the molten slag is given to the raw material to the heat sink 1 (used as part of the heat for sintering). In addition, the molten slab is sprayed on the raw materials 1 to 1 in the vicinity of the entrance of the rotary kiln 6, but in the rotary kiln 6, the raw material is in powder form, The surface of layer 31 is constantly stirred and renewed as the rotary kiln (3) rotates, thereby preventing re-fusion between slag particles due to J! Ifi of the sprayed molten slag. The mixed resin 1-raw material 31 and blast furnace slag are fired (forming cement liqueur) and sent to the coal cooler 30.
一方、[]−]タリー二1ルン6内に哨’i’A’J1
体とし(送り込まれた空気は、高温用の 次空気どして
焼成炉6及び仮焼炉!□5t“r ”r、Ll、aられ
、予熱、仮焼及び焼成に用いられる1゜
−に記のJ、うなセメントの製造方法及び装置によれば
、従来セメンiへ製造の副舵オ′+1としく徐冷スラグ
、急冷スラグ等の状態で使用されでいた高炉スラグを高
温の溶融状態でセメンl−1i1 JUIに噴霧、混合
づるようにしたため、高炉から[1出された溶ハ(1ス
ラグのbつ人fi5の熱的1ネル1−4レメン1−!ル
(J+1及び7−次空気に句え(有効に利用刀ることが
(・さる。また、上記の溶融スラグの顕然回収に伴・っ
(、しメン1へ製造設備の消費燃才11を減少し、コス
1〜の低減をも図ることかC゛る。史には、溶融スラブ
が噴霧され、微粒子化されCセメン1−原1’lと均に
混合されるのC゛、Ij;l:1被1) 4’+’ l
’l (1) III 下ヤ’ ソhに1゛1′うセメ
ントクリンカーのテ11焼f’l及び設備への悪影v1
智を防J(でき、これによりt、L求lノメン1−11
〜ンあlこり100へ・150kCIにおさえられCい
た+!’L力1スラグの添加量を、門通ボルトノン1〜
レメントの場合340−350 kgとすることかひき
る。On the other hand, there is a sentry 'i'A'J1 in []-] Tally 21 run 6.
(The injected air is passed through the high-temperature secondary air to the firing furnace 6 and the calcining furnace! According to J, the method and apparatus for producing eel cement, blast furnace slag, which had previously been used in the form of slowly cooled slag, rapidly cooled slag, etc., as a sub-rudder o'+1 in the production of cement i, is molten at a high temperature. Since the cement was sprayed and mixed with JUI, the molten metal discharged from the blast furnace (1 slag of 1 molten metal, 1 mol of fi5, In addition, with the obvious recovery of the molten slag mentioned above, the fuel consumption of manufacturing equipment is reduced by 11, and the cost is reduced by 1 to 1. In the past, the molten slab was sprayed, atomized, and evenly mixed with C cement 1-1'l. 4'+'l
'l (1) III Lower 'The cement clinker's 11th grade f'l and the negative impact on the equipment v1
Prevent Wisdom from J
〜NAlkori 100・C was suppressed to 150kCI+! 'L force 1 slag addition amount, Mondori bolt non 1 ~
In the case of lemento, the weight should be 340-350 kg.
本発明等の試粋によれば、セメント11ヘンあたりの高
炉溶融スラグ1が3/lo〜350 kgどなるように
キルンに投入した場合、溶融スラグ増量に伴う石灰石原
単位減少く換言づれば、l1ri籾分解に要求される熱
印の減少)を考慮して、溶融スラグ)411度が140
0℃でセメン1ヘクリン力−1kc+あたり約140キ
ロカロリー、1200 ”Cc約120−Iロカロリー
の焼成熱減少を図ることができる。According to the essence of the present invention, when molten blast furnace slag 1 per 11 hectares of cement is charged into the kiln at a rate of 3/lo to 350 kg, the unit of limestone decreases as the amount of molten slag increases, in other words, 1ri rice grains Taking into account the reduction in heat stamp required for decomposition, the molten slag) from 411 degrees to 140 degrees
At 0° C., it is possible to reduce the firing heat by about 140 kilocalories per 1 kc+ of cement, or about 120 kcal by 1200"Cc.
また、第4図は、本発明のけメン1ル製造具首の別の実
施例を示ず図である。この図中、第1図と同一構成要素
には、同−行目をイqしてその説明を省略づる。Further, FIG. 4 is a diagram without showing another embodiment of the neck of the stub-manufacturing tool of the present invention. In this figure, components that are the same as those in FIG.
第4図に示すセメント製造装置が第1図に示づものと異
なる点は、噴霧装置31が、クリンカークーラ30ど、
仮焼炉5との間を連結4るダクト32の中間部に設(プ
られCいる点である。The cement manufacturing apparatus shown in FIG. 4 is different from the one shown in FIG.
This point is installed in the middle of the duct 32 that connects the calcining furnace 5 with the duct 32.
プなわら、第55図に承りように、仮焼炉5の下部に連
結にされたダクト32にリイクロン予熱器3Cからセメ
ン1−原石を導入するための原わ1シユー1〜33が連
結される共に、ダクト32の原オ′31シ]−h 33
の聞1−1部33aと仮焼炉(5どの間に噴fIi装置
31がシ旧)られでいる、。Meanwhile, as shown in FIG. 55, the ducts 32 connected to the lower part of the calcining furnace 5 are connected to the raw water 1 shows 1 to 33 for introducing cement 1-ore from the Reikron preheater 3C. At the same time, the original o'31 of the duct 32]-h 33
The injection fIi device 31 is installed between the 1-1 part 33a and the calcining furnace (5).
−1−記の474成にa3い(、DJjΔ”l > r
i 433を軽(タクト32内に投入されるヒメン
ト1京オ′;1は、クリンカークーラ30がら送)It
される5流中Cかj役しつつ、仮焼炉5内部に向けて送
られる。そしてこのセメン]へ原わ1には、++15霧
装置31にj、り溶融スラグが噴霧、混合され、溶融ス
ラグの顕熱が勺えlうれる1、史に、スラグとセメンl
−13i! J’lどの混合物は、1反焼炉5内部に送
り込まれ、乱流により攪拌、混合されつつバーt 5
i+によりSly焼され、次いC【−1−タリー−1:
ルン6に送られ焼成される。-1- 474 composition a3 (, DJjΔ”l > r
i 433 as a light (1 million yen of heat input into the tact 32; 1 is sent from the clinker cooler 30) It
It is sent toward the inside of the calcining furnace 5 while acting as C or J in the 5 streams. Then, molten slag is sprayed and mixed in a ++15 fogging device 31 into the cement raw material 1, and the sensible heat of the molten slag rises.
-13i! The mixture is fed into the inside of the incinerator 5, where it is stirred and mixed by turbulent flow and passed through the bar t5.
Sly fired by i+, then C[-1-Tally-1:
It is sent to Run 6 and fired.
−1,記のJ、うなヒメント製造装置にJ、れば、溶融
スラグの右づる顕熱か仮焼炉5前段のダクト32でロメ
ント原邪1【こIjえられるlこめ、1反焼に乃りろ熱
ifの節減を図ることがてさる。史(ごは、11−タリ
ーキルン6に導入されるス)りとセメン1−原わ1どの
混合物が、仮焼炉5内部て乱流にJ、り完全に混合され
ているため、その均−II[か高く、[1−タリーキル
ン6ての焼成士11が向」−ツる。-1, If the J of the above is used in the eel heat production equipment, the sensible heat of the molten slag or the duct 32 in the front stage of the calcining furnace 5 will cause the heat of the molten slag to be heated. It is important to try to reduce Noriro Netsu if. The mixture of raw material, cement, and raw material introduced into the 11-tally kiln 6 is completely mixed in the turbulent flow inside the calciner 5, so that the mixture is not evenly mixed. II [Kakataka, [1-Tally kiln 6 firing staff 11 are facing] - Tsuru.
なお、第4図に示づセメント製造装置7にJ3いC1仮
焼炉5前段のダクト32への原第′)1シー1−1・3
33及び噴霧装置31の配設構造を、第6図、または第
7図に承り構造とづることもできる。第6図に承り構造
は、ダク1−32に対して斜交づるJ、うに固定された
原オ′81シューi〜33の基部に、噴霧装置31が・
ての噴出口31aをタクト32内部を向り−C設りられ
たものである。また第7図に示づ構造は、ダク1へ32
に対して略直角に固定された原簿31輸送管(原料シュ
ー1− ) 33の内部の基部近傍に噴霧装置31を同
軸的に設け、その1ltl f、HIJ 31 aをタ
フ1〜32内部に向りて設訂したしのである。In addition, the cement production equipment 7 shown in FIG.
33 and the arrangement structure of the spray device 31 can also be referred to as a structure similar to that shown in FIG. 6 or 7. As shown in FIG. 6, the spraying device 31 is attached to the base of the shoe I-33, which is fixed to the duct 1-32 at an angle to the duct 1-32.
The two spout ports 31a are provided facing the inside of the tactile chamber 32. In addition, the structure shown in FIG.
A spray device 31 is installed coaxially near the base inside the transportation pipe (raw material shoe 1-) 33, and its 1ltl f and HIJ 31a are directed toward the inside of the toughs 1 to 32. It was revised by
第6図に承り構造においては、ダグ1〜32内に向IJ
て噴霧された溶融スラグが原オ′81シー1−1〜33
を流上りる原J’l Rと衝突し、熱交換される1、こ
の際、スラブ粒子は、失速して粒子間に衝突が起こるが
、900 に稈麿以上の温度であれは融着を起こす恐れ
はない。また、多少融着が起さ′Cも原料層と衝突した
溶融スラグ粒子表面に他の原料粒子も(=J着し−Cく
るため、原料組成は均一となっC口−クリー1ルン6内
部r ff111焼成11どなる克(れはない。In the receiving structure shown in Fig. 6, there is a direction IJ in Doug 1 to 32.
The molten slag sprayed by
The slab particles collide with the flowing raw material J'lR and undergo heat exchange1.At this time, the slab particles stall and collisions occur between the particles, but if the temperature is above 900℃, fusion will not occur. There's no danger of it happening. In addition, some fusion occurs and other raw material particles also adhere to the surface of the molten slag particles that have collided with the raw material layer (=J - C), so the raw material composition becomes uniform and the inside of C-Cree 1 Run 6 r ff111 firing 11 there is no such thing.
また、第7図に承り構造に、1夕い(は、原料輸送管3
3中を移送されル、ffi j)(r、+ ’=9 (
J) I= メントII’、iオ′31ハ、噴霧装置ν
i3’lの周りに導かれ、11(°コ霧駅f!!’!”
331がら噴霧される溶融スラグと気流中(速かに効率
良く混合されたうえでタクト32内に導かれる。In addition, the structure shown in Fig. 7 is shown in Figure 7.
3, ffi j) (r, + '=9 (
J) I=ment II', io'31c, spray device ν
Guided around i3'l, 11 (°Kogiri Station f!!'!”
The molten slag sprayed from 331 is mixed quickly and efficiently in the air stream, and then introduced into the tact 32.
これらのような構造にJ、れば、しメント原料ど溶融ス
ラグとの混合効率を高めることができ、焼成炉にJ−3
1jる焼成性を損うことがイ【い。If J-3 has a structure like these, it is possible to increase the mixing efficiency with molten slag such as cement raw material, and it is possible to increase the mixing efficiency with J-3 in the firing furnace.
It is impossible to impair the firing properties.
なお、上記実施例においCは、昌炉溶融スラグ’a仮焼
炉及ヒ焼成炉でセメン+−D;t J:jlにl!(、
! ’IA、)12合りる例(ごついて説明したか、こ
41.らの実部1例に限ることなく予熱器または分離リ
イク[JンCレメン1〜18;【オ;1に噴霧、)I4
合りるΔ、うにしCらJ、い。In addition, in the above embodiment, C is cement +-D; t J: l in jl! (,
! 'IA,) 12 examples (I have explained the roughness, but these 41. are not limited to the real part 1 example, but are not limited to the preheater or separation leak [J&C Remen 1 to 18; [E; )I4
It fits Δ, sea urchin C and J.
以」−1詳細に説明したJ、うに、本発明にJ、る高炉
溶融スラグを利用りるセメン1〜の製造/’J 71<
A; J、び装置は、製鉄高炉の溶融スラグ01 r
l; IJとセメンl−製造設備どの間に溶融スラブ移
′Jλ路を設(づるどJj、に前記セメント製j貴設廂
の予熱器、仮焼炉または焼成炉、もしくはこれらの炉の
いり゛れかの前段のダク1へ(゛、前記溶融スラグ移送
路を搬送された溶用lスラグを1rj霧装置によりセメ
ント1京料に噴霧、混合し、もって従来しメン1〜製迄
の副舵オ′;1としC使用され(いた溶融スラグを11
温の溶融状態Cセメン(−製造」−程中に導き、その顕
熱を予熱用熱、仮焼用熱または焼成用熱の一部として利
用りるJ、うにしたから、従来充分な回収がなされ(い
なかつl〔高炉溶融スラグのもつ入量の熱的1ネル4゛
−を有効に利用することができ、かつセメン1〜製造設
備の必要とりる熱量の低減、りなわlう燃料の節減を図
ることができる。また、これに伴つCセメント顎造」ス
1〜の低減を図ることができる。史【こ、前記溶融スラ
グを、しメン1−製造設備の仮焼炉内部または同仮焼炉
の前段のダグ1〜rtメン1〜15:’! Flに噴霧
、混合りることにより、仮焼炉内部でセメン1−原オ:
81とスラグとが充分に混合され、均一化りるため、焼
成炉内部にてより易焼成性とり−ることができる等の効
果を秦づるしの(ある。71<
A; J, and the equipment is molten slag 01
l; A molten slab transfer path is installed between the IJ and the cement manufacturing equipment. The molten slag conveyed through the molten slag transfer path is sprayed and mixed with the cement material by the 1rj atomizer to the duct 1 in the previous stage of the duct 1. Rudder O'; 1 and C were used (melted slag was 11
The sensible heat is brought into the molten state C cement (-manufacturing) during the process, and the sensible heat is used as part of the heat for preheating, heat for calcination, or heat for firing. It is possible to effectively utilize the input thermal energy of blast furnace molten slag, reduce the amount of heat required for cement manufacturing equipment, and increase the amount of fuel required. In addition, it is possible to reduce the amount of C cement jaw construction. By spraying and mixing with Fl, cement 1-1-15 in the previous stage of the calcining furnace:
Since the 81 and the slag are sufficiently mixed and homogenized, the slag can be fired more easily inside the firing furnace.
第1図は、ホット明の 実施例を示り慨I18構成図、
第2図は、溶融スラク貯(イイ容器の一例庖示!I断面
図、り13図は、噴霧装置の一例を示づlDi而図面第
4図は、本発明の別の実施例を示り(1((略構成図、
第り図はセメン1〜製j青設置イ^l\の11C)極装
置rイの設置i部分の構造の一例を承り断面図、第0図
、第7図は、同構造の他の例を/J’% リ匹面図(・
ある1゜1・・・・・・製鉄高炉、1a・・・・・・溶
81(スラグ抽出L1.2・・・・・・セメント製j六
設備、5〕・・・・・・仮力1・1炉、6・・・・・・
焼成炉(ロータリーキルン)、E3・・・・・・溶融ス
ラグ移送路、ε3a・・・・・・第1の移送管路、81
)・・・・・・第2の移送管路、9・・・・・・溶融ス
ラグ貯留容器、10.31・・・・・・噴霧装置、10
a、31a・・・・・・110出1’、I 、−19,
20・・・・・・タンパ、23・・・・・・給気?2.
24・・・・・・−1ンゾレツリ−12巳)・・・・・
・熱交換器、32・・・・・・グク1−133・・・・
・・原料シ+−1−a第5図
第6図Figure 1 shows an example of the hot light I18 configuration diagram;
Figure 2 shows an example of a container suitable for storing molten slurry. Figure 13 shows an example of a spraying device. Figure 4 shows another embodiment of the present invention. (1((schematic configuration diagram,
Figure 2 is a cross-sectional view of an example of the structure of the installation part i of the 11C) pole device r, manufactured by Cement 1~, and Figures 0 and 7 are other examples of the same structure. /J'%
1゜1... Steelmaking blast furnace, 1a... Molten 81 (slag extraction L1.2... Cement j6 equipment, 5)... Temporary force 1.1 furnace, 6...
Calcining furnace (rotary kiln), E3... Molten slag transfer path, ε3a... First transfer pipe, 81
)... Second transfer pipe line, 9... Molten slag storage container, 10.31... Spraying device, 10
a, 31a...110 out 1', I, -19,
20...Tampa, 23...Air supply? 2.
24...-1 Nzoretsuri-12)...
・Heat exchanger, 32...Guku 1-133...
・・Raw material +-1-a Figure 5 Figure 6
Claims (1)
ラブ移送路を通してセメンl−’In造設備に導さ、前
記高炉溶融スラグを前記セメンI−少1 込設置!tf
iの予熱工程、仮焼1稈または焼成工程でUメン1〜原
N’ilに定量的に噴霧、混合し、前記高炉溶t、6i
スラグの顕熱を前記セメンl−原料に与えるようにした
ことを特徴とする高炉溶融スラグを利用りるセメンl〜
の製造方法。 2、前記溶融スラブ移送路が、中間部に溶融スラブ貯留
容器を備え、この溶融スラグ貯留容器に導入される前記
高炉溶融スラグのうら所定鉛が前記しメン1−製造設備
に導かれ、残部が貯留または1ノ1出されるにうにした
特う′[請求の範囲第1項記載の高炉溶融スラグを利用
づるセメン1−の製造方法。 3、前記焼成工程がロータリーキルンによりなされ、前
記高炉溶融スラグが前記ロータリーキルン内部に噴霧さ
れるようにした特許請求の範囲第1項または第2項記載
の高炉溶融スラグを利用づるヒメントの製造方法。 4、前記仮焼上程が気流炉式仮焼炉によりなされ、前記
高炉溶融スラグが前記仮焼炉内部もしくは仮焼炉入口近
傍のダク1へ内部に噴霧されるようにした特許請求の範
囲第1項または第2項記載の高炉溶融スラグを利用する
セメン1−の製造方法。 5、製鉄高炉の溶融スラブ刊出口と廿メント製造設備と
の間に、溶融スラグ移送路を設けると共に、この溶融ス
ラグ移送路の一端部に、前記セメンl−製造設備の予熱
器、仮焼炉または焼成炉の内部もしくは、これら予熱器
、仮焼炉または焼成炉にセメン1〜原石を導入づるダク
トの内部へ前記高炉溶融スラグを定量的に噴霧りるため
の噴霧′!A置を設けてなる高炉溶融スラグを利用づる
セメン1−の製造装置。 6、前記溶融スラグ移送路が、中間部に溶融スラグ貯留
容器を1禎え−(なる4ゼj l、’l :+i’j求
の範囲第5Jj’1記戦の高炉溶融スラグを利用づるセ
メン1〜の製造具IC1“。 7、前記焼成炉がLl−タリー1ルン(゛あって、前記
噴霧装置の口0出口がOrl記II 、−タリーキルン
内部に向(](設置され−U イ、−る乃^′11iI
′l求の範囲第5)項ま/、:は第6項記載の高炉溶融
スラグを利用づ−るセメン1−の製造装置。 8、前記仮焼炉が気流炉式仮焼炉であって、前記11.
r1霧装置の噴出にLlが前置仮焼炉内部31、たは同
板焼炉ヘセメント原料を導入するためのグクト内部に向
fノー’C設置サレT ’J ルq’!J R’l”=
6求の範囲第5 Jj’jまたは第6項記載の高炉溶融
スラグを利用りるセメン!〜の製造装置。[Claims] 1. The blast furnace molten slag discharged from the iron-making blast furnace is guided to the cement I-'In production equipment through the molten slab transfer path, and the blast furnace molten slag is installed in the cement I-In production facility! tf
In the preheating step, calcination 1 culm or firing step of i, quantitatively spray and mix on Umen 1 to raw N'il, and add the blast furnace melt t, 6i
Cement l~ using blast furnace molten slag, characterized in that sensible heat of the slag is imparted to the cement l~ raw material
manufacturing method. 2. The molten slab transfer path is provided with a molten slab storage container in the middle part, and a predetermined amount of lead from the back of the blast furnace molten slag introduced into the molten slag storage container is guided to the manufacturing equipment, and the remainder is A process for producing cement using blast furnace molten slag according to claim 1. 3. The method for producing hymento using blast furnace molten slag according to claim 1 or 2, wherein the firing step is performed in a rotary kiln, and the blast furnace molten slag is sprayed into the rotary kiln. 4. The first stage of calcination is carried out in an airflow furnace type calcination furnace, and the blast furnace molten slag is sprayed inside the calcination furnace or into a duct 1 near the entrance of the calcination furnace. A method for producing cement 1- using the blast furnace molten slag described in item 1 or 2. 5. A molten slag transfer path is provided between the molten slab outlet of the steelmaking blast furnace and the cement manufacturing equipment, and a preheater and calciner of the cement production equipment are installed at one end of this molten slag transfer path. Or a spray for quantitatively spraying the blast furnace molten slag into the inside of the firing furnace or the inside of the duct that introduces cement to raw stone into the preheater, calcining furnace, or firing furnace! A device for manufacturing cement 1- using blast furnace molten slag, which is equipped with A-place. 6. The molten slag transfer path has a molten slag storage container in the middle part. 7. The firing furnace is located in the Ll-tally kiln, and the mouth and outlet of the spraying device are directed toward the inside of the tally kiln. ,-Runo^'11iI
'l Desired Range Item 5) or: is an apparatus for producing cement 1- using the blast furnace molten slag described in Item 6. 8. The calcining furnace is an airflow furnace type calcining furnace, and the calcination furnace described in 11.
For the ejection of the r1 mist device, Ll is installed inside the pre-calciner 31 or inside the gutter for introducing the cement raw material into the same sheet calciner. J R'l”=
Cement using the blast furnace molten slag described in the range 5 Jj'j or item 6! ~ manufacturing equipment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57123689A JPS5913652A (en) | 1982-07-15 | 1982-07-15 | Cement manufacture and device utilizing blast furnace molten slag |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57123689A JPS5913652A (en) | 1982-07-15 | 1982-07-15 | Cement manufacture and device utilizing blast furnace molten slag |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5913652A true JPS5913652A (en) | 1984-01-24 |
| JPH0313181B2 JPH0313181B2 (en) | 1991-02-21 |
Family
ID=14866883
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57123689A Granted JPS5913652A (en) | 1982-07-15 | 1982-07-15 | Cement manufacture and device utilizing blast furnace molten slag |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5913652A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6018114A (en) * | 1996-09-19 | 2000-01-25 | Yamaha Corporation | Rotary valve of brass instrument |
| US6709510B1 (en) | 2002-11-19 | 2004-03-23 | Texas Industries, Inc. | Process for using mill scale in cement clinker production |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5525147A (en) * | 1978-08-10 | 1980-02-22 | Murata Manufacturing Co | Television set with alarm |
| JPS5621989A (en) * | 1979-07-31 | 1981-02-28 | Tech Res & Dev Inst Of Japan Def Agency | Rigging for fiber reinforced plastic ship |
-
1982
- 1982-07-15 JP JP57123689A patent/JPS5913652A/en active Granted
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5525147A (en) * | 1978-08-10 | 1980-02-22 | Murata Manufacturing Co | Television set with alarm |
| JPS5621989A (en) * | 1979-07-31 | 1981-02-28 | Tech Res & Dev Inst Of Japan Def Agency | Rigging for fiber reinforced plastic ship |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6018114A (en) * | 1996-09-19 | 2000-01-25 | Yamaha Corporation | Rotary valve of brass instrument |
| US6709510B1 (en) | 2002-11-19 | 2004-03-23 | Texas Industries, Inc. | Process for using mill scale in cement clinker production |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0313181B2 (en) | 1991-02-21 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4489022A (en) | Forming coherent refractory masses | |
| US20020172907A1 (en) | Oxygen enrichment of cement kiln system combustion | |
| CN102135376A (en) | Stepped furnace | |
| IT7354661A1 (en) | WASTE CONVERTER, TO OXYGEN. | |
| US1468168A (en) | Apparatus for calcining and clinkering | |
| US4236932A (en) | Method and apparatus for producing a hydraulic binder | |
| JP2003528793A (en) | Method and apparatus for producing cement clinker from granular cement raw material | |
| GB1573010A (en) | Method for thermal traetment of dustlike material particularly for the pupose of burning cement in several stages | |
| US3365521A (en) | Process for producing substantially alkali-free kiln output when burning minerals containing difficult-to-volatilize alkali | |
| CN1030396A (en) | The melting method of glass batch and equipment | |
| US20230175778A1 (en) | Installation for the thermal treatment of dispersible raw material, and method for operating such an installation | |
| US4477283A (en) | Process and apparatus for producing hydraulic cements | |
| EP1017958B1 (en) | Oxygen enrichment of cement kiln system combustion | |
| JPS5913652A (en) | Cement manufacture and device utilizing blast furnace molten slag | |
| US3998649A (en) | Process of manufacturing Portland cement clinker | |
| US3954391A (en) | Process for endothermic heat treatment of materials | |
| EP4313899B1 (en) | Method for the cooling and heat recovery from materials at very high temperature | |
| CN100391882C (en) | Process for producing silicate cement chamotte by blast furnace liquid residue and apparatus thereof | |
| JPH02229743A (en) | Low-heat cement clinker and its production | |
| US3193264A (en) | Process and device for producing building material | |
| CN107043246A (en) | A kind of hot semidry method spray paint of mixed iron blast | |
| SU970059A1 (en) | Apparatus for roasting cement clinker | |
| US806146A (en) | Process of manufacturing portland cement. | |
| SU937395A1 (en) | Method for producing cement clinker | |
| SU77831A1 (en) | Converter for alumina cement |