JPS6127932Y2 - - Google Patents

Info

Publication number
JPS6127932Y2
JPS6127932Y2 JP1981181106U JP18110681U JPS6127932Y2 JP S6127932 Y2 JPS6127932 Y2 JP S6127932Y2 JP 1981181106 U JP1981181106 U JP 1981181106U JP 18110681 U JP18110681 U JP 18110681U JP S6127932 Y2 JPS6127932 Y2 JP S6127932Y2
Authority
JP
Japan
Prior art keywords
slag
air
airtight chamber
particles
heat recovery
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
JP1981181106U
Other languages
Japanese (ja)
Other versions
JPS5887844U (en
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 filed Critical
Priority to JP1981181106U priority Critical patent/JPS5887844U/en
Publication of JPS5887844U publication Critical patent/JPS5887844U/en
Application granted granted Critical
Publication of JPS6127932Y2 publication Critical patent/JPS6127932Y2/ja
Granted legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C21—METALLURGY OF IRON
    • C21B—MANUFACTURE OF IRON OR STEEL
    • C21B2400/00—Treatment of slags originating from iron or steel processes
    • C21B2400/02—Physical or chemical treatment of slags
    • C21B2400/022—Methods of cooling or quenching molten slag
    • C21B2400/026—Methods of cooling or quenching molten slag using air, inert gases or removable conductive bodies
    • C—CHEMISTRY; METALLURGY
    • C21—METALLURGY OF IRON
    • C21B—MANUFACTURE OF IRON OR STEEL
    • C21B2400/00—Treatment of slags originating from iron or steel processes
    • C21B2400/05—Apparatus features
    • C21B2400/06—Conveyors on which slag is cooled
    • C—CHEMISTRY; METALLURGY
    • C21—METALLURGY OF IRON
    • C21B—MANUFACTURE OF IRON OR STEEL
    • C21B2400/00—Treatment of slags originating from iron or steel processes
    • C21B2400/05—Apparatus features
    • C21B2400/062—Jet nozzles or pressurised fluids for cooling, fragmenting or atomising slag
    • C—CHEMISTRY; METALLURGY
    • C21—METALLURGY OF IRON
    • C21B—MANUFACTURE OF IRON OR STEEL
    • C21B2400/00—Treatment of slags originating from iron or steel processes
    • C21B2400/08—Treatment of slags originating from iron or steel processes with energy recovery
    • 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
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00—Technologies for solid waste management
    • Y02W30/50—Reuse, recycling or recovery technologies

Landscapes

  • Manufacture Of Iron (AREA)

Description

【考案の詳細な説明】 本考案は溶融スラグが保有する高熱を高温空気
として回収する溶融スラグからの熱回収装置に関
する。
[Detailed Description of the Invention] The present invention relates to a heat recovery device from molten slag that recovers high heat contained in molten slag as high-temperature air.

従来、溶融スラグからその保有する高熱を回収
する装置には、溶融スラグを細粒化固形物にして
熱回収を行うものが多く、例えば第1図に示す様
なものがある。
Conventionally, there are many devices for recovering the high heat contained in molten slag by converting the molten slag into finely granulated solids, such as the one shown in FIG. 1, for example.

該装置において、溶融スラグの落し口5より流
下した溶融スラグは、粒化用噴射ノズル6により
飛散し、飛散中に気密室1内空気との熱交換がな
され、再融着を起こさない温度まで冷却された固
形スラグ粒子として回収部3に捕集される。一
方、気密室1内空気はスラグ粒子との熱交換によ
り高温空気となり、排気口7を通じて、排風機1
5により、除塵器9を通り、清浄化された高温空
気となり、熱交換器10で熱回収される。(な
お、図にあつて11は回収スラグの充填層で、1
7はその切出装置、12は熱交換器、16は充填
層用フアン等で、スラグ顕熱を回収する構成とな
つている。) この従来方式では次の様な欠点があつた。即
ち、スラグウールの発生に伴ない、飛散中のスラ
グ粒子と、スラグウールが気密室1内空間又は回
収部において接触する事が避けられず、固形スラ
グ粒子の生産効率が低下するだけでなく固形スラ
グ粒子を気密室より搬出し、後段設備へ供給する
上で障害となり、装置の安定した連続運転が困難
となる等、実用上極めて不都合となる。
In this device, the molten slag flowing down from the molten slag drop port 5 is scattered by the granulating injection nozzle 6, and during the scattering, heat exchange is performed with the air in the airtight chamber 1, and the temperature reaches a temperature that does not cause re-fusion. The solid slag particles are collected in the collection section 3 as cooled solid slag particles. On the other hand, the air inside the airtight chamber 1 becomes high-temperature air due to heat exchange with the slag particles, and is passed through the exhaust port 7 to the exhaust fan 1.
5, the air passes through a dust remover 9 to become purified high-temperature air, and the heat is recovered by a heat exchanger 10. (In the figure, 11 is a packed bed of recovered slag, and 1
Reference numeral 7 indicates a cutting device, 12 a heat exchanger, 16 a packed bed fan, etc., which are configured to recover sensible heat from the slag. ) This conventional method had the following drawbacks. In other words, as slag wool is generated, it is unavoidable that the flying slag particles come into contact with the slag wool in the space inside the airtight chamber 1 or in the recovery section, which not only reduces the production efficiency of solid slag particles but also reduces the amount of solid slag particles. This is extremely inconvenient in practical terms, as it becomes a hindrance in transporting the slag particles out of the airtight chamber and supplying them to subsequent equipment, making stable continuous operation of the equipment difficult.

本考案は、従来法における上記欠点を解消し、
装置の連続安定運転を可能とし、且つ固形スラグ
粒子の生産効率を向上し、更にスラグ細粒化段階
での熱回収メリツトを少なくとも従来法以上に確
保すると云う画期的なものである。以下、本考案
による実施例の一つについて詳細に説明する。
The present invention eliminates the above drawbacks of the conventional method,
This is an epoch-making method that enables the continuous and stable operation of the equipment, improves the production efficiency of solid slag particles, and further ensures the advantage of heat recovery in the slag refinement stage at least more than conventional methods. Hereinafter, one embodiment of the present invention will be described in detail.

第2図において、スラグ粒化機構部2及び固形
スラグ回収部3は従来法と同様である。即ち、ス
ラグ粒化機構により飛散したスラグ粒子は飛散
中、冷却されながら、最終的に回収部3へ落下す
る。一方発生したスラグウールは、スラグ粒子と
混在した状態又は、スラグ粒子群の周囲を囲む状
態で、空間中に浮遊しながら、大部分は気密室排
気口から排出される。しかしながら、一部は前述
の様に、スラグ粒子と接触し、回収部等へ落下
し、気密室内へ残留し、装置の運転の障害の原因
等となる。ここで、本考案にあつては第2図bに
示す如く、気密室1内にあつて細粒化ノズル5の
位置しない側壁部又は底部に、複数個の噴射ノズ
ル18を概略水平方向又は上向きに配設する。し
かしてヒーター20及びフアン19を介し温風を
噴射する事により、スラグウールは、スラグ粒子
の飛行方向から離れ他方の側壁又は天井部に設け
た排気口7に概略すみやかに排出され、スラグウ
ールと接触する事が実用上無くなり、装置運転へ
の支障が解消される。
In FIG. 2, the slag granulation mechanism section 2 and the solid slag recovery section 3 are the same as those in the conventional method. That is, the slag particles scattered by the slag granulation mechanism are cooled during the scattering, and finally fall to the recovery section 3. On the other hand, most of the generated slag wool is discharged from the airtight chamber exhaust port while floating in the space in a state mixed with slag particles or in a state surrounding a group of slag particles. However, as described above, some of the slag particles come into contact with the slag particles, fall into the recovery section, etc., and remain in the airtight chamber, causing trouble in the operation of the equipment. In the present invention, as shown in FIG. 2b, a plurality of injection nozzles 18 are installed on the side wall or bottom of the airtight chamber 1 where the atomizing nozzle 5 is not located, in a generally horizontal or upward direction. to be placed. By injecting hot air through the heater 20 and the fan 19, the slag wool is almost immediately discharged away from the flight direction of the slag particles to the exhaust port 7 provided on the other side wall or ceiling. Contact is virtually eliminated, eliminating any hindrance to equipment operation.

又、本考案では、温風を噴射する事により、気
密室1からの排気温度を実用上低下させる事がな
いので該スラグ粒化段階での熱回収メリツトは、
単位時間当りは概略、従来と同レベルであり、装
置を安定的に連続運転できる様になる事により、
向上する。更に固形スラグ粒子の生産効率はスラ
グウールに付着して持去られる分が減少する事に
より向上する事は明らかである。
In addition, in the present invention, by injecting hot air, the temperature of the exhaust gas from the airtight chamber 1 is not practically lowered, so the merits of heat recovery at the slag granulation stage are as follows.
The unit time is roughly the same level as before, and by being able to operate the equipment stably and continuously,
improves. Furthermore, it is clear that the production efficiency of solid slag particles is improved by reducing the amount of solid slag particles that are attached to and removed from the slag wool.

尚、本考案でスラグウール対策用として使用す
る温風源は、外気を別途設置する加熱装置20で
加熱してよいが、第3図、第4図に示す様に、気
密室1から得られる高温空気を除塵した後、一部
抽気するか、又は気密室1後段に設置する充填層
等の固形スラグの熱交換装置11で得られる高温
空気の一部を抽気したものを、単独で又は外気と
混合して使用する事により更にエネルギーの有効
利用を図る事が可能である。
The hot air source used in the present invention to prevent slag wool may heat the outside air with a separately installed heating device 20, but as shown in FIGS. 3 and 4, the hot air source obtained from the airtight chamber 1 After removing dust, a portion of the high-temperature air is extracted, or a portion of the high-temperature air obtained from a solid slag heat exchange device 11 such as a packed bed installed at the latter stage of the airtight chamber 1 is extracted, either alone or mixed with outside air. It is possible to use energy even more effectively by using it.

この様に本考案により、スラグウールのすみや
かな除去ができ、装置の安定運転が達成でき、従
来法に較べ、熱回収メリツト、固形スラグの生産
効率、共に向上させる事が可能となりその利用価
値は高い。
As described above, the present invention enables prompt removal of slag wool, achieves stable operation of the equipment, and improves both heat recovery merits and solid slag production efficiency compared to conventional methods. expensive.

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

第1図は従来法による熱回収装置の実施例の一
つを示す概略図、第2図は本考案による実施例を
示す概略図であり、aは正面図、bはaのA−A
断面、cは噴射ノズルの他の実施例を示す図、第
3図は温風源として、気密室から得られる高温空
気を除塵後、一部抽気し単独で又は、外気と混合
して使用する、本考案による実施例の一つを示す
概略図、第4図は温風源として、気密室後段に設
置する充填層等の固形スラグとの熱交換装置で得
られる高温空気を単独で又は外気と混合して使用
する本考案による実施例の一つを示す概略図であ
る。 1:気密室、2:スラグ細粒化機構、3:細粒
化スラグ回収部、4:回収部用空気流入口、5:
スラグ落し口、6:噴射ノズル、7:排気孔、
8:固形スラグ搬出装置、9:除塵器、10:熱
交換器、11:充填層等、12:熱交換器、1
3:細粒化機構部用噴射空気用フアン、14:回
収部空気用フアン、15:排気フアン、16:充
填層用フアン、17:切出装置、18:スラグウ
ール対策用噴射ノズル、19:スラグウール対策
用フアン、20:スラグウール対策用ヒータ。
Fig. 1 is a schematic diagram showing one embodiment of a heat recovery device according to a conventional method, and Fig. 2 is a schematic diagram showing an embodiment according to the present invention, in which a is a front view and b is an A-A in a.
The cross section, c, is a diagram showing another embodiment of the injection nozzle, and Figure 3 is a diagram showing a hot air source in which high-temperature air obtained from an airtight chamber is partially extracted after dust removal and used alone or mixed with outside air. FIG. 4 is a schematic diagram showing one of the embodiments of the invention. As a hot air source, high-temperature air obtained from a heat exchange device with solid slag such as a packed bed installed at the latter stage of the airtight chamber is used alone or mixed with outside air. 1 is a schematic diagram showing one embodiment of the present invention in use; FIG. 1: Airtight chamber, 2: Slag refining mechanism, 3: Refined slag collection section, 4: Air inlet for collection section, 5:
Slag dropping port, 6: Injection nozzle, 7: Exhaust hole,
8: Solid slag transport device, 9: Dust remover, 10: Heat exchanger, 11: Filled bed, etc., 12: Heat exchanger, 1
3: Injection air fan for atomization mechanism section, 14: Recovery section air fan, 15: Exhaust fan, 16: Packed bed fan, 17: Cutting device, 18: Slag wool countermeasure injection nozzle, 19: Fan for preventing slag wool, 20: Heater for preventing slag wool.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 溶融スラグを細粒化して気密室内に飛散させる
スラグ細粒化機構を備なえると共に、該気密室の
一方に給気口、他方に排気口を備なえ、気密室内
空気をスラグ粒子との熱交換により高温空気にし
て取出すようにした熱回収装置において、上記細
粒化ノズルの位置しない側壁又は底部に、温風を
概略水平方向又は上向きに強制的に噴射する如く
なした噴射ノズルを複数個配設したことを特徴と
する溶融スラグからの熱回収装置。
It is equipped with a slag atomization mechanism that makes the molten slag into fine particles and scatters it inside the airtight chamber, and is also equipped with an air supply port on one side of the airtight chamber and an exhaust port on the other side, so that the air in the airtight room can be heated with the slag particles. In a heat recovery device that extracts high-temperature air through exchange, a plurality of injection nozzles are provided on the side wall or bottom where the atomization nozzle is not located, so as to forcibly inject hot air approximately horizontally or upward. A heat recovery device from molten slag characterized by the following:
JP1981181106U 1981-12-07 1981-12-07 Heat recovery device from molten slag Granted JPS5887844U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1981181106U JPS5887844U (en) 1981-12-07 1981-12-07 Heat recovery device from molten slag

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1981181106U JPS5887844U (en) 1981-12-07 1981-12-07 Heat recovery device from molten slag

Publications (2)

Publication Number Publication Date
JPS5887844U JPS5887844U (en) 1983-06-14
JPS6127932Y2 true JPS6127932Y2 (en) 1986-08-20

Family

ID=29978289

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1981181106U Granted JPS5887844U (en) 1981-12-07 1981-12-07 Heat recovery device from molten slag

Country Status (1)

Country Link
JP (1) JPS5887844U (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6020957B2 (en) * 1979-08-07 1985-05-24 岩崎通信機株式会社 Alarm circuit using button telephone device

Also Published As

Publication number Publication date
JPS5887844U (en) 1983-06-14

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