JPS587121B2 - Equipment that generates high pressure steam from molten slag - Google Patents

Equipment that generates high pressure steam from molten slag

Info

Publication number
JPS587121B2
JPS587121B2 JP52044546A JP4454677A JPS587121B2 JP S587121 B2 JPS587121 B2 JP S587121B2 JP 52044546 A JP52044546 A JP 52044546A JP 4454677 A JP4454677 A JP 4454677A JP S587121 B2 JPS587121 B2 JP S587121B2
Authority
JP
Japan
Prior art keywords
casing
superheated steam
boiler
steam
slag
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
Application number
JP52044546A
Other languages
Japanese (ja)
Other versions
JPS53129708A (en
Inventor
西岡和正
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsui Engineering and Shipbuilding Co Ltd
Original Assignee
Mitsui Engineering and Shipbuilding Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Mitsui Engineering and Shipbuilding Co Ltd filed Critical Mitsui Engineering and Shipbuilding Co Ltd
Priority to JP52044546A priority Critical patent/JPS587121B2/en
Publication of JPS53129708A publication Critical patent/JPS53129708A/en
Publication of JPS587121B2 publication Critical patent/JPS587121B2/en
Expired legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明は、溶鉱炉などから排出される高温の溶融スラグ
から、高圧の水蒸気を発生する装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for generating high-pressure steam from high-temperature molten slag discharged from a blast furnace or the like.

従来,溶融炉から排出される溶融スラグは、水をかけて
冷却した後に投棄するか、またスラグの熱を気体に伝達
して,通常のボイラでこの熱を回収するかしていた。
Conventionally, the molten slag discharged from the melting furnace was either cooled by water and then dumped, or the heat of the slag was transferred to gas and the heat was recovered in a normal boiler.

前者の場合、溶融スラグのもっている大量の熱は、大気
中に放散されてしまうため、省エネルギの点から極めて
遺感であり、また後者の場合、溶融スラグのもつ熱エネ
ルギは回収されるもの一それは、スラグ→気体→ボイラ
という手順によるため、能率が悪く、かつ莫大な伝熱面
を必要とするという欠点をもっている。
In the former case, a large amount of heat contained in the molten slag is dissipated into the atmosphere, which is extremely important from an energy saving perspective, and in the latter case, the thermal energy contained in the molten slag can be recovered. First, because it relies on the procedure of slag -> gas -> boiler, it has the disadvantage of being inefficient and requiring a huge heat transfer surface.

本発明は、このような現状に鑑み発明されたものであっ
て、小型で、能率のよい、溶融スラグの熱を高圧蒸気の
形で回収する水蒸気発生装置の提供を目的とするもので
あって、本発明は溶融スラグのもっている熱を過熱蒸気
、飽和蒸気、給水予熱の三段階で回収するようにした点
を特長とするものである。
The present invention was invented in view of the current situation, and aims to provide a small and efficient steam generator that recovers heat from molten slag in the form of high-pressure steam. The present invention is characterized in that the heat possessed by molten slag is recovered in three stages: superheated steam, saturated steam, and preheating of feed water.

次に、図面により、本発明の一実施例を説明する。Next, one embodiment of the present invention will be described with reference to the drawings.

1はボイラ本体であって.ホッパ状をなしていて、下端
には細径状の給水予熱ケーシング12が連設されている
1 is the boiler body. It has a hopper shape, and a small diameter water preheating casing 12 is connected to the lower end.

そしてボイラ本体1の上部にC上本体1を貫通して本体
1内のボイラ水20/上に開口する過熱蒸気ケーシング
10が設けられ、このケーシング10の上端には、溶融
スラグを粒状にして供給する装置、たとえば溶融スラグ
導入用のホツパ4とこのホツパ4に連なる回転式フイー
ダ6が取付けられている。
A superheated steam casing 10 is provided in the upper part of the boiler body 1, and the superheated steam casing 10 penetrates through the upper body 1 and opens above the boiler water 20 in the body 1.The upper end of the casing 10 is supplied with molten slag in the form of particles. For example, a hopper 4 for introducing molten slag and a rotary feeder 6 connected to the hopper 4 are attached.

該フイーダ6は、ケーシング5内に回転可能に装架され
たドラムから成り、該ドラムの外周には、凹みが穿設さ
れていて、反時計方向に回転するようになっている。
The feeder 6 consists of a drum rotatably mounted within the casing 5, and a recess is bored in the outer periphery of the drum so that it can rotate counterclockwise.

また、ボイラ本体1には、ボイラ本体内のボイラ水20
’上に開口する飽和蒸気取出管25と、ボイラ本体1を
貫通して過熱蒸気ケーシング10に開口する過熱蒸気取
出管24が夫々設けられている。
In addition, the boiler body 1 includes boiler water 20 inside the boiler body.
A saturated steam take-off pipe 25 that opens upward and a superheated steam take-off pipe 24 that penetrates the boiler body 1 and opens into the superheated steam casing 10 are provided.

なお図では過熱蒸気取出皆24と飽和蒸気取出管25同
心状となっているが、本発明はこれに限定されるもので
はなく、夫々、単独に設けることもできる。
In the figure, the superheated steam outlet 24 and the saturated steam outlet pipe 25 are shown concentrically, but the present invention is not limited to this, and each may be provided independently.

給水予熱ケーシング12内には、スラグ排出調整用のス
クリュー13が設けられており、その下端には、スラグ
排出回転ロータ15が回転可能に装架されている。
A screw 13 for adjusting slag discharge is provided inside the water supply preheating casing 12, and a slag discharge rotating rotor 15 is rotatably mounted on the lower end of the screw 13.

17は給水配管で、給水制御弁18を介して給水予熱ケ
ーシング12の下端に開口19し、またその分岐管23
は過熱温度調節用注水制御弁22を介して、蒸気過熱ケ
ーシング10内に開口する,なお図中、14はロータ1
5を回転可能に装架するロータケーシング、16はロー
タ15に穿設した凹み、11は分散板である。
Reference numeral 17 denotes a water supply pipe, which opens at the lower end of the water supply preheating casing 12 via a water supply control valve 18, and a branch pipe 23 thereof.
is opened into the steam superheating casing 10 via the water injection control valve 22 for superheating temperature adjustment. In the figure, 14 is the rotor 1.
A rotor casing 5 is rotatably mounted, 16 is a recess formed in the rotor 15, and 11 is a dispersion plate.

次に、本装置の作動を説明する。Next, the operation of this device will be explained.

ホツパ4に,スラグを流動状態2で注入すると、ホツパ
4内でスラグは3で示す状態で溜り、ホツパ4の下方か
ら、フイーダ6の凹みT内に、少量づ\順次フイーダ6
の回転につれて充填される。
When slag is injected into the hopper 4 in a fluid state 2, the slag accumulates in the hopper 4 in the state shown by 3, and is gradually poured into the recess T of the feeder 6 from below the hopper 4 in small quantities.
It is filled as it rotates.

フイーダ6の回転によって、凹みT内に充填されたスラ
グ8は蒸気過熱ケーシング10を介して粒状のスラグ9
となって,ボイラ本体1内に落下する。
As the feeder 6 rotates, the slag 8 filled in the recess T passes through the steam superheated casing 10 and becomes granular slag 9.
and falls into the boiler body 1.

ボイラ本体1内には、27で示したレベルまで水が注入
されており、ボイラ本体1内に落下したスラグ9は、ま
わりのボイラ水21’に直接接触して水に熱を伝え、水
を沸騰させると共に、スラグ自体は固形化する。
Water is injected into the boiler body 1 to the level shown at 27, and the slag 9 that has fallen into the boiler body 1 directly contacts the surrounding boiler water 21' and transfers heat to the water, causing the water to rise. Upon boiling, the slag itself solidifies.

固形化したスラグ9は、さらにボイラ本体1内を落下し
続け、分散板11に当接してボイラ本体1内に広く分散
する。
The solidified slag 9 further continues to fall within the boiler main body 1, comes into contact with the distribution plate 11, and is widely dispersed within the boiler main body 1.

そして、給水予熱ケーシング12内に落下して、ここに
注入されている水20を加熱し、最後にはスクリュー1
3でロータ15に送られ、ロータ15の凹み16に順次
充填され、ロータ15の回転と共に、ケーシング12外
に排出される。
Then, it falls into the water supply preheating casing 12 and heats the water 20 injected there, and finally the screw 1
3, it is sent to the rotor 15, sequentially filled into the recesses 16 of the rotor 15, and discharged to the outside of the casing 12 as the rotor 15 rotates.

給水配管17から供給される給水は、その一部は、予熱
ケーシング12内で、スラグで予熱されつ5ボイラ本体
1にむかって上昇し、ボイラ本体1内で、高温のスラグ
に直接接触して飽和蒸気21となり弁26により調節さ
れ乍ら、管25から取出される。
A portion of the water supplied from the water supply pipe 17 is preheated with slag in the preheating casing 12 and rises toward the boiler body 1, where it comes into direct contact with the high-temperature slag. This becomes saturated steam 21, which is regulated by a valve 26 and taken out through a pipe 25.

また、給水の他の一部は、分岐管23によって過熱蒸気
ケーシング10内に供給され、こ\で極めて高温のスラ
グに接触して、過熱蒸気21’となり、一方、飽和蒸気
21の一部21Aも過熱蒸気ケーシング10に浸入して
高温のスラグに接触して過熱蒸気21’となり、両者は
共に過熱蒸気取出管24から取出される。
Further, another part of the feed water is supplied into the superheated steam casing 10 through the branch pipe 23, where it comes into contact with the extremely high temperature slag and becomes superheated steam 21', while a part of the saturated steam 21 21A The superheated steam also enters the superheated steam casing 10 and comes into contact with the high temperature slag to become superheated steam 21', and both are taken out from the superheated steam extraction pipe 24.

飽和蒸気21と過熱蒸気21’は系外において夫々別々
に使用に供されても良いし、或は図示の如く混合蒸気2
1′として用いることもできる。
The saturated steam 21 and the superheated steam 21' may be used separately outside the system, or the mixed steam 21' may be used separately as shown in the figure.
It can also be used as 1'.

このように、本装置では溶融状の極めて高温のスラグを
先ず、これに直接給水を接触させることにより、過熱蒸
気とし、この熱交換により、固形化したスラグを、ボイ
ラ本体内を、下方から上昇してくる給水に、これと対向
するように落下させて、この給水を飽和蒸気とすると共
に、この飽和蒸気の一部を高温のスラグと接触させて過
熱蒸気を得る。
In this way, in this device, molten extremely high-temperature slag is first brought into direct contact with feed water to turn it into superheated steam, and through this heat exchange, the solidified slag rises from below inside the boiler body. The feed water is made to fall opposite to the incoming feed water to turn the feed water into saturated steam, and a portion of this saturated steam is brought into contact with high temperature slag to obtain superheated steam.

さらに,スラグは、給水予熱ケーシング内で、ボイラ本
体1内に供給される給水を予熱した後に,ケーシングか
ら取出すようにしたため溶鉱炉から排出される溶融状の
スラグのもっている熱は蒸気状態で回収されることにな
る。
Furthermore, since the slag is taken out from the casing after the feed water supplied to the boiler body 1 is preheated in the feed water preheating casing, the heat of the molten slag discharged from the blast furnace is recovered in the form of steam. That will happen.

そして、本装置は、上述のように,スラグのもっている
熱は、過熱蒸気発生、飽和蒸気発生、給水予熱の三つの
段階で、それぞれ回収されるため、その能率は良好なも
のとなり、また、小形であるにも拘らず、大量の熱量を
回収することができる。
As mentioned above, this device has good efficiency because the heat possessed by the slag is recovered in each of the three stages of superheated steam generation, saturated steam generation, and feed water preheating. Despite its small size, it can recover a large amount of heat.

またスラグは、粒状の固形物となって、ケーシングから
排出されるから、その後の取扱いが極めて簡単となる。
Further, since the slag is discharged from the casing in the form of granular solids, subsequent handling becomes extremely easy.

【図面の簡単な説明】[Brief explanation of drawings]

図は本発明の一実施例を示すものである。 1・・・・・・ボイラ本体、4・・・・・・ホッパ、6
・・・・・・回転式のフイーダ、10・・・・・・過熱
蒸気ケーシン久,12・・・・・・給水予熱ケーシング
、15・・・・・・スラグ排出回転ロータ、17・・・
・・・給水管、21・・・・・・分岐管、24・・・・
・・過熱蒸気取出管、25・・・・・・飽和蒸気取出管
The figure shows one embodiment of the invention. 1...boiler body, 4...hopper, 6
... Rotating feeder, 10 ... Superheated steam casing, 12 ... Water supply preheating casing, 15 ... Slag discharge rotating rotor, 17 ...
... Water supply pipe, 21 ... Branch pipe, 24 ...
...Superheated steam takeoff pipe, 25...Saturated steam takeoff pipe.

Claims (1)

【特許請求の範囲】[Claims] 1 下方に細径状の給水予熱ケーシングがのびるボイラ
本体と、該ボイラ本体の上部を貫通して該ボイラ本体内
のボイラ水上に開口する過熱蒸気ケーシングとから成り
、溶融状のスラグを粒状にして前記過熱蒸気ケーシング
を介して前記ボイラ本体内に供給する装置を前記過熱蒸
気ケーシング上に設け、前記ボイラ本体内の前記ボイラ
水上に開口する飽和蒸気取出管と、前記ボイラ本体を貫
通して前記過熱蒸気ケーシングに開口する過熱蒸気取出
管を夫々設け、前記給水予熱ケーシングと前記過熱蒸気
ケーシングに至る給水管を配設し、更に前記給水予熱ケ
ーシング内に落下した粒状スラグを排出するロータを前
記給水予熱ケーシングの下端に設けたことを特徴とする
溶融スラグから高圧蒸気を発生する装置。
1 Consists of a boiler body with a small-diameter feedwater preheating casing extending downwards, and a superheated steam casing that penetrates through the top of the boiler body and opens above the boiler water in the boiler body, and converts molten slag into particles. A device for supplying the superheated steam into the boiler main body via the superheated steam casing is provided on the superheated steam casing, and a saturated steam extraction pipe opens above the boiler water in the boiler main body, and a saturated steam extraction pipe that penetrates the boiler main body and supplies the superheated steam to the boiler main body. Superheated steam take-off pipes opening in the steam casing are provided, water supply pipes are provided leading to the feedwater preheating casing and the superheated steam casing, and a rotor for discharging granular slag that has fallen into the feedwater preheating casing is connected to the feedwater preheating casing. A device for generating high-pressure steam from molten slag, characterized by being installed at the lower end of a casing.
JP52044546A 1977-04-20 1977-04-20 Equipment that generates high pressure steam from molten slag Expired JPS587121B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP52044546A JPS587121B2 (en) 1977-04-20 1977-04-20 Equipment that generates high pressure steam from molten slag

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP52044546A JPS587121B2 (en) 1977-04-20 1977-04-20 Equipment that generates high pressure steam from molten slag

Publications (2)

Publication Number Publication Date
JPS53129708A JPS53129708A (en) 1978-11-13
JPS587121B2 true JPS587121B2 (en) 1983-02-08

Family

ID=12694489

Family Applications (1)

Application Number Title Priority Date Filing Date
JP52044546A Expired JPS587121B2 (en) 1977-04-20 1977-04-20 Equipment that generates high pressure steam from molten slag

Country Status (1)

Country Link
JP (1) JPS587121B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104266157A (en) * 2014-10-12 2015-01-07 中国科学院工程热物理研究所 Direct contact type high temperature particle fluidization steam generator

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5965201U (en) * 1982-10-21 1984-05-01 三菱重工業株式会社 Powder contact boiler

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104266157A (en) * 2014-10-12 2015-01-07 中国科学院工程热物理研究所 Direct contact type high temperature particle fluidization steam generator
CN104266157B (en) * 2014-10-12 2015-11-18 中国科学院工程热物理研究所 A kind of direct contact type high-temperature particle fluidizing vapor generator

Also Published As

Publication number Publication date
JPS53129708A (en) 1978-11-13

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