TWI393697B - A cooling treatment device for melting molten slag and a cooling method - Google Patents

A cooling treatment device for melting molten slag and a cooling method Download PDF

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TWI393697B
TWI393697B TW098108889A TW98108889A TWI393697B TW I393697 B TWI393697 B TW I393697B TW 098108889 A TW098108889 A TW 098108889A TW 98108889 A TW98108889 A TW 98108889A TW I393697 B TWI393697 B TW I393697B
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slag
cooling
drum
molten slag
cooling treatment
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TW098108889A
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TW200951098A (en
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Katsuhiro Iwasaki
Hiroyuki Tobo
Kazuya Yabuta
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Jfe Steel Corp
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23JREMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J1/00Removing ash, clinker, or slag from combustion chambers
    • F23J1/08Liquid slag removal
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B5/00Treatment of  metallurgical  slag ; Artificial stone from molten  metallurgical  slag 
    • C04B5/06Ingredients, other than water, added to the molten slag or to the granulating medium or before remelting; Treatment with gases or gas generating compounds, e.g. to obtain porous slag
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/02Physical or chemical treatment of slags
    • C21B2400/022Methods of cooling or quenching molten slag
    • C21B2400/026Methods of cooling or quenching molten slag using air, inert gases or removable conductive bodies
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/04Specific shape of slag after cooling
    • C21B2400/042Sheets
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/05Apparatus features
    • C21B2400/052Apparatus features including rotating parts
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/05Apparatus features
    • C21B2400/052Apparatus features including rotating parts
    • C21B2400/056Drums whereby slag is poured on or in between
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/08Treatment of slags originating from iron or steel processes with energy recovery
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23JREMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2900/00Special arrangements for conducting or purifying combustion fumes; Treatment of fumes or ashes
    • F23J2900/01002Cooling of ashes from the combustion chamber by indirect heat exchangers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23JREMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2900/00Special arrangements for conducting or purifying combustion fumes; Treatment of fumes or ashes
    • F23J2900/01003Ash crushing means associated with ash removal means

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Ceramic Engineering (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Curing Cements, Concrete, And Artificial Stone (AREA)
  • Furnace Details (AREA)
  • Gasification And Melting Of Waste (AREA)

Description

熔化熔渣之冷卻處理裝置及冷卻處理方法 Cooling treatment device for melting slag and cooling treatment method

本發明係關於冷卻滾筒式之熔化熔渣冷卻處理裝置,以及使用該裝置的熔化熔渣之冷卻處理方法暨熔渣製品之製造方法。 The present invention relates to a cooling drum type molten slag cooling treatment apparatus, a cooling treatment method using the molten slag of the apparatus, and a method of manufacturing the slag product.

在鐵鋼製造製程所產生的熔化熔渣(例如製鋼熔渣),大多係在冷卻場放冷後,再施行灑水而冷卻。此外,亦有採行將其中一部分流入至通稱「盤冷卻式」的鐵製容器中並施行灑水冷卻的方法。 The molten slag (such as steel slag) produced in the iron and steel manufacturing process is mostly cooled in a cooling field and then sprinkled with water. In addition, some of them have been introduced into an iron container known as a "plate cooling type" and subjected to watering and cooling.

另一方面,用於對高爐熔渣、垃圾焚化灰熔化熔渣等熔化熔渣施行冷卻處理的裝置,已知有雙滾筒式之熔渣冷卻處理裝置(例如專利第3613106號公報等)。該熔渣冷卻處理裝置係具備有於水平方向上並排、且具有相對向之外周部分朝上旋轉之旋轉方向的1對冷卻滾筒,從上方供應熔化熔渣至該1對冷卻滾筒的上部外周面間,而形成熔渣液滯留。藉由從該熔渣液滯留附著‧凝固於旋轉中的冷卻滾筒表面上,而將熔化熔渣夾帶出,該熔化熔渣係在附著於冷卻滾筒面的狀態下,冷卻至適度凝固狀態後,再於既定滾筒旋轉位置處,利用自重而從冷卻滾筒面上剝離,並由回收手段回收。 On the other hand, a device for cooling a molten slag such as blast furnace slag or waste incineration ash melting slag is known as a double drum type slag cooling treatment device (for example, Patent No. 3613106). The slag cooling treatment apparatus includes a pair of cooling drums arranged side by side in the horizontal direction and having a rotation direction that rotates upward with respect to the outer peripheral portion, and the molten slag is supplied from above to the upper outer peripheral surface of the pair of cooling drums. Between, and the formation of slag liquid retention. The molten slag is entrained by the slag liquid adhering and adhering to the surface of the cooling drum that is being rotated, and the molten slag is cooled to a moderately solidified state while being attached to the surface of the cooling drum. Further, at a predetermined drum rotation position, it is peeled off from the cooling drum surface by its own weight, and is recovered by a recovery means.

藉由利用此種冷卻處理裝置對熔化熔渣施行冷卻處理,具有下述優點:(i)不需要如習知的廣大冷卻場;(ii)可獲得 厚度較小的熔渣凝固體,因此可輕易加工為所需粒度的土木材料、粗骨材等,且在施行破碎處理而製造粒狀熔渣時,粉末或細粒品產生量較少,因而提升製品良率;(iii)不需要用於施行冷卻用的灑水、或依較少灑水量便可,因而能獲得未含水分或水分量較少的熔渣,在供於水泥原料等情況時不需要乾燥處理等。 Cooling treatment of the molten slag by using such a cooling treatment device has the following advantages: (i) does not require a large number of cooling fields as is conventional; (ii) a slag solidified body having a small thickness, so that it can be easily processed into a civil material, a coarse aggregate, or the like of a desired particle size, and when the pulverized slag is produced by the crushing treatment, the amount of powder or fine granules is small, and thus Improve the yield of the product; (iii) do not need to be used for the cooling of the sprinkling water, or less watering, so that the slag without water or less moisture can be obtained, in the case of cement raw materials, etc. No drying treatment is required at the time.

但是,如上述的雙滾筒式之熔渣冷卻處理裝置,因為從1對冷卻滾筒朝各自相反方向排出處理完之熔渣,因而冷卻處理完之熔渣的排出/處理需要2路徑,導致需要寬廣的場地面積。所以,冷卻處理完之熔渣的處置、後處理、熱回收均較為煩雜,且效率差、設備成本亦會增加。 However, in the above-described double drum type slag cooling processing apparatus, since the processed slag is discharged from the pair of cooling drums in opposite directions, the slag discharge/treatment of the cooling process requires 2 paths, resulting in a wide need. The area of the venue. Therefore, the disposal, post-treatment, and heat recovery of the slag after cooling treatment are both cumbersome, and the efficiency is poor and the equipment cost is also increased.

以冷卻滾筒式之冷卻處理裝置施行冷卻處理的熔渣尚具有相當的顯熱,所以,從能量有效利用的觀點而言,若欲盡可能地回收熔渣顯熱,則重要的是從該經冷卻處理之熔渣中施行熱回收。但是,如習知雙滾筒式之熔渣冷卻處理裝置,若欲將朝正反二方向排出的冷卻處理完之熔渣,利用1個熱回收設備施行處理,則在將2路徑整合為1個的搬送過程中熔渣溫度會降低,無法施行有效率的熱回收。此情形特別係在大量處理熔化熔渣時將造成大問題。 The slag subjected to the cooling treatment by the cooling drum type cooling treatment device has a considerable sensible heat. Therefore, from the viewpoint of efficient use of energy, if it is desired to recover the sensible heat of the slag as much as possible, it is important from the Heat recovery is performed in the slag cooled. However, in the case of the conventional double-drum type slag cooling treatment device, if the slag which has been cooled and discharged in the forward and reverse directions is to be treated by one heat recovery device, the two paths are integrated into one. During the transfer process, the slag temperature is lowered and efficient heat recovery cannot be performed. This situation is particularly problematic when a large amount of molten slag is processed.

再者,使用大型雙滾筒式之熔渣冷卻處理裝置,大量處理熔化熔渣時(例如熔渣處理量:1t/min以上),當從熔渣鍋朝冷卻滾筒灌注熔化熔渣時,有因落下的熔化熔渣荷重導致 冷卻滾筒遭受損耗之虞。為防止此現象,便必需在冷卻滾筒上方設置澆口盤,先將熔渣鍋的熔化熔渣暫時移至澆口盤,再從該澆口盤施行灌注至冷卻滾筒。但是,當熔化熔渣的灌注係使用澆口盤的情況,不同於熔融金屬,熔渣會凝固附著於澆口,導致無法適當地施行灌注等而容易對操作構成障礙。此外,在澆口盤內殘留/附著的熔渣量亦變多,容易發生灌注口阻塞、殘留熔渣之粉化等問題。另一方面,為了不致發生此種殘留‧附著熔渣情形,便必需設置澆口盤加熱器,而導致發生能量效率降低、處理成本上升等問題。 Furthermore, when a large double-drum slag cooling treatment device is used, a large amount of molten slag is processed (for example, slag processing amount: 1 t/min or more), and when molten slag is poured from the slag pot toward the cooling drum, there is a cause Falling molten slag load causes The cooling drum suffers from a loss. In order to prevent this, it is necessary to provide a tundish above the cooling drum, and the molten slag of the slag pot is temporarily moved to the tundish, and then poured into the cooling drum from the tundish. However, when the infusion of the molten slag is performed using a tundish, unlike the molten metal, the slag is solidified and adhered to the gate, resulting in failure to properly perform the perfusion or the like, which may easily hinder the operation. Further, the amount of slag remaining/attached in the tundish is also increased, and problems such as clogging of the infusion port and pulverization of residual slag are likely to occur. On the other hand, in order not to cause such residual ‧ adhesion slag, it is necessary to provide a tundish heater, which causes problems such as a decrease in energy efficiency and an increase in processing cost.

當製造高爐熔渣等偏向骨材的熔渣製品時,依照製造條件會成為非晶質(玻璃質)熔渣,但非晶質熔渣的吸濕性低,容易出現尖角部分,因而造成問題。此外,當發生纖維狀熔渣的情況,則屬於不適用為偏向骨材製品的形狀。且,若成為細微纖維狀,則有必需採取包括防止飛散等環境對策的問題。 When a slag product such as blast furnace slag or the like is produced, it becomes amorphous (glassy) slag according to the production conditions, but the amorphous slag has low hygroscopicity and is prone to sharp corners, thereby causing problem. Further, in the case where fibrous slag is generated, it is not suitable as a shape that biases the aggregate product. Further, if it is in the form of fine fibers, it is necessary to take measures including environmental measures such as prevention of scattering.

再者,依照本發明者等人的檢討結果,判斷習知雙滾筒式之熔渣冷卻處理裝置尚有如下述問題: Further, according to the results of the review by the inventors of the present invention, it has been determined that the conventional double drum type slag cooling processing apparatus has the following problems:

(a)如轉爐脫碳精煉熔渣般鹼度[質量比:%CaO/%SiO2](以下簡稱「鹼度」)較高的熔化熔渣,黏性較高,將此種黏性較高的熔化熔渣,利用習知雙滾筒式之熔渣冷卻處理裝置施行冷卻處理時,會因為高黏性,導致熔化熔渣不易均勻附著於冷卻滾筒面上,造成滾筒面整體無法有效地使用於冷卻處 理。因而,熔化熔渣的冷卻效率偏低,無法獲得高生產性。此外,鹼度較高的熔渣(特別係鹼度≧3)較容易粉化,此種熔渣藉由從熔融狀態進行急冷,雖可不易粉化,但當利用習知熔渣冷卻處理裝置施行冷卻處理時,因為高黏性導致厚度無法變薄,無法獲得充分之冷卻速度,所以無法適當地抑制冷卻後的粉化。 (a) If the melting slag has a higher alkalinity [mass ratio: %CaO/%SiO 2 ] (hereinafter referred to as "alkalinity"), such as converter decarburization refining slag, the viscosity is higher, and the viscosity is higher. When the high melting slag is cooled by the conventional double drum type slag cooling treatment device, the molten slag is not easily adhered to the cooling drum surface due to high viscosity, and the entire drum surface cannot be effectively used. After cooling treatment. Therefore, the cooling efficiency of the molten slag is low, and high productivity cannot be obtained. In addition, the slag having a relatively high alkalinity (especially alkalinity ≧3) is more easily pulverized, and the slag is quenched from a molten state, although it is not easy to be pulverized, but when using a conventional slag cooling treatment device When the cooling treatment is performed, the thickness cannot be reduced due to the high viscosity, and a sufficient cooling rate cannot be obtained, so that the powdering after cooling cannot be appropriately suppressed.

(b)利用習知雙滾筒式之熔渣冷卻處理裝置,對高爐熔渣般之黏度較小的熔化熔渣施行冷卻處理時,僅能獲得厚度2~3mm左右的薄熔渣凝固體,即使將其施行成粒狀的破碎處理,仍無法滿足粗骨材、路床料等所必要的粒度。此外,因為薄熔渣凝固體成為玻璃質,因而保水性降低,從此觀點而言,亦可謂不適合於路床料等。所以,本發明目的在於解決此種習知技術問題,提供:冷卻處理完之熔渣的處置‧後處理等較為容易且能抑低設備成本的熔渣製品製造裝置,即使大型裝置仍不需要使用澆口盤,且能在不致因所供應之熔化熔渣的落下荷重,導致冷卻滾筒遭受損耗的情形下,對熔化熔渣施行大量處理的冷卻滾筒式熔化熔渣冷卻處理裝置。 (b) When the slag cooling treatment device of the conventional double drum type is used to cool the molten slag having a small viscosity like the blast furnace slag, only the solid slag solidified body having a thickness of about 2 to 3 mm can be obtained, even if The crushing treatment is carried out in a granular form, and the particle size necessary for the coarse aggregate, the road bed material, and the like is still not satisfied. Further, since the thin slag solidified body is made of glass, the water retention property is lowered, and from this point of view, it is not suitable for a road bed material or the like. Therefore, the object of the present invention is to solve such conventional technical problems and to provide a slag product manufacturing apparatus which is easy to handle, such as disposal of slag after cooling treatment, post-treatment, etc., and which can reduce equipment cost, even if large equipment is not required. A cooling drum type molten slag cooling treatment device that performs a large amount of treatment on the molten slag without the loss of the molten slag supplied by the supplied molten slag, resulting in a loss of the cooling slag.

再者,本發明另一目的係提供可對鹼度較高、具黏性的熔化熔渣有效率地施行冷卻處理,且特別係即使鹼度較高的熔渣,仍可獲得不易粉化之熔渣凝固體的熔化熔渣之冷卻處理裝置。 Furthermore, another object of the present invention is to provide an efficient cooling treatment for a molten slag having a high alkalinity and viscosity, and in particular, even if the slag having a high alkalinity is obtained, it is not easy to be pulverized. A cooling treatment device for melting slag of a slag solidified body.

再者,本發明另一目的在於提供:以黏度較小之熔化熔渣 作為處理對象時,可製造出適於獲得粗骨材等熔渣製品之厚板熔渣凝固體的熔化熔渣之冷卻處理裝置。 Furthermore, another object of the present invention is to provide a molten slag having a small viscosity. When it is to be processed, it is possible to manufacture a cooling treatment apparatus for melting slag which is suitable for obtaining a thick slag solidified body of a slag product such as a coarse aggregate.

再者,本發明另一目的在於提供使用如上述冷卻處理裝置的熔化熔渣之冷卻處理方法。 Further, another object of the present invention is to provide a cooling treatment method using molten slag as in the above-described cooling treatment apparatus.

再者,本發明另一目的在於提供使用此種冷卻處理方法的熔渣製品之製造方法。 Furthermore, another object of the present invention is to provide a method of producing a slag product using such a cooling treatment method.

為解決上述問題,本發明主旨如下: In order to solve the above problems, the gist of the present invention is as follows:

[1]一種熔化熔渣之冷卻處理裝置,係具備有:使熔化熔渣附著於外周滾筒面(100)上並予以冷卻,且可旋轉的單一橫式冷卻滾筒(1);以及對該橫式冷卻滾筒(1)供應熔化熔渣的盛桶(2);其中,滾筒面(100)上所附著並經冷卻的熔渣,係隨橫式冷卻滾筒(1)的旋轉,從滾筒面(100)上剝離並朝一方向排出。 [1] A cooling treatment apparatus for melting slag, comprising: a single horizontal cooling drum (1) that causes molten slag to adhere to a peripheral drum surface (100) and is cooled, and rotatable; The cooling drum (1) supplies a barrel (2) for melting the slag; wherein the slag attached to the drum surface (100) and cooled is rotated by the horizontal cooling drum (1) from the drum surface ( 100) peel off and discharge in one direction.

[2]如上述[1]之熔化熔渣之冷卻處理裝置,其中,以使盛桶(2)之前端部鄰接或靠近於橫式冷卻滾筒(1)的滾筒面(100)之方式設置盛桶(2),熔化熔渣係從盛桶(2)前端部直接供應給滾筒面(100),並附著於滾筒面(100)上。 [2] The cooling treatment device for molten slag according to [1] above, wherein the front end portion of the tub (2) is adjacent to or close to the drum surface (100) of the horizontal cooling drum (1) The tub (2), the molten slag is directly supplied to the drum surface (100) from the front end portion of the tub (2), and is attached to the drum surface (100).

[3]如上述[1]之熔化熔渣之冷卻處理裝置,其中,以使盛桶(2)之前端部鄰接或靠近於橫式冷卻滾筒(1)的滾筒面(100)之方式設置盛桶(2),且利用盛桶(2)與滾筒面(100)形成熔渣液滯留部(A),並隨橫式冷卻滾筒(1)的旋轉,熔渣 液滯留部(A)內的熔化熔渣會附著於滾筒面(100)上並被帶出。 [3] The cooling treatment device for molten slag according to the above [1], wherein the front end portion of the tub (2) is adjacent to or close to the drum surface (100) of the horizontal cooling drum (1). a barrel (2), and a slag liquid retention portion (A) is formed by the barrel (2) and the drum surface (100), and the slag is rotated with the horizontal cooling drum (1) The molten slag in the liquid retention portion (A) adheres to the drum surface (100) and is taken out.

[4]如上述[1]~[3]項中任一項之熔化熔渣之冷卻處理裝置,其中,具有用於將橫式冷卻滾筒(1)的滾筒面(100)上所附著之熔化熔渣施行軋延並朝滾筒寬度方向拉伸的拉伸輥(3)。 [4] The cooling treatment apparatus for molten slag according to any one of the above [1] to [3], which has melting for adhesion to the drum surface (100) of the horizontal cooling drum (1) The slag is subjected to a stretching roll (3) which is rolled and stretched toward the width of the drum.

[5]如上述[1]之熔化熔渣之冷卻處理裝置,其中,以使盛桶(2)之前端部鄰接或靠近於橫式冷卻滾筒(1)的滾筒面(100)之方式設置盛桶(2),且在橫式冷卻滾筒(1)上方設置堰(4),利用該堰(4)、滾筒面(100)及盛桶(2)形成熔渣液滯留部(A),且在堰(4)與橫式冷卻滾筒(1)間,設有將熔渣液滯留部(A)內的熔化熔渣擠出之開口(5)。 [5] The cooling treatment device for molten slag according to the above [1], wherein the front end portion of the tub (2) is adjacent to or close to the drum surface (100) of the horizontal cooling drum (1). a barrel (2), and a crucible (4) is disposed above the horizontal cooling drum (1), and the slag liquid retention portion (A) is formed by the crucible (4), the drum surface (100), and the barrel (2), and An opening (5) for extruding molten slag in the slag liquid retention portion (A) is provided between the crucible (4) and the horizontal cooling drum (1).

[6]如上述[5]之熔化熔渣之冷卻處理裝置,其中,堰(4)係由冷卻滾筒(4x)構成,該冷卻滾筒(4x)係下部外周面具有朝反熔渣液滯留部(A)方向旋轉的旋轉方向。 [6] The cooling treatment device for molten slag according to the above [5], wherein the crucible (4) is constituted by a cooling drum (4x) having a lower outer peripheral surface having an anti-slag liquid retention portion (A) Direction of rotation in the direction of rotation.

[7]如上述[3]~[6]項中任一項之熔化熔渣之冷卻處理裝置,其中,具有為將流體朝熔渣液滯留部(A)內吹入的流體供應手段(6)。 [7] The cooling treatment apparatus for molten slag according to any one of the above [3], wherein the fluid supply means for blowing the fluid into the slag liquid retention portion (A) is provided (6) ).

[8]如上述[1]~[7]項中任一項之熔化熔渣之冷卻處理裝置,其中,設有用於將從橫式冷卻滾筒(1)的滾筒面(100)所剝離的熔渣施行冷卻的冷卻手段(7)。 [8] The cooling treatment apparatus for molten slag according to any one of the above [1] to [7], wherein the melting treatment for peeling off the drum surface (100) of the horizontal cooling drum (1) is provided. The slag is cooled by means of cooling (7).

[9]一種熔化熔渣之冷卻處理方法,係使用上述[1]~[8] 項中任一項之冷卻處理裝置,對熔化熔渣施行冷卻處理。 [9] A cooling treatment method for molten slag, which uses the above [1]~[8] The cooling treatment device according to any one of the preceding claims, wherein the molten slag is subjected to a cooling treatment.

[10]如上述[9]之熔化熔渣之冷卻處理方法,係使用具有拉伸輥(3)之冷卻處理裝置者,將熔渣鹼度[質量比:%CaO/%SiO2]達2以上的熔化熔渣作為處理對象,並將滾筒面(100)上所附著之熔化熔渣,利用拉伸輥(3)施行軋延而朝滾筒寬度方向拉伸。 [10] The cooling treatment method of the molten slag according to the above [9], which uses a cooling treatment apparatus having a stretching roll (3), and has a slag basicity [mass ratio: %CaO/%SiO 2 ] of 2 The molten slag described above is treated as a target, and the molten slag adhering to the drum surface (100) is rolled by the stretching roll (3) and stretched in the roll width direction.

[11]如上述[9]之熔化熔渣之冷卻處理方法,係使用具有堰(4)的冷卻處理裝置者,其從開口(5)擠出熔渣。 [11] The method for cooling a molten slag according to [9] above, wherein a cooling treatment apparatus having ruthenium (4) is used, which extrudes slag from the opening (5).

[12]如上述[11]之熔化熔渣之冷卻處理方法,其中,從開口(5)擠出厚度5mm以上的板狀熔渣。 [12] The method for cooling a molten slag according to [11] above, wherein the plate-shaped slag having a thickness of 5 mm or more is extruded from the opening (5).

[13]如上述[9]~[12]項中任一項之熔化熔渣之冷卻處理方法,其係,使用具有熔渣液滯留部(A)的冷卻處理裝置者,在熔渣液滯留部(A)內的熔化熔渣中添加粉體。 [13] The method for cooling a molten slag according to any one of the above [9] to [12], wherein the slag liquid is retained by using a cooling treatment device having a slag liquid retention portion (A) Powder is added to the molten slag in the portion (A).

[14]如上述[9]~[13]項中任一項之熔化熔渣之冷卻處理方法,係使用具有熔渣液滯留部(A)的冷卻處理裝置者,對熔渣液滯留部(A)內的熔化熔渣中吹入流體。 [14] The method for cooling a molten slag according to any one of the above [9] to [13], wherein the slag liquid retention portion is used in a cooling treatment device having a slag liquid retention portion (A) A fluid is blown into the molten slag in A).

[15]如上述[9]~[14]項中任一項之熔化熔渣之冷卻處理方法,係進行下述(i)~(iv)中至少1者的熱回收:(i)從通過橫式冷卻滾筒(1)內部的冷媒中施行熱回收;(ii)使用具有堰(4)之冷卻處理裝置的熔化熔渣之冷卻處理中,從通過堰(4)內部的冷媒進行熱回收;(iii)將以橫式冷卻滾筒(1)冷卻的熔渣,更進一步使與冷 媒相接觸,而從該冷媒中施行熱回收;(iv)使用具有熔渣液滯留部(A)之冷卻處理裝置的熔化熔渣之冷卻處理時,於在熔渣液滯留部(A)內的熔化熔渣中吹入流體時,將所吹入的流體回收,且從該流體施行熱回收。 [15] The method for cooling a molten slag according to any one of the above [9] to [14], wherein the heat recovery is performed by at least one of the following (i) to (iv): (i) passing Heat recovery is performed in the refrigerant inside the horizontal cooling drum (1); (ii) in the cooling treatment using the molten slag having the cooling treatment device of the crucible (4), heat recovery is performed from the refrigerant passing through the crucible (4); (iii) further cooling the slag cooled by the horizontal cooling drum (1) The medium is in contact with the heat recovery from the refrigerant; (iv) in the cooling treatment of the molten slag using the cooling treatment device having the slag liquid retention portion (A), in the slag liquid retention portion (A) When the fluid is blown into the molten slag, the blown fluid is recovered, and heat recovery is performed from the fluid.

[16]一種熔渣製品之製造方法,係將利用上述[9]~[15]項中任一項冷卻處理方法進行冷卻、並經凝固的熔渣,施行破碎處理或/及磨碎處理,而獲得粒狀熔渣製品。 [16] A method for producing a slag product, which is a slag which is cooled and solidified by the cooling treatment method according to any one of the above [9] to [15], and is subjected to a crushing treatment and/or a grinding treatment. A granular slag product is obtained.

另外,本發明中,堰(4)與橫式冷卻滾筒(1)間的開口(5),係有視堰(4)或橫式冷卻滾筒(1)的外面形狀等,而間歇式形成(即,堰(4)與橫式冷卻滾筒(1)之間間歇性形成開口)的情況,此時,熔渣液滯留部(A)內的熔化熔渣係從開口(5)擠出呈不連續狀。 Further, in the present invention, the opening (5) between the crucible (4) and the horizontal cooling drum (1) is formed by intermittently forming the outer shape of the crucible (4) or the horizontal cooling drum (1). That is, when the crucible (4) and the horizontal cooling drum (1) intermittently form an opening), at this time, the molten slag in the slag liquid retention portion (A) is extruded from the opening (5). Continuous.

本發明的熔化熔渣之冷卻處理裝置及冷卻處理方法中,成為冷卻處理之對象的熔渣種類並無限制,例如可為:高爐熔渣、製鋼熔渣(例如:轉爐脫碳熔渣、脫磷熔渣、脫矽熔渣、脫硫熔渣、電爐熔渣、鑄造熔渣等)、熔融還原熔渣(例如:鐵礦、Cr礦、Ni礦、Mn礦等依熔融還原所產生的熔渣)、從其他冶煉爐、精煉爐所產生的熔渣、垃圾焚化灰熔化熔渣、廢棄物氣體化熔化熔渣等各種熔渣。 In the cooling treatment apparatus and the cooling treatment method of the molten slag according to the present invention, the type of the slag to be subjected to the cooling treatment is not limited, and for example, it may be: blast furnace slag or steel slag (for example, converter decarburization slag or detachment) Phosphate slag, desulfurization slag, desulfurization slag, electric furnace slag, casting slag, etc.), smelting reduction slag (for example: iron ore, Cr ore, Ni ore, Mn ore, etc. Slag), slag generated from other smelting furnaces, refining furnaces, ash incineration ash melting slag, waste gasification melting slag, and other slag.

圖1所示係本發明的熔化熔渣之冷卻處理裝置及冷卻處理方法一實施形態的示意正視圖。 Fig. 1 is a schematic front elevational view showing an embodiment of a cooling treatment device and a cooling treatment method for a molten slag according to the present invention.

本熔化熔渣之冷卻處理裝置係具備有:於外周的滾筒面100上附著熔化熔渣並予以冷卻,且可旋轉的單一橫式冷卻滾筒1(以下簡稱「冷卻滾筒1」。其他實施形態亦同);以及對該冷卻滾筒1供應熔化熔渣的盛桶2。此處所謂橫式冷卻滾筒的「橫式」,係指滾筒的旋轉軸概略呈水平。 The cooling treatment device for the molten slag includes a single horizontal cooling drum 1 (hereinafter referred to as "cooling drum 1") which is provided with a molten slag attached to the outer drum surface 100 and cooled, and is also referred to as "cooling drum 1". And the tub 2 for supplying the molten slag to the cooling drum 1. Here, the "horizontal type" of the horizontal cooling drum means that the rotation axis of the drum is substantially horizontal.

上述盛桶2係配置於冷卻滾筒徑方向之其中一側,從適當高度朝冷卻滾筒1的上部滾筒面供應熔化熔渣S。對該盛桶2的上游側從熔渣鍋等供應熔化熔渣S。 The tub 2 is disposed on one side of the radial direction of the cooling drum, and supplies the molten slag S from the appropriate height toward the upper drum surface of the cooling drum 1. The molten slag S is supplied from the slag pot or the like to the upstream side of the tub 2 .

盛桶2的形態係任意,藉由使用於冷卻滾筒寬度方向(滾筒軸方向)上具有充分寬度者,便可使熔化熔渣朝滾筒寬度方向擴大,可將熔化熔渣利用滾筒面100均勻地冷卻。 The form of the tub 2 is arbitrary, and by using a sufficient width in the width direction of the cooling drum (the direction of the drum axis), the molten slag can be expanded toward the width direction of the drum, and the molten slag can be uniformly distributed by the drum surface 100. cool down.

冷卻滾筒1係利用驅動裝置(未圖示),依上部滾筒面朝反盛桶方向旋轉的方式進行旋轉驅動。從盛桶2所供應的熔化熔渣S,在附著於滾筒面100上並冷卻後,隨冷卻滾筒1的旋轉而從滾筒面100上剝離,並排出於冷卻滾筒徑方向之另一側。 The cooling drum 1 is rotationally driven by a driving device (not shown) so as to rotate in the direction of the counter drum in the upper drum surface. The molten slag S supplied from the tub 2 is attached to the drum surface 100 and cooled, and then peeled off from the drum surface 100 as the cooling drum 1 rotates, and is discharged to the other side in the radial direction of the cooling drum.

另外,冷卻滾筒1最好能配合操業條件對旋轉數進行控制。 Further, it is preferable that the cooling drum 1 can control the number of rotations in accordance with the operating conditions.

在上述冷卻滾筒1的內部設有具備供冷媒通過用之流路的內部冷卻機構(未圖示),在滾筒軸各端部分別設置對該內部冷卻機構的冷媒供應部與冷媒排出部。另外,冷媒一般係使用水(冷卻水),但亦可使用其他流體(液體或氣體)。 An internal cooling mechanism (not shown) including a flow path through which the refrigerant passes is provided inside the cooling drum 1, and a refrigerant supply unit and a refrigerant discharge unit for the internal cooling mechanism are provided at respective ends of the drum shaft. In addition, the refrigerant generally uses water (cooling water), but other fluids (liquid or gas) may also be used.

在冷卻滾筒徑方向之另一側,配置著用於收取經冷卻而從滾筒面100剝離的熔渣Sx、並進行搬送的搬送輸送帶8。附著於冷卻滾筒1表面並冷卻的熔渣,係在滾筒面100開始繞入滾筒下方側的旋轉位置處,因自重而從滾筒面100上剝離,因而本實施形態的搬送輸送帶8係配置於能承接如此剝離之熔渣Sx的高度位置處。另外,亦可設有用於將從滾筒面100上剝離的熔渣Sx導引於搬送輸送帶8用的導引構件。 On the other side of the cooling drum radial direction, a transport conveyor belt 8 for collecting and transporting the slag Sx which has been cooled and peeled off from the drum surface 100 is disposed. The slag adhering to the surface of the cooling drum 1 and being cooled is detached from the drum surface 100 by the self-weight at the rotational position of the drum surface 100 at the lower side of the drum, so that the transport conveyor 8 of the present embodiment is disposed. It is capable of receiving the height position of the slag Sx thus peeled off. Further, a guide member for guiding the slag Sx peeled off from the drum surface 100 to the conveyance conveyor belt 8 may be provided.

在搬送輸送帶8的搬送目的地處設置用於承接熔渣Sx,並藉由將該熔渣Sx利用冷媒施行冷卻而進行熱回收的熔渣桶9。 A slag bucket 9 for receiving the slag Sx and carrying out heat recovery by cooling the slag Sx with a refrigerant is provided at a transfer destination of the conveyance conveyor 8.

另外,亦可不設置搬送輸送帶8,而在冷卻滾筒1與熔渣桶9間設置滑槽,俾將從冷卻滾筒1上剝離的熔渣Sx,經由該滑槽裝入於熔渣桶9中。 Further, a transporting belt 8 may not be provided, and a chute may be provided between the cooling drum 1 and the slag tank 9, and the slag Sx peeled from the cooling drum 1 may be loaded into the slag tank 9 via the chute. .

再者,本實施形態的冷卻滾筒1係表面呈平滑的圓筒體,惟未必僅侷限於此,亦可設有溝等凹凸。 Further, the cooling drum 1 of the present embodiment has a smooth cylindrical surface, but is not limited thereto, and may have irregularities such as grooves.

使用如上述冷卻處理裝置的熔化熔渣之冷卻處理,係將從盛桶2中流下的熔化熔渣S供應給冷卻滾筒1的滾筒面100,而該熔化熔渣S係以在滾筒面100上附著呈板狀的狀態下,冷卻至適度凝固狀態(例如半凝固狀態、或者僅單面或雙面表層凝固的狀態)後,在既定滾筒旋轉位置處利用自重從冷卻滾筒面自然剝離,該經剝離的熔渣Sx直接由搬送輸送帶8收取,並利用該搬送輸送帶8進行搬送且裝入至熔 渣桶9中。另外,搬送輸送帶8的搬送速度係大致與冷卻滾筒1的周速一致。 The cooling treatment using the molten slag of the above-described cooling treatment apparatus supplies the molten slag S flowing down from the tub 2 to the drum surface 100 of the cooling drum 1, and the molten slag S is applied to the drum surface 100. When it adheres to a plate shape, it is cooled to a moderately solidified state (for example, a semi-solidified state or a state in which only one surface or double-sided surface layer is solidified), and then naturally peeled off from the cooling drum surface by its own weight at a predetermined drum rotation position. The peeled slag Sx is directly collected by the transport conveyor 8 and transported by the transport conveyor 8 and loaded into the melt In the slag bucket 9. Moreover, the conveyance speed of the conveyance conveyor 8 is substantially the same as the circumferential speed of the cooling drum 1.

如上述的熔化熔渣S之冷卻處理,因為從單一冷卻滾筒1的滾筒面100上剝離之冷卻處理完之熔渣Sx被朝一方向排出,因而冷卻處理完之熔渣的處置‧後處理等較為容易。所以,從冷卻處理完之熔渣Sx施行顯熱回收時,亦可利用1個熱回收設備有效率地施行熱回收。此外,因為不會因熔化熔渣S而對冷卻滾筒1施加較大的落下荷重,因而能在不致損耗冷卻滾筒1的情況下,大量處理熔化熔渣S。 In the cooling treatment of the molten slag S as described above, since the slag Sx subjected to the cooling treatment which is peeled off from the drum surface 100 of the single cooling drum 1 is discharged in one direction, the treatment of the slag after the cooling treatment is performed, and the post treatment is performed. easily. Therefore, when sensible heat recovery is performed from the cooled slag Sx, heat recovery can be efficiently performed by one heat recovery apparatus. Further, since a large drop load is not applied to the cooling drum 1 by melting the slag S, the molten slag S can be processed in a large amount without losing the cooling drum 1.

對熔渣桶9內供應冷媒,並施行熔渣Sx的冷卻。另外,從冷卻滾筒1上剝離的熔渣Sx之冷卻,亦可利用其他手段或場所實施。經冷卻之熔渣Sx被輸送給用於作成熔渣製品的破碎處理或/及磨碎處理的步驟,且視需要利用篩分等施行整粒。 The refrigerant is supplied into the slag tank 9 and the slag Sx is cooled. Further, the cooling of the slag Sx peeled off from the cooling drum 1 can be carried out by other means or places. The cooled slag Sx is supplied to a step of performing a crushing treatment and/or a grinding treatment for forming a slag product, and is subjected to sizing by sieving or the like as necessary.

通常,剛利用冷卻滾筒1完成冷卻後的熔渣Sx,係呈現如上述的適度凝固狀態,因為尚具有可塑性,因而從冷卻滾筒面上剝離,並由搬送輸送帶8收取的熔渣Sx係呈板狀連續體。但,依照熔渣Sx的厚度、凝固程度,在從冷卻滾筒面上剝離、並由搬送輸送帶8收取的期間,板狀熔渣的連續體有時會遭粉碎,但並不會構成問題。 Usually, the slag Sx which has just been cooled by the cooling drum 1 exhibits a moderately solidified state as described above, and since it has plasticity, it is peeled off from the cooling drum surface, and the slag Sx collected by the conveying conveyor belt 8 is Plate-like continuum. However, depending on the thickness of the slag Sx and the degree of solidification, the continuous body of the plate-shaped slag may be pulverized while being peeled off from the surface of the cooling drum and collected by the conveyance belt 8, but it does not pose a problem.

另外,將熔渣Sx從搬送輸送帶8輸送給桶等時,視需要亦可將熔渣Sx利用適當手段施行粗破碎。 Further, when the slag Sx is transported from the transport conveyor 8 to the tub or the like, the slag Sx may be coarsely crushed by an appropriate means as needed.

圖2所示係本發明的熔化熔渣之冷卻處理裝置及冷卻處理方法另一實施形態的示意正視圖。 Fig. 2 is a schematic front elevational view showing another embodiment of a cooling treatment apparatus and a cooling treatment method for molten slag according to the present invention.

本實施形態中,盛桶2係以使其前端部鄰接或靠近於冷卻滾筒1的滾筒面100,並將熔化熔渣S從盛桶2前端部直接供應給滾筒面100,而附著於滾筒面100。 In the present embodiment, the tub 2 is such that its front end portion is adjacent to or close to the drum surface 100 of the cooling drum 1, and the molten slag S is directly supplied from the front end portion of the tub 2 to the drum surface 100, and is attached to the drum surface. 100.

盛桶2的前端部亦可鄰接於滾筒面100,亦可形成小間隙而靠近於滾筒面100。後者的情況,最好經考慮熱膨脹等,以具有熔化熔渣S不會洩漏之程度的間隙使其靠近,但為了確實防止熔化熔渣S洩漏,最好對該間隙部分從在盛桶2下方所設置之氣體噴射手段10噴射出迫淨氣體。 The front end portion of the tub 2 may be adjacent to the drum surface 100, or may form a small gap to be close to the drum surface 100. In the latter case, it is preferable to consider the thermal expansion or the like to bring the molten slag S into contact with the gap so that the molten slag S does not leak, but in order to surely prevent the molten slag S from leaking, it is preferable that the gap portion is from below the tub 2 The gas injection means 10 provided is sprayed with a forced gas.

關於該盛桶前端部與滾筒面100的間隙,雖依熔化熔渣的黏性而異,但在高溫下實施熔渣處理時,最寬亦較佳在5mm以下、更佳3mm以下、特佳1mm以下。間隙越狹窄,越能減少迫淨氣體量。能在無迫淨氣體的情況下抑制熔化熔渣洩漏的間隙極限,雖大幅依存於熔化熔渣性狀(黏性),但若能將間隙設定在1mm或以下的幾乎無接觸狀態,則幾乎任何情況下均即使無迫淨氣體仍可抑制熔化熔渣洩漏。因為間隙越狹窄,越會促進盛桶前端部因接觸所導致之滾筒面磨損、損耗,因而關於會接觸到滾筒面之可能性較高的盛桶前端部,最好利用滑性佳的碳質、或氮化硼等其他材料構成。其中,間隙值係實際操業時(高溫狀態)的數值,當在常溫設置裝置時,必需如上述考慮冷卻滾筒熱膨脹。以下例示熱膨脹一 例。鋼性直徑1.6m ψ的冷卻滾筒時,鋼熱膨脹率係15×10-6,滾筒材料平均溫度200℃時,因熱膨脹朝徑方向上延伸的長度成為半徑800mm×200℃×15×10-6=2.4mm。 The gap between the front end portion of the tub and the drum surface 100 varies depending on the viscosity of the molten slag. However, when the slag treatment is performed at a high temperature, the widest width is preferably 5 mm or less, more preferably 3 mm or less. 1mm or less. The narrower the gap, the more the amount of forced gas can be reduced. The gap limit that can suppress the leakage of molten slag without the use of a forced gas, although depending on the properties of the molten slag (viscosity), if the gap can be set to a bare contact state of 1 mm or less, almost any In the case, even if there is no forced gas, the molten slag can be suppressed from leaking. Because the narrower the gap, the more the drum surface wear and loss caused by the contact at the front end of the tub is promoted. Therefore, it is preferable to use the carbon property with good sliding property with respect to the front end portion of the tub which is likely to contact the drum surface. Or other materials such as boron nitride. Among them, the gap value is a value at the time of actual operation (high temperature state), and when the device is set at a normal temperature, it is necessary to consider the thermal expansion of the cooling drum as described above. An example of thermal expansion is exemplified below. When the steel has a diameter of 1.6 m 冷却 cooling drum, the thermal expansion coefficient of the steel is 15×10 -6 , and when the average temperature of the roller material is 200° C., the length extending in the radial direction due to thermal expansion becomes a radius of 800 mm×200° C×15×10 -6 . =2.4mm.

另外,因為本實施形態的其餘構造均如同圖1所示實施形態,因而省略詳細說明。 In addition, since the rest of the structure of this embodiment is the embodiment shown in FIG. 1, the detailed description is abbreviate|omitted.

使用如上述冷卻處理裝置的熔化熔渣之冷卻處理,因為對冷卻滾筒1幾乎不會施加因熔化熔渣S所產生的落下荷重,因而可更加減輕冷卻滾筒1的損耗。 By using the cooling treatment of the molten slag of the above-described cooling treatment apparatus, since the falling load due to the molten slag S is hardly applied to the cooling drum 1, the loss of the cooling drum 1 can be further alleviated.

圖3所示係本發明的熔化熔渣之冷卻處理裝置及冷卻處理方法另一實施形態的示意正視圖。 Fig. 3 is a schematic front elevational view showing another embodiment of a cooling treatment apparatus and a cooling treatment method for molten slag according to the present invention.

本實施形態中,盛桶2係設置成其前端部鄰接或靠近冷卻滾筒1的滾筒面100,且利用盛桶2的前端部分與滾筒面100形成熔渣液滯留部A,隨冷卻滾筒1的旋轉,熔渣液滯留部A內的熔化熔渣S附著於滾筒面100上並被帶出。為了形成熔渣液滯留部A,盛桶2的前端部分具有朝上側(水平狀)曲撓或彎曲的承接皿狀形態,且盛桶2的前端部鄰接或靠近於下部滾筒面。 In the present embodiment, the tub 2 is provided such that the front end portion thereof is adjacent to or close to the drum surface 100 of the cooling drum 1, and the slag liquid retention portion A is formed by the front end portion of the tub 2 and the drum surface 100, with the cooling drum 1 After the rotation, the molten slag S in the slag liquid retention portion A adheres to the drum surface 100 and is taken out. In order to form the slag liquid retention portion A, the front end portion of the tub 2 has a receiving dish shape that is curved or curved toward the upper side (horizontal shape), and the front end portion of the tub 2 is adjacent to or close to the lower drum surface.

再者,形成熔渣液滯留部A的盛桶前端部分之側壁200,為了保持熔化熔渣S而具有既定高度。 Further, the side wall 200 of the front end portion of the tub which forms the slag liquid retention portion A has a predetermined height in order to hold the molten slag S.

另外,因為本實施形態的其餘構造均如同圖1所示實施形態,因而省略詳細說明。 In addition, since the rest of the structure of this embodiment is the embodiment shown in FIG. 1, the detailed description is abbreviate|omitted.

使用如上述冷卻處理裝置的熔化熔渣之冷卻處理中,供應 給盛桶2的熔化熔渣S流入至熔渣液滯留部A中,藉由在此滯留適當時間而冷卻後,附著於冷卻滾筒1的滾筒面100上並被帶出,如同圖1與圖2之實施形態,再附著於滾筒面100的狀態下,經冷卻至適度凝固狀態(例如半凝固狀態、或者僅單面或雙面表層凝固的狀態)後,再於既定之滾筒旋轉位置處利用自重從冷卻滾筒面上自然剝離。本實施形態中,藉由熔化熔渣S在熔渣液滯留部A內滯留充分地時間而促進冷卻,因此可輕易地獲得厚板熔渣Sx。 Supplying using a cooling slag of a cooling treatment device as described above, The molten slag S of the tub 2 flows into the slag liquid retention portion A, and after being cooled for a suitable period of time, it is attached to the drum surface 100 of the cooling drum 1 and taken out, as shown in Fig. 1 and In the embodiment of the second embodiment, after being adhered to the drum surface 100, it is cooled to a moderately solidified state (for example, a semi-solidified state or a state in which only one surface or both surfaces are solidified), and then used at a predetermined drum rotation position. The self-weight is naturally peeled off from the surface of the cooling drum. In the present embodiment, the molten slag S is retained in the slag liquid retention portion A for a sufficient period of time to promote cooling, so that the thick plate slag Sx can be easily obtained.

圖4~圖6所示係本發明的熔化熔渣之冷卻處理裝置及冷卻處理方法另一實施形態示意,圖4所示係正視圖,圖5所示係平面圖,圖6所示係冷卻滾筒上所附設之拉伸輥的作用的說明圖。 4 to 6 are schematic views showing another embodiment of a cooling treatment device and a cooling treatment method for a molten slag according to the present invention, and Fig. 4 is a front view, Fig. 5 is a plan view, and Fig. 6 is a cooling roller. An explanatory view of the action of the stretching roller attached thereto.

本實施形態的冷卻處理裝置係設有用於將冷卻滾筒1的滾筒面100上所附著之熔化熔渣S施行軋延,而朝滾筒寬度方向拉伸的拉伸輥3,特別適用於黏度較高且熔渣鹼度[質量比:%CaO/%SiO2](以下簡稱「鹼度」)達2以上的熔化熔渣之冷卻處理。鹼度≧2的熔渣係有如:普通鋼及不銹鋼的轉爐脫碳精煉熔渣、脫磷熔渣、電爐熔渣等製鋼熔渣、廢棄物氣體化熔化熔渣、垃圾焚化灰熔化熔渣等。 The cooling treatment apparatus according to the present embodiment is provided with a stretching roll 3 for rolling the molten slag S attached to the drum surface 100 of the cooling drum 1 and stretching in the width direction of the drum, and is particularly suitable for high viscosity. Further, the slag basicity [mass ratio: %CaO/%SiO 2 ] (hereinafter referred to as "basicity") is a cooling treatment of molten slag of 2 or more. The slag of alkalinity ≧2 is, for example, converter decarburization refining slag, dephosphorization slag, electric furnace slag, steel slag, waste gasification melting slag, waste incineration ash melting slag, etc. .

在冷卻滾筒1的上部,平行於冷卻滾筒1而設置屬於熔渣拉伸手段的拉伸輥3。該拉伸輥3係將冷卻滾筒1的滾筒面100(上部外周面)所附著之熔化熔渣S施行軋延,並朝滾筒 寬度方向拉伸,依其外周面300與冷卻滾筒1的滾筒面100之間形成既定間隔t之方式,由支撐臂11旋轉自如地支撐。本實施形態中,在支撐臂11前端(下端)形成朝上下方向拉長的長圓形軸承孔110,在該軸承孔110中可上下滑動地支撐著拉伸輥3的輥軸301。所以,本實施形態的拉伸輥3係非驅動,而是利用自重將冷卻滾筒1的上部滾筒面所附著之熔化熔渣S軋延成間隔t的厚度。 In the upper portion of the cooling drum 1, a stretching roller 3 belonging to a slag drawing means is provided in parallel with the cooling drum 1. The drawing roll 3 performs rolling rolling of the molten slag S adhered to the drum surface 100 (upper outer peripheral surface) of the cooling drum 1, and is directed toward the drum The support arm 11 is rotatably supported so as to form a predetermined interval t between the outer peripheral surface 300 and the drum surface 100 of the cooling drum 1 in the width direction. In the present embodiment, an elliptical bearing hole 110 elongated in the vertical direction is formed at the front end (lower end) of the support arm 11, and the roller shaft 301 of the stretching roller 3 is supported by the bearing hole 110 so as to be slidable up and down. Therefore, the drawing roll 3 of the present embodiment is not driven, but the molten slag S adhered to the upper drum surface of the cooling drum 1 is rolled to a thickness of the interval t by its own weight.

如本實施形態,藉由使拉伸輥3由支撐臂11支撐成可上下滑動,即使在冷卻滾筒面所附著之熔化熔渣中含有堅固塊狀物的情況,藉由拉伸輥3朝上方逃離便可使塊狀物通過。 According to the present embodiment, the stretching roller 3 is supported by the support arm 11 so as to be vertically slidable, and even if the molten slag adhering to the cooling drum surface contains a solid block, the stretching roller 3 faces upward. Escape can make the block pass.

另外,拉伸輥3亦可依與冷卻滾筒面之間具有既定間隔t的狀態,固定地支撐成可對支撐臂11旋轉自如的構造。此情況,最好拉伸輥3可在上下方向上進行位置調整,俾可調整間隔t。此外,旋轉自如地保持著拉伸輥3的輥軸承,亦可經由彈簧而由支撐臂11等所支撐,並利用該彈簧獲得適度按押力,且構成為當有異物卡入時便可使拉伸輥3退避的構造。此外,拉伸輥3亦可設定為驅動輥。 Further, the stretching roller 3 may be fixedly supported so as to be rotatable with respect to the support arm 11 in a state of having a predetermined interval t from the surface of the cooling drum. In this case, it is preferable that the stretching roller 3 can be positionally adjusted in the up and down direction, and the interval t can be adjusted. Further, the roller bearing of the stretching roller 3 is rotatably held, and can be supported by the support arm 11 or the like via a spring, and the spring is used to obtain a moderate pressing force, and is configured to be able to be engaged when foreign matter is caught. The structure in which the stretching roll 3 is retracted. Further, the stretching roller 3 can also be set as a driving roller.

拉伸輥3係用於將冷卻滾筒面所附著熔化熔渣S施行軋延並拉伸用,外徑最好充分小於冷卻滾筒1的外徑,但若輥長度變長,則因熔渣熱或自重而發生曲撓、或與冷卻滾筒面間的間隔t在滾筒寬度方向上容易發生變動,因而最好配合輥長度與輥剛性而選擇外徑。 The stretching roller 3 is used for rolling and stretching the molten slag S attached to the cooling drum surface, and the outer diameter is preferably sufficiently smaller than the outer diameter of the cooling drum 1, but if the length of the roller becomes long, the slag heat is generated. The bending of the self-weight or the interval t between the surfaces of the cooling rolls tends to fluctuate in the width direction of the roll. Therefore, it is preferable to select the outer diameter in accordance with the length of the roll and the rigidity of the roll.

再者,相關拉伸輥3,從熔化熔渣冷卻效率及拉伸輥耐久性的觀點而言,最好具有如同上述冷卻滾筒1的內部冷卻機構。 Further, the related stretching rolls 3 preferably have an internal cooling mechanism like the above-described cooling drum 1 from the viewpoint of melting slag cooling efficiency and durability of the stretching rolls.

再者,亦可將拉伸輥3設置於冷卻滾筒圓周方向的複數地方,藉由該等複數拉伸輥3而對滾筒面所附著之熔渣施行多段軋延。 Further, the stretching rolls 3 may be placed at a plurality of places in the circumferential direction of the cooling drum, and the slag adhering to the drum surface may be rolled in a plurality of stages by the plurality of stretching rolls 3.

另外,因為本實施形態的其餘構造均如同圖3所示實施形態,因而省略詳細說明。此外,如本實施形態的拉伸輥3,亦可附設於如圖1、圖2所示形態的冷卻處理裝置中。 In addition, since the rest of the structure of this embodiment is the embodiment shown in FIG. 3, detailed description is abbreviate|omitted. Further, the stretching roll 3 of the present embodiment may be attached to the cooling processing apparatus of the embodiment shown in Figs. 1 and 2 .

利用如上述冷卻處理裝置對黏性較高熔化熔渣施行冷卻處理時,因為從熔渣液滯留部A中被帶出至冷卻滾筒1上,並附著於該滾筒面100上的黏性較高熔化熔渣S,係不易朝滾筒寬度方向(滾筒軸方向)擴展,因而呈現不均勻地附著在滾筒寬度方向上的滾筒面100之狀態(局部性附著於冷卻滾筒面的狀態)。在此狀態下,熔化熔渣S的冷卻效率(=每單位時間的熔渣散熱量/熔渣單位容積)非常差,且熔渣從冷卻滾筒1上剝離時的凝固狀態變得不均勻,導致品質發生變動。本實施形態中,係將如此不均勻附著在滾筒面100的熔化熔渣S,利用拉伸輥3施行軋延,而使其朝滾筒寬度方向拉伸。藉此,可提高熔化熔渣S的冷卻效率,且亦提高熔化熔渣S的冷卻速度。如同圖1~圖3的實施形態,熔化熔渣S在附著於冷卻滾筒面的狀態下,經冷卻至適度凝固狀態(例 如半凝固狀態、或僅表層凝固的狀態)後,在既定滾筒旋轉位置處利用自重從冷卻滾筒面上自然剝離。 When the viscous slag is cooled by the cooling treatment device as described above, it is carried out from the slag liquid retention portion A to the cooling drum 1 and adhered to the drum surface 100 with high viscosity. The molten slag S is not easily spread in the drum width direction (the drum axis direction), and thus exhibits a state in which the drum surface 100 is unevenly attached to the drum width direction (a state in which it is locally adhered to the cooling drum surface). In this state, the cooling efficiency of the molten slag S (= slag heat dissipation per unit time / slag unit volume) is very poor, and the solidified state when the slag is peeled off from the cooling drum 1 becomes uneven, resulting in unevenness Quality has changed. In the present embodiment, the molten slag S which is unevenly adhered to the drum surface 100 is rolled by the stretching rolls 3 and stretched in the drum width direction. Thereby, the cooling efficiency of the molten slag S can be increased, and the cooling rate of the molten slag S can also be increased. As in the embodiment of FIGS. 1 to 3, the molten slag S is cooled to a moderately solidified state in a state of being attached to the surface of the cooling drum (for example) After the semi-solidified state or the state in which only the surface layer is solidified, it is naturally peeled off from the surface of the cooling drum by its own weight at a predetermined drum rotation position.

依此,熔化熔渣S利用拉伸輥3朝滾筒寬度方向拉伸的結果,熔化熔渣S的厚度變薄,而提高熔渣的冷卻效率,提升生產性,且熔化熔渣S的冷卻速度亦提高,因而可獲得不易粉化的熔渣凝固體。此外,可獲得熔渣凝固狀態呈均勻化、均勻品質的熔渣凝固體。 According to this, as a result of the stretching of the molten slag S by the stretching rolls 3 in the width direction of the drum, the thickness of the molten slag S is thinned, the cooling efficiency of the slag is improved, the productivity is improved, and the cooling rate of the molten slag S is increased. It is also improved, so that a slag solidified body which is not easily pulverized can be obtained. Further, a slag solidified body in which the slag solidified state is uniform and uniform in quality can be obtained.

圖7所示係本發明的熔化熔渣之冷卻處理裝置及冷卻處理方法另一實施形態的示意平面圖。本實施形態的冷卻處理裝置,亦具有屬於熔渣拉伸手段的拉伸輥3。 Fig. 7 is a schematic plan view showing another embodiment of a cooling treatment apparatus and a cooling treatment method for molten slag according to the present invention. The cooling treatment apparatus of the present embodiment also has a stretching roll 3 which is a slag stretching means.

本實施形態中,係對冷卻滾筒1配置複數拉伸輥3x~3z。具體而言,係在冷卻滾筒旋轉方向之上游側位置的滾筒寬度方向中央部處配置拉伸輥3x,並於冷卻滾筒旋轉方向之下游側位置的滾筒寬度方向二側部分配置拉伸輥3y、3z。拉伸輥3y、3z在滾筒寬度方向的軋延範圍,係部份重疊於拉伸輥3x在滾筒寬度方向上的軋延範圍。依此,藉由在冷卻滾筒旋轉方向的上游側與下游側配置拉伸輥3x~3z,可將冷卻滾筒面上的熔化熔渣S階段性地依序拉伸。如本實施形態,因為較短的拉伸輥3x~3z在長邊方向的曲撓情形較小,因而有利於使冷卻滾筒寬度方向上的熔渣之軋延厚度均勻。 In the present embodiment, the plurality of stretching rolls 3x to 3z are disposed on the cooling drum 1. Specifically, the stretching rolls 3x are disposed at the center portion in the drum width direction at the upstream side of the cooling drum rotation direction, and the stretching rolls 3y are disposed on both sides in the drum width direction at the downstream side of the cooling drum rotating direction. 3z. The rolling range of the stretching rolls 3y and 3z in the width direction of the roll is partially overlapped with the rolling range of the stretching roll 3x in the roll width direction. According to this, by arranging the stretching rolls 3x to 3z on the upstream side and the downstream side in the rotation direction of the cooling drum, the molten slag S on the cooling drum surface can be sequentially stepwise stretched. According to the present embodiment, since the short stretching rolls 3x to 3z are less curved in the longitudinal direction, it is advantageous to make the rolling thickness of the slag in the width direction of the cooling drum uniform.

另外,因為本實施形態的其餘構造均如同圖4~6所示實施形態,因而省略詳細說明。 In addition, since the rest of the structure of this embodiment is the embodiment shown in FIGS. 4 to 6, the detailed description is omitted.

圖8所示係本發明的熔化熔渣之冷卻處理裝置及冷卻處理方法另一實施形態的示意正視圖。 Fig. 8 is a schematic front view showing another embodiment of a cooling treatment apparatus and a cooling treatment method for molten slag according to the present invention.

本實施形態係將盛桶2設置成其前端部鄰接或靠近於冷卻滾筒1的滾筒面100狀態,且在冷卻滾筒1上方設置堰4,利用該堰4、滾筒面100及盛桶2前端部分形成熔渣液滯留部A,在堰4與冷卻滾筒1之間形成使熔渣液滯留部A內的熔化熔渣擠出之開口5。 In the present embodiment, the tub 2 is disposed such that its front end portion abuts or is close to the drum surface 100 of the cooling drum 1, and a crucible 4 is disposed above the cooling drum 1, and the crucible 4, the drum surface 100, and the front end portion of the tub 2 are used. The slag liquid retention portion A is formed, and an opening 5 for extruding molten slag in the slag liquid retention portion A is formed between the crucible 4 and the cooling drum 1.

本實施形態目標在於獲得厚度5mm以上、較佳20mm以上的熔渣凝固體,因而開口5寬度(厚度)較佳設定為5mm以上、更佳20mm以上。此外,最好藉由能調整堰4的上下方向位置,而可改變開口5的寬度(厚度)。 The present embodiment is directed to obtaining a slag solidified body having a thickness of 5 mm or more, preferably 20 mm or more. Therefore, the width (thickness) of the opening 5 is preferably set to 5 mm or more, more preferably 20 mm or more. Further, it is preferable to change the width (thickness) of the opening 5 by adjusting the position of the up and down direction of the crucible 4.

上述堰4在本實施形態中係由固定式堰體4a(壁體)所構成,經由適當的支撐構件由裝置本體(基體)所支撐。亦可在堰體4a的內部設置具有供冷媒流通用之流路的內部冷卻機構(未圖示),此情況,分別設置對內部冷卻機構的冷媒供應部與冷媒排出部。另外,冷媒一般係使用水(冷卻水),但亦可使用其他流體(液體或氣體)。 In the present embodiment, the crucible 4 is composed of a fixed body 4a (wall), and is supported by a device body (base) via an appropriate supporting member. An internal cooling mechanism (not shown) having a flow path common to the refrigerant flow may be provided inside the body 4a. In this case, a refrigerant supply unit and a refrigerant discharge unit for the internal cooling mechanism are provided. In addition, the refrigerant generally uses water (cooling water), but other fluids (liquid or gas) may also be used.

另外,因為本實施形態的其餘構造均如同圖3所示實施形態,因而省略詳細說明。 In addition, since the rest of the structure of this embodiment is the embodiment shown in FIG. 3, detailed description is abbreviate|omitted.

使用如上述冷卻處理裝置的熔化熔渣之冷卻處理,供應給盛桶2的熔化熔渣S流入至熔渣液滯留部A中,藉由在此滯留適當時間而冷卻後,從冷卻滾筒1與堰4(堰體4a)之間的 開口5,一邊冷卻一邊擠出。擠出的熔化熔渣S在附著於冷卻滾筒面的狀態下,經冷卻至適度凝固狀態(例如半凝固狀態、或者僅單面或雙面表層凝固的狀態)後,便如同圖1~圖3的實施形態,在既定滾筒旋轉位置處利用自重從冷卻滾筒面上自然剝離。 The cooling slag S supplied to the tub 2 flows into the slag liquid retention portion A by using the cooling treatment of the molten slag as in the above-described cooling treatment device, and after cooling for a suitable period of time, from the cooling drum 1 and Between 堰4 (堰4a) The opening 5 is extruded while cooling. The extruded molten slag S is cooled to a moderately solidified state (for example, a semi-solidified state, or a state in which only one or both surfaces are solidified) in a state of being attached to the surface of the cooling drum, as shown in FIGS. 1 to 3 . In the embodiment, the self-weight is naturally peeled off from the surface of the cooling drum at a predetermined drum rotation position.

此種熔化熔渣的冷卻處理,係藉由熔化熔渣S在熔渣液滯留部A內滯留充分時間,而促進冷卻,並在從開口5中擠出時亦利用冷卻滾筒1進行冷卻,因而即使充分加大開口5寬度(厚度)而擠出厚板熔渣Sx時,仍可將熔化熔渣S適當地冷卻。因此可從開口5擠出經適當冷卻且厚度5mm以上的厚板之板狀熔渣Sx。根據本實施形態,亦可輕易地製造厚度20~30mm左右的厚板熔渣凝固體。 The cooling treatment of the molten slag is accelerated by the molten slag S in the slag liquid retention portion A for a sufficient period of time to promote cooling, and is also cooled by the cooling drum 1 when being extruded from the opening 5. Even when the thick plate slag Sx is sufficiently enlarged by increasing the width (thickness) of the opening 5, the molten slag S can be appropriately cooled. Therefore, the plate-like slag Sx of the thick plate which is appropriately cooled and has a thickness of 5 mm or more can be extruded from the opening 5. According to this embodiment, it is also possible to easily manufacture a thick plate slag solidified body having a thickness of about 20 to 30 mm.

另外,圖8所示實施形態中,當堰體4a不具有特別內部冷卻機構的情況,從開口5擠出的熔渣Sx,通常係鄰接冷卻滾筒1之側的下面與二側端面凝固,而上面側則呈熔融或半熔融狀態,但若所擠出之熔渣Sx呈此程度的凝固狀態則並不會構成問題。 Further, in the embodiment shown in Fig. 8, when the cartridge 4a does not have a special internal cooling mechanism, the slag Sx extruded from the opening 5 is usually solidified by the lower surface and the both end faces of the side adjacent to the cooling drum 1, and The upper side is in a molten or semi-molten state, but does not pose a problem if the extruded slag Sx is in such a state of solidification.

圖9所示係本發明的熔化熔渣之冷卻處理裝置及冷卻處理方法另一實施形態示意正視圖。本實施形態的冷卻處理裝置亦在冷卻滾筒1上部設有堰4。 Fig. 9 is a front elevational view showing another embodiment of a cooling treatment apparatus and a cooling treatment method for molten slag according to the present invention. The cooling treatment apparatus of this embodiment is also provided with a crucible 4 on the upper portion of the cooling drum 1.

本實施形態中,在冷卻滾筒1上部所設置堰4,係由下部滾筒面具有朝反熔渣液滯留部A方向旋轉之旋轉方向的冷 卻滾筒4x所構成。 In the present embodiment, the crucible 4 is provided on the upper portion of the cooling drum 1, and the lower drum surface has a cold direction of rotation in the direction of the anti-slag liquid retention portion A. But the drum 4x is composed.

如同冷卻滾筒1,在上述冷卻滾筒4x內部設有具供冷媒流通用之流路的內部冷卻機構(未圖示),並在滾筒軸的各端部分別設置對該內部冷卻機構的冷媒供應部與冷媒排出部。另外,冷媒一般係使用水(冷卻水),但亦可使用其他流體(液體或氣體)。 Like the cooling drum 1, an internal cooling mechanism (not shown) having a flow path for supplying a refrigerant flow is provided inside the cooling drum 4x, and a refrigerant supply unit for the internal cooling mechanism is provided at each end portion of the drum shaft. With the refrigerant discharge section. In addition, the refrigerant generally uses water (cooling water), but other fluids (liquid or gas) may also be used.

如同圖8所示實施形態,開口5的寬度(厚度)較佳設定為5mm以上、更佳20mm以上。此外,最好藉由能調整冷卻滾筒4x的上下方向位置,而改變開口5的寬度(厚度)。 As in the embodiment shown in Fig. 8, the width (thickness) of the opening 5 is preferably set to 5 mm or more, more preferably 20 mm or more. Further, it is preferable to change the width (thickness) of the opening 5 by adjusting the position in the up and down direction of the cooling drum 4x.

再者,如同冷卻滾筒1,冷卻滾筒4x亦利用驅動裝置(未圖示)朝上述旋轉方向旋轉驅動。另外,冷卻滾筒1、與冷卻滾筒4x亦均最好能配合操業條件而控制旋轉數。另外,冷卻滾筒4x未必一定要位於冷卻滾筒1的正上方,亦可如本實施形態般在水平方向上偏移位置。 Further, like the cooling drum 1, the cooling drum 4x is also rotationally driven in the above-described rotational direction by a driving device (not shown). Further, it is preferable that both the cooling drum 1 and the cooling drum 4x can control the number of rotations in accordance with the operating conditions. Further, the cooling drum 4x does not necessarily have to be located directly above the cooling drum 1, and may be displaced in the horizontal direction as in the present embodiment.

另外,因為本實施形態的其餘構造均如同圖3所示實施形態,因而省略詳細說明。 In addition, since the rest of the structure of this embodiment is the embodiment shown in FIG. 3, detailed description is abbreviate|omitted.

使用如上述冷卻處理裝置的熔化熔渣之冷卻處理,熔化熔渣S係藉由在熔渣液滯留部A內滯留適當時間而冷卻後,依在冷卻滾筒1-冷卻滾筒4x之間被軋延的方式,從開口5一邊施行冷卻一邊擠出。此時,熔化熔渣因為承受:(i)在熔渣液滯留部A內滯留充分時間而冷卻,以及(ii)在開口5的進入側與冷卻滾筒1及冷卻滾筒4x進行長時間接觸後, 再於開口5內利用冷卻滾筒1與冷卻滾筒4x從二側施行軋延並冷卻;的冷卻作用,因而可更有效地促進熔化熔渣S的冷卻,可更安定地獲得厚板熔渣凝固體。 By using the cooling treatment of the molten slag of the above-described cooling treatment apparatus, the molten slag S is cooled by being retained in the slag liquid retention portion A for a suitable period of time, and then rolled between the cooling drum 1 and the cooling drum 4x. In the manner, it is extruded while cooling is performed from the opening 5. At this time, the molten slag is subjected to: (i) cooling for a sufficient time in the slag liquid retention portion A, and (ii) long-term contact with the cooling drum 1 and the cooling drum 4x on the entry side of the opening 5, Further, in the opening 5, the cooling roller 1 and the cooling drum 4x are used for rolling and cooling from both sides; the cooling effect is thereby more effectively promoted the cooling of the molten slag S, and the thick plate slag solidified body can be obtained more stably. .

另外,本實施形態的冷卻滾筒1、冷卻滾筒4x、以及圖8所示實施形態的冷卻滾筒1,係屬表面呈平滑的圓筒體,惟未必僅侷限於此,亦可設有溝等凹凸。若滾筒面100設有凹凸,則與熔化熔渣間的接觸面積增加,可促進熔渣的冷卻。此外,亦有凝固的熔渣容易破碎‧磨碎的優點。此外,關於透過冷媒的熱回收,亦因為比表面積較大,因而提高熱交換效率。 In addition, the cooling drum 1 and the cooling drum 4x of the embodiment and the cooling drum 1 of the embodiment shown in Fig. 8 have a smooth cylindrical surface, but are not limited thereto, and may have irregularities such as grooves. . When the drum surface 100 is provided with irregularities, the contact area with the molten slag increases, and the cooling of the slag can be promoted. In addition, there is also the advantage that the solidified slag is easily broken and ground. Further, regarding the heat recovery through the refrigerant, the heat exchange efficiency is also improved because the specific surface area is large.

再者,亦可利用在冷卻滾筒1的滾筒面100上所形成之環狀溝等凹凸,在冷卻滾筒1與冷卻滾筒4x的滾筒面間形成孔形狀開口5,熔渣便利用該孔形狀擠出。所以,從冷卻滾筒1與冷卻滾筒4x間的開口5所擠出之熔渣Sx的形狀,亦可為除板狀之外的線狀或柱狀等。此外,依照冷卻滾筒1或冷卻滾筒4x的滾筒面凹凸形狀,會有開口5呈間歇性形成,使熔渣Sx的擠出呈不連續的情況,此情況下,係從開口5將熔渣Sx實質上依塊形狀擠出。 Further, it is also possible to form a hole-shaped opening 5 between the cooling drum 1 and the drum surface of the cooling drum 4x by using irregularities such as an annular groove formed on the drum surface 100 of the cooling drum 1, and the slag is easily squeezed by the shape of the hole. Out. Therefore, the shape of the slag Sx extruded from the opening 5 between the cooling drum 1 and the cooling drum 4x may be a line shape or a column shape other than a plate shape. Further, depending on the uneven shape of the drum surface of the cooling drum 1 or the cooling drum 4x, the opening 5 may be formed intermittently, so that the extrusion of the slag Sx may be discontinuous. In this case, the slag Sx is taken from the opening 5. Substantially extruded in a block shape.

圖8與圖9所示實施形態中,從開口5擠出的熔渣Sx厚度,係定義為在圖8所示之冷卻滾筒徑方向上的熔渣最大厚度t。而所擠出之熔渣Sx的形狀係除板狀以外的情況,依照上述定義的熔渣Sx之厚度較佳為5mm以上、更佳20mm 以上。 In the embodiment shown in Figs. 8 and 9, the thickness of the slag Sx extruded from the opening 5 is defined as the maximum thickness t of the slag in the radial direction of the cooling drum shown in Fig. 8. The shape of the extruded slag Sx is other than a plate shape, and the thickness of the slag Sx according to the above definition is preferably 5 mm or more, more preferably 20 mm. the above.

圖8與圖9所示實施形態中,從開口5擠出的厚板熔渣Sx,通常僅單面或雙面表層凝固,而內部則呈熔融或半熔融狀態。而剛從開口5擠出後的凝固表層部,係利用冷卻滾筒進行急冷而成為玻璃質或接近其的組織,但爾後藉由內部未凝固熔渣的熱而回熱,變化為結晶質。所以,該等實施形態中,可獲得玻璃質較少的厚板熔渣凝固體。 In the embodiment shown in Fig. 8 and Fig. 9, the slag slag Sx extruded from the opening 5 is usually solidified only on one side or both sides, and the inside is in a molten or semi-molten state. The solidified surface layer portion which has just been extruded from the opening 5 is quenched by a cooling drum to form a vitreous or a structure close thereto, but is then heated back by the heat of the internal unsolidified slag to change to a crystalline form. Therefore, in these embodiments, a thick plate slag solidified body having less glass quality can be obtained.

圖10及圖11、圖12及圖13、圖14及圖15、圖16及圖17、圖18及圖19所示之各實施形態,係從冷卻滾筒1與冷卻滾筒4x間的開口5,將熔渣Sx依板狀以外的形狀進行擠出。具體而言,在冷卻滾筒1或/及冷卻滾筒4x的滾筒面(外周面)上形成下述(一)或/及(二):(一)滾筒圓周方向之環狀溝;(二)在滾筒圓周方向上相間隔設置的凹部;藉由使冷卻滾筒4x的滾筒面400抵接於冷卻滾筒1的滾筒面100,而利用上述(一)或/及(二)形成孔形狀開口5,並從該孔形狀開口5擠出熔渣Sx。 10 and 11, FIG. 12 and FIG. 13, FIG. 14 and FIG. 15, FIG. 16 and FIG. 17, FIG. 18 and FIG. 19 are the openings 5 between the cooling drum 1 and the cooling drum 4x. The slag Sx is extruded in a shape other than a plate shape. Specifically, the following (1) or/and (2) are formed on the drum surface (outer peripheral surface) of the cooling drum 1 or/and the cooling drum 4x: (1) an annular groove in the circumferential direction of the drum; (2) a recessed portion that is spaced apart in the circumferential direction of the drum; by abutting the drum surface 400 of the cooling drum 4x against the drum surface 100 of the cooling drum 1, the hole shape opening 5 is formed by the above (a) or/and (ii), and The slag Sx is extruded from the hole shape opening 5.

圖10與圖11所示之實施形態中,圖10所示係冷卻處理裝置及冷卻處理方法其中一部分的示意正視圖,圖11所示係側視圖。該實施形態中,在冷卻滾筒4x的滾筒面400(外周面)於滾筒長邊方向上相間隔地形成複數環狀溝401,藉由使冷卻滾筒4x的滾筒面400抵接於冷卻滾筒1的滾筒面 100,則形成利用上述環狀溝401形成孔形狀之開口5狀態。 In the embodiment shown in Fig. 10 and Fig. 11, Fig. 10 is a schematic front view showing a part of the cooling processing apparatus and the cooling processing method, and Fig. 11 is a side view. In the embodiment, the plurality of annular grooves 401 are formed at intervals in the longitudinal direction of the drum on the drum surface 400 (outer peripheral surface) of the cooling drum 4x, and the drum surface 400 of the cooling drum 4x is brought into contact with the cooling drum 1 Roller surface 100, a state in which the opening 5 of the hole shape is formed by the annular groove 401 is formed.

本實施形態的其餘構造均如同圖3、圖9所示實施形態,因而省略詳細說明。 The rest of the structure of the present embodiment is the same as that of the embodiment shown in Figs. 3 and 9, and therefore detailed description thereof will be omitted.

本實施形態中,係從由環狀溝401所形成之複數之孔形狀開口5擠出柱狀熔渣Sx。 In the present embodiment, the columnar slag Sx is extruded from a plurality of hole-shaped openings 5 formed by the annular groove 401.

另外,亦可不在冷卻滾筒4x的滾筒面400、而是在冷卻滾筒1的滾筒面100上於滾筒長邊方向上相間隔地形成複數環狀溝,藉由該環狀溝形成孔形狀之開口5。 Further, instead of the drum surface 400 of the cooling drum 4x, a plurality of annular grooves may be formed at intervals in the longitudinal direction of the drum on the drum surface 100 of the cooling drum 1, and the opening of the hole shape may be formed by the annular groove. 5.

圖12及圖13所示實施形態中,圖12所示係冷卻處理裝置及冷卻處理方法其中一部分的示意正視圖,圖13所示係側視圖。本實施形態中,在冷卻滾筒1的滾筒面100、與冷卻滾筒4x的滾筒面400上,分別於滾筒長邊方向上相間隔地形成複數環狀溝101與環狀溝401,藉由使冷卻滾筒4x的滾筒面400抵接於冷卻滾筒1的滾筒面100,使相對向的上述環狀溝101與環狀溝401相合而形成孔形狀開口5。另外,盛桶2之前端部係構成為與冷卻滾筒1的軸方向凹凸形狀(由複數環狀溝101所構成的凹凸形狀)相嚙合形狀,俾在與冷卻滾筒1間不會產生間隙、或儘可能縮小間隙。 In the embodiment shown in Fig. 12 and Fig. 13, Fig. 12 is a schematic front view showing a part of the cooling processing apparatus and the cooling processing method, and Fig. 13 is a side view. In the present embodiment, a plurality of annular grooves 101 and annular grooves 401 are formed on the drum surface 100 of the cooling drum 1 and the drum surface 400 of the cooling drum 4x at intervals in the longitudinal direction of the drum, and are cooled. The drum surface 400 of the drum 4x abuts against the drum surface 100 of the cooling drum 1, and the opposing annular groove 101 and the annular groove 401 are combined to form a hole-shaped opening 5. Further, the front end portion of the tub 2 is configured to be engaged with the axially concavo-convex shape of the cooling drum 1 (the uneven shape formed by the plurality of annular grooves 101), and the gap between the cooling drum 1 and the cooling drum 1 does not occur, or Reduce the gap as much as possible.

本實施形態中,係從環狀溝101與環狀溝401相合形成的複數之孔形狀開口5中擠出柱狀熔渣Sx。 In the present embodiment, the columnar slag Sx is extruded from a plurality of hole-shaped openings 5 formed by the annular groove 101 and the annular groove 401.

本實施形態的其餘構造均如同圖3、圖9所示實施形態,因而省略詳細說明。 The rest of the structure of the present embodiment is the same as that of the embodiment shown in Figs. 3 and 9, and therefore detailed description thereof will be omitted.

圖14與圖15所示實施形態中,圖14所示係冷卻處理裝置及冷卻處理方法其中一部分的示意正視圖,圖15所示係側視圖。本實施形態中,在冷卻滾筒4x的滾筒面400上,於滾筒長邊方向上相間隔地形成複數環狀溝402,且該等環狀溝402的底面在滾筒圓周方向上構成為凹凸狀(齒輪狀),藉由使冷卻滾筒4x的滾筒面400抵接於冷卻滾筒1的滾筒面100,而利用環狀溝402形成孔形狀之開口5。本實施形態中,利用環狀溝402底面的凹部而間歇性地加大開口5。 In the embodiment shown in Fig. 14 and Fig. 15, Fig. 14 is a schematic front view showing a part of the cooling processing apparatus and the cooling processing method, and Fig. 15 is a side view. In the present embodiment, a plurality of annular grooves 402 are formed on the drum surface 400 of the cooling drum 4x at intervals in the longitudinal direction of the drum, and the bottom surfaces of the annular grooves 402 are formed in a concave-convex shape in the circumferential direction of the drum ( In the gear shape, the annular surface 402 is formed by the annular groove 402 by abutting the drum surface 400 of the cooling drum 4x against the drum surface 100 of the cooling drum 1. In the present embodiment, the opening 5 is intermittently increased by the recessed portion on the bottom surface of the annular groove 402.

本實施形態中,係從由環狀溝402所形成之複數之孔形狀開口5中擠出熔渣Sx。該熔渣Sx係因為利用環狀溝402底面的凹部而將開口5呈間歇性地變大,因而依塊狀部b呈串珠狀連串的形狀擠出。此種形狀的熔渣Sx在從冷卻滾筒1剝離後,利用自重而分離為塊狀、或利用小外力即輕易地分離呈塊狀。 In the present embodiment, the slag Sx is extruded from a plurality of hole-shaped openings 5 formed by the annular groove 402. In the slag Sx, since the opening 5 is intermittently increased by the concave portion on the bottom surface of the annular groove 402, the block portion b is extruded in a beaded shape. The slag Sx having such a shape is separated into a block shape by its own weight after being peeled off from the cooling drum 1, or is easily separated into a block shape by a small external force.

本實施形態的其餘構造均如同圖3、圖9所示實施形態,因而省略詳細說明。 The rest of the structure of the present embodiment is the same as that of the embodiment shown in Figs. 3 and 9, and therefore detailed description thereof will be omitted.

另外,圖15中,省略在環狀溝402底面所形成的凹凸之圖示,而底面的凸部位置則利用假想線標示。 In addition, in Fig. 15, the illustration of the unevenness formed on the bottom surface of the annular groove 402 is omitted, and the position of the convex portion of the bottom surface is indicated by an imaginary line.

再者,亦可取代如圖14及圖15的實施形態之環狀溝402,改為在滾筒圓周方向上相間隔地形成溝狀或孔狀凹部,此情況,利用該凹部間歇性地形成開口5,並從該開口 5擠出塊狀熔渣Sx。 Further, instead of the annular groove 402 of the embodiment shown in Figs. 14 and 15, the groove or the hole-shaped recess may be formed at intervals in the circumferential direction of the drum. In this case, the opening is intermittently formed by the recess. 5, and from the opening 5 Extrusion of the massive slag Sx.

再者,亦可不在冷卻滾筒4x的滾筒面400上,而是在冷卻滾筒1的滾筒面100上於滾筒長邊方向上相間隔地形成複數之環狀溝(或如上述在滾筒圓周方向上相間隔地形成溝狀或孔狀之凹部),利用該環狀溝等形成孔形狀開口5。 Further, instead of the drum surface 400 of the cooling drum 4x, a plurality of annular grooves may be formed on the drum surface 100 of the cooling drum 1 at intervals in the longitudinal direction of the drum (or as described above in the circumferential direction of the drum) A groove-shaped or hole-shaped recess is formed at intervals, and a hole-shaped opening 5 is formed by the annular groove or the like.

圖16及圖17的實施形態中,圖16所示係冷卻處理裝置及冷卻處理方法其中一部分的示意正視圖,圖17係側視圖。本實施形態中,在冷卻滾筒1的滾筒面100、與冷卻滾筒4x的滾筒面400上,分別於滾筒長邊方向上相間隔地形成複數之環狀溝102與環狀溝403,且使該等環狀溝102與環狀溝403的底面在滾筒圓周方向上構成凹凸狀(齒輪狀),藉由使冷卻滾筒4x的滾筒面400抵接於冷卻滾筒1的滾筒面100,使相對向的上述環狀溝102與環狀溝403相合而形成孔形狀之開口5。本實施形態中,藉由使環狀溝102與環狀溝403的各底面凹部彼此相容,而使開口5間歇性放大。 In the embodiment of Fig. 16 and Fig. 17, Fig. 16 is a schematic front view showing a part of the cooling processing apparatus and the cooling processing method, and Fig. 17 is a side view. In the present embodiment, a plurality of annular grooves 102 and annular grooves 403 are formed on the drum surface 100 of the cooling drum 1 and the drum surface 400 of the cooling drum 4x so as to be spaced apart from each other in the longitudinal direction of the drum. The annular groove 102 and the bottom surface of the annular groove 403 are formed in a concave-convex shape (gear shape) in the circumferential direction of the drum, and the drum surface 400 of the cooling drum 4x is brought into contact with the drum surface 100 of the cooling drum 1 so as to face each other. The annular groove 102 is combined with the annular groove 403 to form a hole 5 having a hole shape. In the present embodiment, the opening 5 is intermittently enlarged by making the annular groove 102 and the bottom surface concave portions of the annular groove 403 compatible with each other.

另外,盛桶2前端部係構成為與冷卻滾筒1的軸方向之凹凸形狀(由複數之環狀溝102所形成的凹凸形狀)相嚙合形狀,俾在與冷卻滾筒1間不會產生間隙、或儘可能縮小間隙。 Further, the front end portion of the tub 2 is configured to be in a shape in which the concave and convex shape (the uneven shape formed by the plurality of annular grooves 102) in the axial direction of the cooling drum 1 is meshed, and no gap is formed between the cooling drum 1 and the cooling drum 1 Or narrow the gap as much as possible.

本實施形態的其餘構造均如同圖3、圖9所示實施形態,因而省略詳細說明。 The rest of the structure of the present embodiment is the same as that of the embodiment shown in Figs. 3 and 9, and therefore detailed description thereof will be omitted.

本實施形態中,係從由環狀溝102與環狀溝403相合形成 的複數之孔形狀開口5中擠出熔渣Sx。該熔渣Sx係藉由環狀溝102與環狀溝403的各底面之凹部彼此相合,而將開口5呈間歇性放大,因而使塊狀部b以串珠狀連接的形狀擠出。此種形狀的熔渣Sx在從冷卻滾筒1剝離後,利用自重而分離為塊狀、或依小外力即可輕易地分離為塊狀。 In the present embodiment, the annular groove 102 and the annular groove 403 are combined to form The slag Sx is extruded in the plurality of pore-shaped openings 5. The slag Sx is formed by the annular groove 102 and the concave portions of the respective bottom surfaces of the annular groove 403 being joined to each other, and the openings 5 are intermittently enlarged, so that the block portions b are extruded in a bead-like shape. The slag Sx having such a shape is separated into a block shape by its own weight after being peeled off from the cooling drum 1, or can be easily separated into a block shape by a small external force.

另外,圖16及圖17中,係省略在環狀溝102與環狀溝403的底面所形成之凹凸的圖示,但將底面的凸部位置依假想線標示。 In addition, in FIGS. 16 and 17, the unevenness formed on the bottom surface of the annular groove 102 and the annular groove 403 is omitted, but the position of the convex portion of the bottom surface is indicated by an imaginary line.

再者,亦可取代如本實施形態的環狀溝102與環狀溝403,改為在滾筒圓周方向上相間隔地形成溝狀或孔狀凹部,此情況,利用該凹部間歇性形成開口5,並從該開口5中擠出塊狀熔渣Sx。 Further, instead of the annular groove 102 and the annular groove 403 according to the present embodiment, a groove-shaped or hole-shaped recess may be formed at intervals in the circumferential direction of the drum. In this case, the opening 5 is intermittently formed by the recess. And extruding the slag slag Sx from the opening 5.

圖18及圖19的實施形態中,圖18所示係冷卻處理裝置及冷卻處理方法其中一部分的示意正視圖,圖19所示係側視圖。本實施形態中,在冷卻滾筒1的滾筒面100、與冷卻滾筒4x的滾筒面400,分別多數形成截面弧狀(半球狀)的凹部103與凹部404,藉由使冷卻滾筒4x的滾筒面400抵接於冷卻滾筒1的滾筒面100,則可使相對向的上述凹部103與凹部404相合而間歇性地形成開口5。 In the embodiment of Fig. 18 and Fig. 19, Fig. 18 is a schematic front view showing a part of the cooling processing apparatus and the cooling processing method, and Fig. 19 is a side view. In the present embodiment, a concave portion 103 and a concave portion 404 having a cross-sectional arc shape (hemispherical shape) are formed in the drum surface 100 of the cooling drum 1 and the drum surface 400 of the cooling drum 4x, respectively, and the drum surface 400 of the cooling drum 4x is formed. When the roller surface 100 of the cooling drum 1 is abutted, the opposing concave portion 103 and the concave portion 404 can be brought into contact with each other to form the opening 5 intermittently.

本實施形態的其餘構造均如同圖3、圖9所示實施形態,因而省略詳細說明。 The rest of the structure of the present embodiment is the same as that of the embodiment shown in Figs. 3 and 9, and therefore detailed description thereof will be omitted.

本實施形態中,係透過由凹部103與凹部404相合而間歇 性形成的複數開口5,擠出塊狀熔渣Sx。 In the present embodiment, the transmission is intermittent by the concave portion 103 and the concave portion 404. The plurality of openings 5 formed by the formation, extruding the massive slag Sx.

另外,在冷卻滾筒1與冷卻滾筒4x中,亦可使任一冷卻滾筒的滾筒面構成為平滑,而僅在另一冷卻滾筒的滾筒面形成凹部(凹部103或凹部404)。 Further, in the cooling drum 1 and the cooling drum 4x, the drum surface of any of the cooling drums may be configured to be smooth, and the concave portion (the recess 103 or the recess 404) may be formed only on the drum surface of the other cooling drum.

依如上述圖10~圖19的各實施形態所獲得之熔渣Sx,因為屬於下述任一情況:(a)將剛從開口5擠出後的熔渣Sx,利用簡易破碎手段等便可容易地加工為塊狀熔渣;(b)從開口5擠出後,利用自重即分離為塊狀、或依小外力即輕易地分離為塊狀;(c)從開口5依塊狀擠出;因而熔渣的塊狀化極為容易。所以,利用冷媒進行的熱回收中,因為熔渣比表面積較大,因而熱交換效率提高,可施行有效率的熱回收。此外,亦具有不需要或減少後續步驟中熔渣破碎‧磨碎處理程序之優點。 The slag Sx obtained in each of the above-described embodiments of FIGS. 10 to 19 may be any of the following cases: (a) the slag Sx which has just been extruded from the opening 5 can be easily crushed or the like. It is easily processed into a block slag; (b) after being extruded from the opening 5, it is separated into a block by its own weight, or is easily separated into a block shape by a small external force; (c) extruded from the opening 5 in a block shape Therefore, the slag of the slag is extremely easy. Therefore, in the heat recovery by the refrigerant, since the specific surface area of the slag is large, the heat exchange efficiency is improved, and efficient heat recovery can be performed. In addition, it also has the advantage of not requiring or reducing the slag breaking and grinding process in the subsequent steps.

將剛從開口5中擠出後的熔渣Sx加工為塊狀熔渣的方法,可利用碎礦機等破碎裝置施行破碎,亦可利用剪斷裝置施行剪斷。 The method of processing the slag Sx which has just been extruded from the opening 5 into a block slag can be crushed by a crushing device such as a crusher, or can be cut by a shearing device.

本發明的冷卻處理裝置,最好係熔化熔渣S在旋轉中的冷卻滾筒1之滾筒面100上呈層狀附著,在此狀態下,於冷卻滾筒1僅旋轉適當旋轉角度的期間即施行必要的冷卻。 In the cooling treatment apparatus of the present invention, it is preferable that the molten slag S adheres in a layer form on the drum surface 100 of the cooling drum 1 that is rotating, and in this state, it is necessary to perform the period in which the cooling drum 1 is rotated only by an appropriate rotation angle. Cooling.

再者,因為熔化熔渣S接觸到冷卻滾筒1,且冷卻至至少表面形成凝固層的程度,因而冷卻滾筒1的旋轉數較佳設為2~20rpm左右,更佳2~10rpm左右。此情況,冷卻滾筒1的 滾筒面周速係依冷卻滾筒1直徑而異,例如較佳設為0.1~2m/sec、更佳0.1~1m/sec左右。若冷卻滾筒1的旋轉速度超過上述範圍,熔化熔渣不易接觸/附著於滾筒面100上。甚至若滾筒面100的周速超過5m/sec,因從滾筒所承受的力,在為高爐熔渣等熔化熔渣的情況,會有發生破碎、細粒化而形成纖維狀的情形,因而不利於熔渣製品品質。反之,冷卻滾筒1的旋轉速度未滿上述範圍時,處理量會減少,不利於熔渣的大量處理。特別係如高爐熔渣等因急冷操作而容易非晶質化的熔渣時,在凝固層厚度變厚,半凝固部分呈消失或幾乎消失的狀態下,結束輥冷卻處理,因而幾乎不會發生輥通過後的回熱。所以,無法使在與輥相接觸的表層所產生非晶質層消失,導致吸濕性降低,作為表層非晶質相特徵的尖角狀態,不利於熔渣製品的品質。此外,當欲將無半凝固層的凝固狀態熔渣利用拉伸輥等施行軋延處理時,因為輥的凹凸中會有卡入熔渣的情況,因而最好避免。相關回收熔渣顯熱的情況,亦是對輥的散熱比例變大,因而由熱回收效率降低而言,最好避免(通常利用冷卻水施行的輥冷卻,冷卻水溫的上升大約設為5℃~10℃左右,因此較難從冷卻水進行熱回收)。 Further, since the molten slag S contacts the cooling drum 1 and is cooled to at least the surface to form a solidified layer, the number of rotations of the cooling drum 1 is preferably about 2 to 20 rpm, more preferably about 2 to 10 rpm. In this case, cooling the drum 1 The circumferential speed of the drum surface varies depending on the diameter of the cooling drum 1, and is preferably, for example, 0.1 to 2 m/sec, more preferably about 0.1 to 1 m/sec. If the rotational speed of the cooling drum 1 exceeds the above range, the molten slag is less likely to contact/attach to the drum surface 100. Even if the circumferential speed of the drum surface 100 exceeds 5 m/sec, when the slag is melted by blast furnace slag or the like due to the force received from the drum, it may be broken and finely granulated to form a fibrous shape, which is disadvantageous. The quality of slag products. On the other hand, when the rotation speed of the cooling drum 1 is less than the above range, the amount of treatment is reduced, which is disadvantageous for a large amount of processing of the slag. In particular, when the slag which is easily amorphized by the quenching operation, such as the blast furnace slag, the thickness of the solidified layer becomes thick, and the semi-solidified portion disappears or almost disappears, the roll cooling treatment is terminated, and thus the occurrence of the slag is hardly occurred. The heat is recovered after the roller passes. Therefore, the amorphous layer generated in the surface layer in contact with the roll cannot be eliminated, resulting in a decrease in hygroscopicity, and the sharp state of the surface amorphous phase characteristic is disadvantageous to the quality of the slag product. Further, when the solidified state slag having no semi-solidified layer is subjected to rolling treatment by a stretching roll or the like, it is preferable to avoid the occurrence of slag stuck in the unevenness of the roll. In the case of sensible heat recovery of the slag, the proportion of heat dissipation to the rolls is also increased. Therefore, it is preferable to avoid the reduction of the heat recovery efficiency (usually using the cooling of the cooling water, the temperature of the cooling water is set to about 5). °C ~ 10 °C or so, it is difficult to recover from cooling water).

圖26所示係本發明冷卻處理裝置的冷卻滾筒1之旋轉數與熔渣處理量間之關係一例。 Fig. 26 is a view showing an example of the relationship between the number of rotations of the cooling drum 1 and the amount of slag treatment in the cooling treatment apparatus of the present invention.

接著,針對上述各實施形態能共通適用的各種實施形態進 行說明。 Next, various embodiments that can be applied in common to the above embodiments are Line description.

為了對冷卻滾筒1施行冷卻,亦可取代在冷卻滾筒內設置如前述的內部冷卻機構,或者除了此種內部冷卻機構之外,設置朝冷卻滾筒1的下部滾筒面吹抵冷卻用流體的滾筒冷卻手段。該冷卻手段係例如可由朝冷卻滾筒1的下部滾筒面,吹抵水或空氣等冷卻用流體的噴嘴等所構成。 In order to cool the cooling drum 1, instead of providing an internal cooling mechanism as described above in the cooling drum, or in addition to such an internal cooling mechanism, a drum cooling for blowing the cooling fluid toward the lower drum surface of the cooling drum 1 may be provided. means. This cooling means can be constituted, for example, by a nozzle that blows a cooling fluid such as water or air toward the lower drum surface of the cooling drum 1.

再者,在具有冷卻滾筒4x的冷卻處理裝置中,亦可取代在冷卻滾筒4x內設置如前述內部冷卻機構、或除了該此種內部冷卻機構之外,設置朝冷卻滾筒4x的滾筒面吹抵冷卻用流體的滾筒冷卻手段。該冷卻手段亦可利用例如朝冷卻滾筒4x的滾筒面吹抵水或空氣等冷卻用流體的噴嘴等所構成。 Further, in the cooling treatment apparatus having the cooling drum 4x, instead of or in addition to the internal cooling mechanism in the cooling drum 4x, the drum surface facing the cooling drum 4x may be blown off. A drum cooling means for cooling fluid. The cooling means may be configured by, for example, a nozzle that blows a cooling fluid such as water or air toward the drum surface of the cooling drum 4x.

再者,亦可設置將從冷卻滾筒1剝離的熔渣Sx,如圖1所示,在冷卻滾筒1與搬送輸送帶8間、或在搬送輸送帶8上施行冷卻的冷卻手段7。該冷卻手段7係例如由對熔渣Sx吹抵水或空氣等冷卻用流體的噴嘴等所構成。 Further, a slag Sx that is peeled off from the cooling drum 1 may be provided, and as shown in FIG. 1, a cooling means 7 that performs cooling between the cooling drum 1 and the conveyance belt 8 or on the conveyance belt 8 may be provided. The cooling means 7 is constituted by, for example, a nozzle that blows the slag Sx against a cooling fluid such as water or air.

具有熔渣液滯留部A的冷卻處理裝置中,設有用於對熔渣液滯留部A內吹入流體用的流體供應手段,在例如(a)熔渣液滯留部A內的熔化熔渣溫度調整、(b)熔渣改質、(c)熔化熔渣的顯熱回收中之1個以上目的下,亦可從該流體供應手段對熔渣液滯留A內供應氣體等流體。另外,無關該等(a)~(c)目的,若對熔渣液滯留部A吹入氣體等流體並將熔 渣浴施行攪拌,便可促進熔渣的冷卻。 The cooling treatment device having the slag liquid retention portion A is provided with a fluid supply means for blowing a fluid into the slag liquid retention portion A, and for example, (a) the molten slag temperature in the slag liquid retention portion A For the purpose of adjusting, (b) slag upgrading, and (c) sensible heat recovery of the molten slag, a fluid such as a gas may be supplied to the slag liquid from the fluid supply means. In addition, irrespective of the purpose of (a) to (c), if a fluid such as a gas is blown into the slag liquid retention portion A and melted The slag bath is stirred to promote the cooling of the slag.

圖20所示係此情況的冷卻處理裝置及冷卻處理方法一實施形態示意正視圖。本實施形態中,在構成熔渣液滯留部A的盛桶2前端部分之底部處設置流體吹入手段6,從該流體吹入手段6朝熔渣液滯留部A內吹入流體。該流體吹入手段6係例如由氣體吹入噴嘴等所構成。 Fig. 20 is a front elevational view showing an embodiment of a cooling treatment device and a cooling treatment method in this case. In the present embodiment, the fluid blowing means 6 is provided at the bottom of the front end portion of the tub 2 constituting the slag liquid retention portion A, and the fluid is blown from the fluid blowing means 6 into the slag liquid retention portion A. This fluid blowing means 6 is constituted by, for example, a gas injection nozzle or the like.

本實施形態的其餘構造均如同圖3、圖9所示實施形態,因而省略詳細說明。 The rest of the structure of the present embodiment is the same as that of the embodiment shown in Figs. 3 and 9, and therefore detailed description thereof will be omitted.

對熔渣液滯留部A供應流體的方法,係除上述實施形態之外,尚可採用例如:在盛桶2的側壁200設置流體供應手段6,並從該流體供應手段6朝熔渣液滯留部A內供應流體的方法;以及從熔渣液滯留部A上方利用流體吹入手段6朝熔渣液滯留部A中吹入流體的方法等方法。 In the method of supplying the fluid to the slag liquid retention portion A, in addition to the above embodiment, for example, the fluid supply means 6 may be provided on the side wall 200 of the tub 2, and the liquid supply means 6 may be retained toward the slag liquid. A method of supplying a fluid in the portion A; and a method of blowing a fluid into the slag liquid retention portion A by the fluid blowing means 6 from above the slag liquid retention portion A.

對熔渣液滯留部A內供應的流體係有如:空氣、富氧化空氣、氧氣、氮氣、碳酸氣體、水蒸氣、天然瓦斯、都市煤氣、丙烷氣體、焦炭爐氣體、其他的製程氣體等,可使用該等之1種以上。 The flow system supplied to the slag liquid retention portion A is, for example, air, oxidizing air, oxygen, nitrogen, carbonic acid gas, water vapor, natural gas, city gas, propane gas, coke oven gas, other process gases, etc. One or more of these types are used.

上述(a)的熔化熔渣之溫度調整,通常利用流體供應而使熔化熔渣的溫度降低。流體係可使用例如:空氣、氮氣、水蒸氣等。 The temperature adjustment of the molten slag of the above (a) is usually such that the temperature of the molten slag is lowered by the supply of the fluid. The flow system can use, for example, air, nitrogen, water vapor, or the like.

相關上述(b)的熔渣改質,例如在以減少熔渣中的f-CaO量為目的時,可使用諸如空氣、富氧化空氣、氧氣等氧或含 氧氣體。若將此種氣體供應給熔化熔渣,則熔渣中的FeO被氧化,其與f-CaO鍵結而形成2CaO‧Fe2O3,因此熔渣中的f-CaO量降低,當將所獲得之熔渣凝固體使用於路床料等時,可抑制水合膨脹。 With respect to the slag upgrading of the above (b), for example, in order to reduce the amount of f-CaO in the slag, oxygen or an oxygen-containing gas such as air, oxidizing air, oxygen or the like can be used. If such a gas is supplied to the molten slag, FeO in the slag is oxidized, and it is bonded to f-CaO to form 2CaO‧Fe 2 O 3 , so the amount of f-CaO in the slag is lowered. When the obtained slag solidified body is used for a road bed material or the like, hydration expansion can be suppressed.

另一方面,當欲獲得內部氣孔比例較多的熔渣時,可對熔渣液滯留部A內供應空氣或氮氣,且調整操業條件(例如提高冷卻滾筒1與冷卻滾筒4x的旋轉速度),並將熔化熔渣S依含氣體的狀態從開口5擠出。藉此,所供應的氣體便被封鎖於熔渣中,可獲得內部氣孔比例較多的熔渣凝固體。因為此種熔渣的吸水性較高,因而特別適用於路床料等。 On the other hand, when it is desired to obtain a slag having a large internal pore ratio, air or nitrogen gas may be supplied to the slag liquid retention portion A, and the operating conditions (for example, increasing the rotational speed of the cooling drum 1 and the cooling drum 4x) may be adjusted. The molten slag S is extruded from the opening 5 in a gas-containing state. Thereby, the supplied gas is blocked in the slag, and a slag solidified body having a large internal pore ratio can be obtained. Since such slag has high water absorption, it is particularly suitable for use in road bed materials and the like.

上述(c)的熔化熔渣之顯熱回收,係回收如後述所供應的流體,並從該流體中執行熱回收。流體係可使用例如:空氣、氮氣、水蒸氣等。 The sensible heat recovery of the molten slag of the above (c) is to recover a fluid supplied as described later, and heat recovery is performed from the fluid. The flow system can use, for example, air, nitrogen, water vapor, or the like.

再者,藉由將水蒸氣(水)、與天然瓦斯或焦炭爐氣體等含烴系成分的氣體,同時供應給熔渣液滯留部A內,而產生水蒸氣改質反應,因為對該改質反應的吸熱供應熔渣的顯熱,因而可促進熔化熔渣的冷卻,且利用反應所生成的氣體(富氫氣體)可回收當作可燃性氣體、或熱回收。當含烴系成分氣體係使用例如甲烷氣體的情況,則發生CH4+H2O→CO+3H2的反應。 Further, by supplying water vapor (water) and a gas containing a hydrocarbon component such as natural gas or coke oven gas to the slag liquid retention portion A, a steam reforming reaction is generated, because the reform The endothermic heat of the mass reaction supplies the sensible heat of the slag, thereby promoting the cooling of the molten slag, and recovering the gas (hydrogen-rich gas) generated by the reaction as a combustible gas or heat recovery. When a hydrocarbon-based component gas system uses, for example, a methane gas, a reaction of CH 4 + H 2 O → CO + 3H 2 occurs.

另外,對熔渣液滯留A內的流體供應,亦可適用於未設置堰4之如圖3所示實施形態。 Further, the supply of the fluid in the slag liquid retention A can also be applied to the embodiment shown in Fig. 3 in which the crucible 4 is not provided.

再者,具有熔渣液滯留部A的冷卻處理裝置中,在(a)熔渣液滯留部A的熔化熔渣之溫度調整、(b)熔渣改質、(c)依熔渣的破碎或磨碎處理所產生之熔渣粉之再利用而提升製品良率中之1個以上之目的下,可在熔渣液滯留部A內的熔化熔渣中添加粉體。該粉體係有如:熔渣粉、矽砂、飛灰(煤灰)、磚屑、氧化鐵粉、煤塵、污泥、鐵礦粉等,可使用該等中之1種以上。 Further, in the cooling treatment apparatus having the slag liquid retention portion A, the temperature of the molten slag in (a) the slag liquid retention portion A is adjusted, (b) the slag is modified, and (c) the slag is broken. In the case where the slag powder produced by the pulverization treatment is reused to increase one or more of the product yields, the powder may be added to the molten slag in the slag liquid retention portion A. The powder system may be, for example, slag powder, strontium sand, fly ash (coal ash), brick scrap, iron oxide powder, coal dust, sludge, iron ore fine powder, etc., and one or more of these may be used.

上述(a)的熔化熔渣溫度調整,係利用粉體的添加而使熔化熔渣的溫度降低。藉由依此種粉體添加(特別係粉粒狀熔渣(熔渣粉)的添加)所進行的溫度調整,可期待如下效果。 The temperature adjustment of the molten slag of the above (a) is such that the temperature of the molten slag is lowered by the addition of the powder. The following effects can be expected by the temperature adjustment by the addition of such a powder (particularly, the addition of the powdery slag (slag powder)).

藉由對熔化熔渣,例如將粉粒狀熔渣依質量比1%~50%左右予以添加,可使熔渣溫度急遽下降而促進凝固。特別係當將熔渣厚度較大的製品熔渣急速冷卻至內部而欲獲得高品質熔渣製品時,則能有效地促進熔渣內部的冷卻‧凝固。若添加量超過50%,熔渣溫度會過度下降,而容易結塊,因而不僅冷卻速度的調整困難,形狀、厚度的調整亦困難。反之,若在添加量未滿1%的少量情況,熔渣溫度的調整實質上較為困難。此外,從經利用本發明冷卻處理裝置施行處理後的固體狀態熔渣進行顯熱回收時,因為熔渣量增加,可縮小固體熔渣的表面溫度與內部溫度差,因而能有效地進行熱回收。另外,因為促進熔化熔渣的冷卻‧凝固,因而可減輕冷卻滾筒1或拉伸輥3等的熱負荷‧熱疲勞。 By adding the molten slag, for example, the powdery slag by a mass ratio of about 1% to 50%, the slag temperature can be drastically lowered to promote solidification. In particular, when the product slag having a large slag thickness is rapidly cooled to the inside and a high-quality slag product is to be obtained, the cooling and solidification inside the slag can be effectively promoted. When the amount added exceeds 50%, the slag temperature is excessively lowered and it is easy to agglomerate, so that adjustment of the cooling rate is difficult, and adjustment of shape and thickness is also difficult. On the other hand, if the amount of addition is less than 1%, the adjustment of the slag temperature is substantially difficult. Further, when sensible heat recovery is performed from the solid state slag subjected to the treatment by the cooling treatment apparatus of the present invention, since the amount of slag is increased, the surface temperature of the solid slag can be reduced from the internal temperature difference, so that heat recovery can be efficiently performed. . Further, since the cooling and solidification of the molten slag is promoted, the heat load and thermal fatigue of the cooling drum 1 or the stretching rolls 3 and the like can be reduced.

上述(b)的熔渣改質,係藉由將例如矽砂、飛灰等SiO2源、高氧磚屑等Al2O3源、氧化鐵粉或鐵礦粉等氧化鐵源,添加於熔化熔渣,而使熔渣中的f-CaO量降低,俾可抑制將所獲得之熔渣凝固體使用於路床料等時的水合膨脹情形。 The slag modification of the above (b) is carried out by adding an iron oxide source such as an SiO 2 source such as cerium or fly ash, a source of Al 2 O 3 such as high-oxygen bricks, an iron oxide powder or an iron ore powder. The molten slag is melted to lower the amount of f-CaO in the slag, and the hydration expansion of the obtained slag solidified body when used for a road bed material or the like can be suppressed.

相關上述(c),若添加對依本發明法施行冷卻的熔渣施行破碎處理或/及磨碎處理時所產生的熔渣粉,便可提升製品良率。 In relation to the above (c), if the slag powder produced by the crushing treatment and/or the grinding treatment of the slag cooled by the method of the present invention is added, the product yield can be improved.

另外,對熔渣液滯留A內的熔化熔渣之粉體添加,亦可適用於未設有堰4的圖3所示實施形態。 Further, the addition of the powder of the molten slag in the slag liquid retention A can also be applied to the embodiment shown in Fig. 3 in which the crucible 4 is not provided.

在實施本發明之際,可將熔化熔渣的顯熱有效率地熱回收之事,從省能源、削減排出CO2的觀點而言,屬特別佳。該熔化熔渣的顯熱回收最好執行下述(i)~(iv)中至少1種、更佳2種以上、特佳全部的熱回收。 In the practice of the present invention, it is particularly preferable to efficiently recover the sensible heat of the molten slag from the viewpoint of energy saving and reduction of CO 2 emission. The sensible heat recovery of the molten slag is preferably carried out by heat recovery of at least one of the following (i) to (iv), more preferably two or more, and particularly preferably all.

(i)從通過冷卻滾筒1內部的冷媒進行熱回收。 (i) Heat recovery from the refrigerant passing through the inside of the cooling drum 1.

(ii)在使用具有堰4(包含冷卻滾筒4x的情況)的冷卻處理裝置施行熔化熔渣的冷卻處理中,從通過堰4內部的冷媒進行熱回收。 (ii) In the cooling treatment in which the molten slag is performed using the cooling treatment apparatus having the crucible 4 (in the case where the cooling drum 4x is included), heat is recovered from the refrigerant passing through the inside of the crucible 4.

(iii)使經冷卻滾筒1冷卻的熔渣,更進一步與冷媒(例如蒸氣、水、空氣等)相接觸而冷卻,並藉由回收該冷媒而進行熱回收。該方法中,基本係在封閉空間中使冷媒接觸到熔渣後,再將與熔渣進行熱交換過的冷媒回收。可採取例如:(a)將利用冷卻滾筒1冷卻過的熔渣,一邊利用搬送手段進 行搬送一邊與冷媒接觸,再從該冷媒中進行熱回收的方法;(b)將利用冷卻滾筒1冷卻過的熔渣,利用經供應冷媒的冷卻用容器或冷卻裝置施行冷卻,而從上述冷媒中進行熱回收的方法等各種方法。 (iii) The slag cooled by the cooling drum 1 is further cooled by contact with a refrigerant (for example, steam, water, air, etc.), and heat is recovered by recovering the refrigerant. In this method, after the refrigerant is brought into contact with the slag in the closed space, the refrigerant exchanged with the slag is recovered. For example, (a) the slag cooled by the cooling drum 1 is used, and the conveying means is used. (b) a method of performing heat recovery from the refrigerant while being transported, and (b) cooling the slag cooled by the cooling drum 1 by cooling the container or the cooling device supplied with the refrigerant, and cooling the refrigerant from the refrigerant Various methods such as a method of performing heat recovery.

(iv)在使用具有熔渣液滯留部A的冷卻處理裝置,施行熔化熔渣的冷卻處理中,於對熔渣液滯留部A內的熔化熔渣中吹入流體時,將所吹入的流體回收,並從該流體中進行熱回收。 (iv) In the cooling treatment for performing the molten slag by using the cooling treatment device having the slag liquid retention portion A, when the fluid is blown into the molten slag in the slag liquid retention portion A, the blown air The fluid is recovered and heat recovered from the fluid.

上述(i)、(ii)的形態中,從通過冷卻滾筒1或堰4(最好冷卻滾筒4x)的內部冷卻機構之冷媒中,進行熱回收。 In the above forms (i) and (ii), heat is recovered from the refrigerant passing through the internal cooling mechanism of the cooling drum 1 or the crucible 4 (preferably the cooling drum 4x).

上述(iii)的(a)形態中,係例如將上述所舉各實施形態的搬送輸送帶8利用隧道覆蓋,並藉由使該隧道內部流通冷媒而將熔渣冷卻,並從該冷媒中進行熱回收。 In the aspect (a) of the above (iii), for example, the conveyance belt 8 of each of the above-described embodiments is covered with a tunnel, and the slag is cooled by circulating a refrigerant inside the tunnel, and the slag is cooled from the refrigerant. Heat recovery.

上述(iii)的(b)形態中,係例如在經供應冷媒的冷卻用容器內收容熔渣並冷卻,而從上述冷媒中進行熱回收。冷卻用容器係例如可使用上述所舉各實施形態的熔渣桶9,並從通過此種冷卻用容器的冷媒中進行熱回收。此外,亦可在螺旋供料機或旋轉爐等冷卻裝置中裝入熔渣,並對該等內部供應空氣等冷媒而將熔渣冷卻,再從該冷媒中進行熱回收。 In the form (b) of the above (iii), for example, in the cooling container to which the refrigerant is supplied, the slag is stored and cooled, and heat is recovered from the refrigerant. For the cooling container, for example, the slag bucket 9 of each of the above-described embodiments can be used, and heat can be recovered from the refrigerant passing through the cooling container. Further, slag may be placed in a cooling device such as a screw feeder or a rotary kiln, and the slag may be cooled by supplying a refrigerant such as air inside, and heat may be recovered from the refrigerant.

上述(iv)的形態中,例如在冷卻滾筒1上方設置流體回收用之罩體等,並將已通過熔渣液滯留部A之熔化熔渣S的流體回收,再從該流體中進行熱回收。 In the embodiment (iv), for example, a cover for fluid recovery or the like is provided above the cooling drum 1, and the fluid having passed through the molten slag S of the slag retention unit A is recovered, and heat is recovered from the fluid. .

上述(i)~(iv)任一情況,係均在熱回收設備(未圖示)中從冷媒或氣體進行熱回收。所回收的熱可利用作為例如原料乾燥用熱源、燃料乾燥用蒸氣的熱源等各種熱源。 In any of the above (i) to (iv), heat recovery is performed from a refrigerant or a gas in a heat recovery facility (not shown). The heat to be recovered can be used as various heat sources such as a heat source for drying a raw material, a heat source for steam for fuel drying, and the like.

上述(iii)的(b)形態中,經冷卻用容器或冷卻裝置施行冷卻的熔渣,從顯熱回收的效率層面而言,粒徑最好縮小至某程度,從此點而言,最好經之前所舉例之圖10~圖19的實施形態施行冷卻處理過。 In the aspect (b) of the above (iii), the slag cooled by the cooling container or the cooling device is preferably reduced in size from a level of efficiency of sensible heat recovery, and from this point, it is preferable. The cooling treatment was carried out in the embodiment of Figs. 10 to 19 exemplified above.

圖21所示係相關上述(iii)形態的冷卻處理方法一實施形態的示意正視圖。本實施形態中,使用大致如同圖14及圖15的實施形態相同之冷卻處理裝置,並從該裝置中擠出塊狀熔渣Sx、或能輕易分離為塊狀的熔渣Sx,再將該熔渣Sx更進一步利用碎礦機等破碎裝置13施行破碎處理後,利用搬送輸送帶8裝入於密閉式冷卻用容器14中。裝入冷卻用容器14中的熔渣Sx之溫度,通常為700~1000℃。對冷卻用容器14中吹入作為冷媒的壓力空氣,而將熔渣Sx冷卻。經熔渣Sx的顯熱施行加熱過的空氣(熱風)被排出於冷卻用容器14外,並利用適當之熱交換手段進行熱回收。經冷卻至適當溫度的熔渣Sx從冷卻用容器14內被取出,並輸送給必要的處理步驟。 Fig. 21 is a schematic front view showing an embodiment of a cooling treatment method according to the above (iii) aspect. In the present embodiment, a cooling treatment device similar to that of the embodiment shown in Figs. 14 and 15 is used, and the slag slag Sx or the slag Sx which can be easily separated into a block shape is extruded from the device. The slag Sx is further subjected to a crushing treatment by a crushing device 13 such as a crusher, and then loaded into the sealed cooling container 14 by the transport conveyor 8 . The temperature of the slag Sx charged in the cooling container 14 is usually 700 to 1000 °C. The pressurized air as the refrigerant is blown into the cooling container 14, and the slag Sx is cooled. The heated air (hot air) heated by the sensible heat of the slag Sx is discharged outside the cooling container 14, and is heat-recovered by an appropriate heat exchange means. The slag Sx cooled to an appropriate temperature is taken out from the cooling container 14 and sent to a necessary processing step.

另外,因為其餘的裝置構造與冷卻處理形態,均如同圖3、圖9、圖14及圖15所示實施形態,因而省略詳細說明。 In addition, since the rest of the device structure and the cooling processing form are the same as those shown in FIGS. 3, 9, 14, and 15, the detailed description is omitted.

圖22所示係相關上述(iii)形態的冷卻處理方法中另一 實施形態的示意正視圖。在使用圖21所示之密閉式冷卻用容器14的情況,必需將熔渣與冷媒在容器內保持一定時間,當冷卻用容器14僅為1座時,在處理效率上會構成問題。針對此種問題,在圖22的實施形態中,藉由設置複數冷卻用容器14a~14c,並依序循環使用該等冷卻用容器14a~14c(熔渣裝入→熱回收→熔渣排出),則可執行有效率的處理。 Figure 22 is another example of the cooling treatment method related to the above (iii) aspect. A schematic front view of an embodiment. In the case of using the hermetic cooling container 14 shown in Fig. 21, it is necessary to keep the slag and the refrigerant in the container for a certain period of time. When the cooling container 14 is only one seat, there is a problem in processing efficiency. In the embodiment of Fig. 22, the plurality of cooling containers 14a to 14c are provided, and the cooling containers 14a to 14c are sequentially circulated (slag loading → heat recovery → slag discharge). , you can perform efficient processing.

另外,因為其餘的裝置構造與冷卻處理形態均如同圖21所示實施形態,因而省略詳細說明。 In addition, since the rest of the apparatus structure and the cooling processing form are the same as those shown in FIG. 21, detailed description is omitted.

圖23所示係關於上述(iii)形態的冷卻處理方法中另一實施形態的示意正視圖。本實施形態中,係在利用冷卻裝置的螺旋供料機15進行熔渣移送的情況下,對內部供應作為冷媒的壓力空氣而將熔渣冷卻。壓力空氣係從螺旋供料機15的出口側朝入口側供應。在螺旋供料機15內流通而將熔渣冷卻的空氣,係被取出於機外,並利用適當之熱交換手段進行熱回收。 Fig. 23 is a schematic front view showing another embodiment of the cooling treatment method of the above aspect (iii). In the present embodiment, when slag transfer is performed by the screw feeder 15 of the cooling device, the slag is cooled by supplying pressurized air as a refrigerant to the inside. The pressurized air is supplied from the outlet side of the screw feeder 15 toward the inlet side. The air that has flowed through the screw feeder 15 and cools the slag is taken out of the machine and heat-recovered by an appropriate heat exchange means.

另外,因為其餘的裝置構造與冷卻處理形態均如同圖21所示實施形態,因而省略詳細說明。 In addition, since the rest of the apparatus structure and the cooling processing form are the same as those shown in FIG. 21, detailed description is omitted.

圖24所示係關於上述(iii)形態的冷卻處理方法中另一實施形態的示意正視圖。本實施形態係使用大致如同圖4~圖6的實施形態相同的冷卻處理裝置,對於利用該裝置施行冷卻並排出的熔渣Sx(例如利用搬送輸送帶8搬送中的熔渣 Sx)、進而在滾筒面100上冷卻中的熔渣或拉伸輥3的輥面,從冷媒供應手段16供應(噴射)霧氣(水+壓縮空氣)等冷媒,而將該等施行冷卻。此外,本實施形態中,對冷卻滾筒1的下面亦從冷媒供應手段16a供應(噴射)霧氣(水+壓縮空氣)等冷媒,而將滾筒面100冷卻。冷媒係除了霧氣之外,尚可使用噴灑水等。 Fig. 24 is a schematic front view showing another embodiment of the cooling treatment method of the above aspect (iii). In the present embodiment, the slag Sx which is cooled and discharged by the apparatus (for example, the slag conveyed by the transport conveyor 8) is used in a cooling processing apparatus similar to that of the embodiment shown in FIG. 4 to FIG. Sx) Further, the slag which is cooled on the drum surface 100 or the roll surface of the stretching roll 3 is supplied (sprayed) with a refrigerant such as mist (water + compressed air) from the refrigerant supply means 16, and is cooled. Further, in the present embodiment, a refrigerant such as mist (water + compressed air) is supplied (sprayed) from the refrigerant supply means 16a to the lower surface of the cooling drum 1, and the drum surface 100 is cooled. In addition to the mist, the refrigerant can be sprayed with water or the like.

冷卻處理裝置與冷媒供應手段16、16a等在裝置出口側的設備係利用蓋體17覆蓋,且該蓋體17連接於排氣管18。在該排氣管18中設有熱交換器19。 The equipment on the outlet side of the apparatus, such as the cooling treatment device and the refrigerant supply means 16, 16a, is covered by the lid body 17, and the lid body 17 is connected to the exhaust pipe 18. A heat exchanger 19 is provided in the exhaust pipe 18.

另外,關於如高爐熔渣般之因急冷而容易非晶質化的熔渣,經滾筒冷卻後,在滾筒接觸部所形成之熔渣表層的非晶質相,係利用從熔渣內部的半凝固部分所供應的回熱,待非晶質相消失之後,藉由施行霧氣冷卻,可形成無非晶質相、且熔渣整體被適當冷卻的狀態。圖式中雖省略圖示,但藉由設置放射溫度計等,可掌握熔渣表面溫度,而調整利用霧冷卻等進行的冷卻速度,可獲得經抑制粉化性與膨脹性的高品質熔渣製品。 In addition, the slag which is easily amorphized by quenching as in the blast furnace slag is cooled by the drum, and the amorphous phase of the slag surface layer formed at the contact portion of the drum is used as a half from the inside of the slag. The reheating supplied from the solidified portion, after the disappearance of the amorphous phase, is cooled by the mist to form a state in which the amorphous phase is not formed and the entire slag is appropriately cooled. Although not shown in the drawings, by providing a radiation thermometer or the like, the surface temperature of the slag can be grasped, and the cooling rate by fog cooling or the like can be adjusted, and a high-quality slag product having suppressed powdering property and swelling property can be obtained. .

在蓋體17內利用冷媒與熔渣的接觸而產生之蒸氣與經加熱之氣體(以下稱「排氣氣體」),係通過排氣管18被回收,並利用熱交換器19而與熱媒進行熱交換,藉此回收熔渣顯熱。例如若使用水作為熱媒,藉由與排氣氣體間的熱交換則可獲得蒸氣。在排氣管18中設置氣體溫度計20,並測定排 氣氣體溫度。控制裝置21中,係根據利用該氣體溫度計20施行的排氣氣體溫度測定,並依成為所需之排氣氣體溫度的方式,控制著從冷媒供應手段16所供應的冷媒量(例如在冷媒為霧氣的情況則為霧量或氣水比,在噴灑水的情況則為水量等)等。 The vapor generated by the contact between the refrigerant and the slag in the lid body 17 and the heated gas (hereinafter referred to as "exhaust gas") are recovered by the exhaust pipe 18, and the heat medium 19 is used together with the heat medium. Heat exchange is performed to recover the sensible heat of the slag. For example, if water is used as the heat medium, steam can be obtained by heat exchange with the exhaust gas. A gas thermometer 20 is disposed in the exhaust pipe 18, and the row is measured Gas temperature. The control device 21 controls the amount of refrigerant supplied from the refrigerant supply means 16 in accordance with the exhaust gas temperature measurement by the gas thermometer 20 and the required exhaust gas temperature (for example, in the refrigerant) The case of fog is the amount of mist or the ratio of gas to water, and in the case of spraying water, the amount of water, etc.).

再者,通常,冷卻滾筒1係利用在冷媒流路中流通著冷卻水而予以冷卻,但可將從通過該冷卻滾筒1的冷卻水其中一部分、或冷卻水其中一部分所產生蒸氣,使用作為從冷媒供應手段16所供應之冷媒(蒸氣、水)的至少一部分,藉此可使熔渣的顯熱回收效率化。 In addition, in general, the cooling drum 1 is cooled by circulating cooling water in the refrigerant flow path, but steam may be used as a slave from a part of the cooling water passing through the cooling drum 1 or a part of the cooling water. At least a part of the refrigerant (vapor, water) supplied from the refrigerant supply means 16 can thereby improve the sensible heat recovery of the slag.

再者,亦可在排氣管18中未設置熱交換器19,而是直接將排氣氣體使用作為其中任一熱源。經冷卻至適當溫度的熔渣Sx,被輸送給必要的處理步驟,而成為製品熔渣。此時,雖產生熔渣粉(微粉狀熔渣),亦可將該熔渣粉,如前述添加於熔渣液滯留A的熔化熔渣中,而施行熔化熔渣的溫度調整。圖中的22係指用於進行此種步驟的熔渣粉供應裝置。 Further, the heat exchanger 19 may not be provided in the exhaust pipe 18, but the exhaust gas may be directly used as any one of the heat sources. The slag Sx cooled to an appropriate temperature is supplied to the necessary processing steps to become a product slag. At this time, although slag powder (micronized slag) is generated, the slag powder may be added to the molten slag in which the slag liquid is retained in A, and the temperature of the molten slag may be adjusted. 22 in the figure refers to a slag powder supply device for performing such a step.

另外,因為其餘的裝置構造與冷卻處理形態均如同圖3、圖4~圖6所示實施形態,因而省略詳細說明。 In addition, since the rest of the apparatus structure and the cooling processing form are the same as those of the embodiment shown in FIG. 3 and FIG. 4 to FIG. 6, detailed description is omitted.

在上述圖20~圖24的實施形態中,冷卻處理裝置亦可使用圖1~圖19中任一實施形態者。 In the embodiment of Figs. 20 to 24 described above, the cooling processing apparatus may use any of the embodiments of Figs. 1 to 19 .

上述(iv)形態的冷卻處理方法,係例如將熔渣液滯留部A的上方空間利用氣體回收用罩體覆蓋,且該罩體連接於氣體 排出管,將從熔渣液滯留部A上升的氣體,利用罩體與氣體排出管輸送給適當氣體回收系統。另外,本實施形態中,係在如前述將水蒸氣(水)、與天然瓦斯或焦炭爐氣體等含烴系成分氣體同時供應給熔渣液滯留A內的情況特別適用。 In the cooling treatment method of the above (iv), for example, the upper space of the slag liquid retention portion A is covered with a gas recovery cover, and the cover is connected to the gas. The discharge pipe transports the gas rising from the slag liquid retention portion A to the appropriate gas recovery system by the cover and the gas discharge pipe. In addition, in the present embodiment, water vapor (water) and a hydrocarbon-containing component gas such as natural gas or coke oven gas are supplied to the slag liquid retention A at the same time as described above.

另外,當實施具有堰4的實施形態時,在開始操作的時點,因為熔渣液滯留部A尚未形成,因而首先必需供應熔化熔渣S,而形成熔渣液滯留部A。所以,例如圖8、圖9等實施形態,在下部冷卻滾筒1與上部堰4(圖9中的冷卻滾筒4x)間隔(開口5寬度)呈狹窄狀態或封閉狀態下,開始進行操作。此時,為了容易生成熔渣液滯留A,亦可施行減少冷卻滾筒1的旋轉數等操作。 Further, when the embodiment having the crucible 4 is carried out, since the slag liquid retention portion A is not yet formed at the time of starting the operation, it is first necessary to supply the molten slag S to form the slag liquid retention portion A. Therefore, for example, in the embodiment of Fig. 8 and Fig. 9, the operation is started when the lower cooling drum 1 and the upper crucible 4 (the cooling drum 4x in Fig. 9) are spaced apart (the width of the opening 5) in a narrow state or in a closed state. At this time, in order to easily generate the slag liquid retention A, operations such as reducing the number of rotations of the cooling drum 1 may be performed.

在形成既定熔渣液滯留A後,藉由將上述間隔(開口5寬度)調整為既定距離,可安定地獲得厚度較厚之熔渣Sx。 After the predetermined slag liquid retention A is formed, by adjusting the above-described interval (opening 5 width) to a predetermined distance, the thick slag Sx can be stably obtained.

相對於此,例如圖10~圖13的實施形態,因為無法使開口5變狹窄或封閉,因而在操作初期便藉由調整對冷卻處理裝置的熔化熔渣S供應量(即,供應較從開口5中擠出量更多量的熔化熔渣S),則可迅速形成熔渣液滯留部A。 On the other hand, for example, in the embodiment of FIGS. 10 to 13 , since the opening 5 cannot be narrowed or closed, the supply amount of the molten slag S to the cooling treatment device is adjusted at the initial stage of operation (ie, the supply is relatively open). When a larger amount of molten slag S) is extruded in 5, the slag liquid retention portion A can be quickly formed.

再者,若有設置熔渣液滯留A的液面高度檢測手段,當熔化熔渣承接量發生變化時,藉由以使熔渣液滯留A的液面高度控制為一定的方式變更冷卻滾筒1的旋轉數,則可安定地獲得一定厚度的熔渣Sx。 In addition, when there is a liquid level detecting means for setting the slag liquid retention A, when the molten slag receiving amount is changed, the cooling drum 1 is changed so that the liquid level of the slag liquid retention A is kept constant. The number of rotations can stably obtain a certain thickness of slag Sx.

通常,圖4~圖6等冷卻處理裝置所具備的拉伸輥3亦具 有內部冷卻機構。圖25所示係內部冷卻機構一實施形態的示意剖視圖。拉伸輥3係內部設有冷媒流路30,且沿輥軸31a、31b的軸方向設有冷媒通路40a、40b。 Generally, the stretching rolls 3 provided in the cooling treatment apparatus such as FIG. 4 to FIG. 6 also have There is an internal cooling mechanism. Fig. 25 is a schematic cross-sectional view showing an embodiment of an internal cooling mechanism. The drawing roller 3 is provided with a refrigerant flow path 30 therein, and refrigerant passages 40a and 40b are provided along the axial direction of the roller shafts 31a and 31b.

本實施形態中,係作僅將拉伸輥3內部形成中空,並將該中空部作為冷媒流路30,且該冷媒流路30二端連接著上述冷媒通路31a、31b的構造。作成此種構造之理由如下。熔渣冷卻處理裝置並不適於經由冷媒施行熔渣顯熱的回收,此時的熔渣冷卻‧熱回收形態之一,可考慮利用在冷媒流路中流通的冷卻水之蒸發潛熱將熔渣冷卻,並從冷媒流路回收該蒸氣。其中,因為拉伸輥3僅有其下部會接觸到熔化熔渣而經常被加熱,因此如本實施形態,將輥內部形成中空而構成冷媒流路30的情況,內部冷卻水被加熱而沸騰,並產生熱水對流。所以,從冷媒通路31a導入至冷媒流路30內的冷卻水,並非馬上從冷媒通路31b流出,而是利用如上述的熱水對流適當地滯留於冷媒流路30內,而發揮作為冷媒之機能,利用該蒸發潛熱則可依較少冷卻水量獲得高冷卻效果。另一方面,在冷媒流路30內所產生的蒸氣,係在從冷媒流路30中排出之後,可於冷媒循環路途中輕易地施行分離‧回收。 In the present embodiment, only the inside of the stretching roll 3 is formed to be hollow, and the hollow portion is used as the refrigerant flow path 30, and the refrigerant passages 30 are connected to the refrigerant passages 31a and 31b at both ends. The reason for this configuration is as follows. The slag cooling treatment device is not suitable for the recovery of the sensible heat of the slag via the refrigerant. In this case, one of the slag cooling and the heat recovery mode, the slag cooling can be considered by utilizing the latent heat of evaporation of the cooling water flowing through the refrigerant flow path. And recover the vapor from the refrigerant flow path. In the present embodiment, the inside of the roll is formed such that the inside of the roll is hollow to form the refrigerant flow path 30, and the internal cooling water is heated and boiled. And produce hot water convection. Therefore, the cooling water introduced into the refrigerant flow path 30 from the refrigerant passage 31a does not immediately flow out of the refrigerant passage 31b, but is appropriately retained in the refrigerant flow passage 30 by the above-described hot water convection, and functions as a refrigerant. By using this latent heat of vaporization, a high cooling effect can be obtained with less cooling water. On the other hand, the vapor generated in the refrigerant flow path 30 can be easily separated and collected in the refrigerant circulation path after being discharged from the refrigerant flow path 30.

本發明之熔渣製品之製造方法,係利用本發明的冷卻處理方法施行冷卻,並將已凝固熔渣施行破碎處理或/及磨碎處理,視需要利用篩分等施行整粒,可獲得粒狀熔渣製品。本 發明係可輕易製得粒徑5mm以上的熔渣製品,特別亦可輕易地製得粒徑20~30mm程度的熔渣製品。該熔渣製品的種類並無限制,通常可成為路床料、粗骨材、細骨材、海洋土木材料等土木材料‧建築材料的熔渣製品,特別適用於路床料、粗骨材。 The method for producing a slag product according to the present invention is cooled by the cooling treatment method of the present invention, and the solidified slag is subjected to crushing treatment and/or grinding treatment, and if necessary, sieving or the like is carried out by using the granules to obtain granules. Slag products. this In the invention, a slag product having a particle diameter of 5 mm or more can be easily produced, and in particular, a slag product having a particle diameter of 20 to 30 mm can be easily produced. The type of the slag product is not limited, and can generally be used as a slag product for road bed materials, coarse aggregates, fine aggregates, marine civil materials, and the like, and is particularly suitable for road bed materials and coarse aggregates.

依本發明所獲得的熔渣製品,因為利用急冷進行製造,因而抑制粉化,所以可減少微粉部分,當利用作為海洋土木材之際,不使海水白濁。此外,因為急冷凝固成接近目標粒度的層狀,因而可將破碎步驟簡略化,可形成微粒分較少的粗骨材、細骨材。此外,因為形成緻密質,因而吸水率低,亦可成為能利用於瀝青用的硬質物。此外,藉由施行熔渣改質,可減少自由CaO,因而老化亦容易進行,即使未使用蒸氣老化,而利用大氣老化仍可抑制膨脹,因而亦可利用作為路床料。 Since the slag product obtained by the present invention is produced by quenching, the pulverization is suppressed, so that the fine powder portion can be reduced, and when it is used as the marine soil, the seawater is not clouded. Further, since the solidification is rapidly cooled to a layer shape close to the target particle size, the crushing step can be simplified, and coarse aggregates and fine aggregates having less fine particles can be formed. Further, since the dense material is formed, the water absorption rate is low, and it can be used as a hard material for the asphalt. Further, by performing slag upgrading, free CaO can be reduced, and aging can be easily performed. Even if vapor aging is not used, expansion can be suppressed by atmospheric aging, and thus it can be utilized as a road bed material.

(產業上之可利用性) (industrial availability)

根據本發明熔化熔渣之冷卻處理裝置及冷卻處理方法,因為從單一橫式冷卻滾筒(1)的滾筒面(100)所剝離之經冷卻處理完之熔渣朝一方向被排出,因而冷卻處理完之熔渣的處置‧後處理等均較容易,亦可降低設備成本。特別係當施行處理完之熔渣的顯熱回收時,若如習知雙滾筒式熔渣冷卻處理裝置般欲將朝正反二方向排出的冷卻處理完之熔渣利用1個熱回收設備施行處理,則在將相反方向2路徑整合為1 個的過程中,熔渣溫度降低,而無法施行有效率的熱回收,相對於此,本發明因為冷卻處理完之熔渣係朝一方向被排出,因而能有效率地施行熱回收。 According to the cooling treatment device and the cooling treatment method of the molten slag according to the present invention, since the cooled slag which is peeled off from the drum surface (100) of the single horizontal cooling drum (1) is discharged in one direction, the cooling process is completed. Disposal of slag, post-treatment, etc. are relatively easy, and equipment costs can also be reduced. In particular, when the sensible heat recovery of the treated slag is performed, if the conventional double drum type slag cooling treatment device is used, the cooled slag discharged in the forward and reverse directions is to be subjected to one heat recovery device. Processing, in the opposite direction 2 paths are integrated into 1 In the process, the slag temperature is lowered, and efficient heat recovery cannot be performed. On the other hand, in the present invention, since the slag which is cooled and processed is discharged in one direction, heat recovery can be efficiently performed.

再者,因為對橫式冷卻滾筒(1)中經由盛桶(2)灌注熔化熔渣,因此不會對橫式冷卻滾筒(1)施加熔化熔渣的落下荷重,或可充分減輕落下荷重,因而尤其即使是大型處理裝置,亦可在未使用澆口盤的情況下,大量地處理熔化熔渣。此外,藉由選擇盛桶形狀,可使熔化熔渣朝滾筒寬度方向擴展,俾可使熔化熔渣在滾筒面(100)上均勻地冷卻。 Further, since the molten slag is poured into the horizontal cooling drum (1) via the tub (2), the falling load of the molten slag is not applied to the horizontal cooling drum (1), or the falling load can be sufficiently reduced. Therefore, even in the case of a large-scale processing apparatus, the molten slag can be processed in a large amount without using a tundish. Further, by selecting the shape of the tub, the molten slag can be expanded toward the width direction of the drum, and the molten slag can be uniformly cooled on the drum surface (100).

再者,根據使用由盛桶(2)與滾筒面(100)形成熔渣液滯留部(A)的冷卻處理裝置、及使用該裝置的熔化熔渣之冷卻處理方法,可有效地促進熔化熔渣的冷卻,因而即使黏度較小的熔化熔渣,仍可確保附著於滾筒面(100)上的熔渣厚度,俾可獲得厚板熔渣凝固體。 Further, according to the cooling treatment device using the slag liquid retention portion (A) formed by the tub (2) and the drum surface (100), and the cooling treatment method using the molten slag using the device, the fusion melting can be effectively promoted. The slag is cooled, so that even if the slag has a small viscosity, the thickness of the slag adhering to the drum surface (100) can be ensured, and the slag solidified body can be obtained.

再者,根據具有拉伸輥(3)的冷卻處理裝置、及使用該裝置的熔化熔渣之冷卻處理方法,因為拉伸輥(3)將滾筒面(100)上所附著之熔化熔渣施行軋延,並在滾筒寬度方向上拉伸,因而對鹼度較高且具黏性的熔化熔渣能依高冷卻效率施行冷卻,可依高生產性獲得熔渣凝固體。此外,因為可將熔化熔渣依高冷卻速度施行冷卻,因而尤其是針對鹼度較高的熔渣,亦可獲得不易粉化的熔渣凝固體。 Further, according to the cooling treatment device having the stretching roller (3) and the cooling treatment method using the molten slag using the device, the stretching roller (3) performs the molten slag attached to the drum surface (100). Rolling and stretching in the width direction of the drum, so that the molten slag having a high alkalinity and viscosity can be cooled by high cooling efficiency, and the slag solidified body can be obtained with high productivity. Further, since the molten slag can be cooled at a high cooling rate, a slag solidified body which is not easily pulverized can be obtained especially for the slag having a high alkalinity.

再者,根據具有堰(4)的冷卻處理裝置、及使用該裝置的 熔化熔渣之冷卻處理方法,因為利用堰(4)、滾筒面(100)及盛桶(2)可形成較大的熔渣液滯留部(A),並可延長在熔渣液滯留部(A)中的熔化熔渣滯留時間,因而能特別有效地促進熔化熔渣的冷卻,可將經適當冷卻的熔渣從開口(5)擠出。所以,藉由充分加大開口(5)的寬度(所擠出熔渣的厚度),可獲得厚板之熔渣凝固體。 Furthermore, according to the cooling treatment device having the crucible (4), and the use of the same The cooling treatment method of the molten slag can form a large slag liquid retention portion (A) by using the crucible (4), the drum surface (100), and the barrel (2), and can be extended in the slag liquid retention portion ( The molten slag retention time in A) is thus particularly effective in promoting the cooling of the molten slag, and the appropriately cooled slag can be extruded from the opening (5). Therefore, by sufficiently increasing the width of the opening (5) (thickness of the extruded slag), a slag solidified body of a thick plate can be obtained.

再者,藉由使堰(4)為由下部外周面朝反熔渣液滯留部(A)方向旋轉之旋轉方向的冷卻滾筒(4x)所構成,可更有效地促進熔化熔渣的冷卻,俾可更安定地獲得厚板熔渣凝固體。 Further, by forming the crucible (4) as a cooling drum (4x) having a rotation direction in which the lower outer peripheral surface is rotated in the direction of the anti-slag liquid retention portion (A), the cooling of the molten slag can be more effectively promoted.俾 The solidified slag solidified body can be obtained more stably.

再者,根據本發明的熔渣製品之製造方法,藉由使用如上述冷卻處理方法,可低成本且安定地製造具有所需粒度的熔渣製品。 Further, according to the method for producing a slag product of the present invention, by using the above-described cooling treatment method, a slag product having a desired particle size can be produced at low cost and stably.

1‧‧‧橫式冷卻滾筒 1‧‧‧Horizontal cooling drum

1、4x‧‧‧冷卻滾筒 1, 4x‧‧‧ Cooling roller

2‧‧‧盛桶 2‧‧‧ barrel

3、3x、3y、3z‧‧‧拉伸輥 3, 3x, 3y, 3z‧‧‧ stretching rolls

4‧‧‧堰 4‧‧‧堰

4a‧‧‧堰體 4a‧‧‧ body

5‧‧‧開口 5‧‧‧ openings

6‧‧‧流體供應手段、流體吹入手段 6‧‧‧Fluid supply means, fluid blowing means

7‧‧‧冷卻手段 7‧‧‧cooling means

8‧‧‧搬送輸送帶 8‧‧‧Transport conveyor belt

9‧‧‧熔渣桶 9‧‧‧ slag bucket

10‧‧‧氣體噴射手段 10‧‧‧ gas injection means

11‧‧‧支撐臂 11‧‧‧Support arm

13‧‧‧破碎裝置 13‧‧‧Crushing device

14、14a、14b、14c‧‧‧冷卻用容器 14, 14a, 14b, 14c‧‧‧cooling containers

15‧‧‧螺旋供料機 15‧‧‧Spiral feeder

16、16a‧‧‧冷媒供應手段 16, 16a‧‧‧ refrigerant supply means

17‧‧‧蓋體 17‧‧‧ Cover

18‧‧‧排氣管 18‧‧‧Exhaust pipe

19‧‧‧熱交換器 19‧‧‧ heat exchanger

20‧‧‧氣體溫度計 20‧‧‧ gas thermometer

21‧‧‧控制裝置 21‧‧‧Control device

22‧‧‧(熔渣粉)供應裝置 22‧‧‧(slag powder) supply device

30‧‧‧冷媒流路 30‧‧‧Refrigerant flow path

31a、31b‧‧‧輥軸 31a, 31b‧‧‧ Roller

40a、40b‧‧‧冷媒通路 40a, 40b‧‧‧ refrigerant passage

100、400‧‧‧滾筒面 100,400‧‧‧ Roller surface

101、102‧‧‧環狀溝 101, 102‧‧ ‧ annular groove

103、404‧‧‧凹部 103, 404‧‧‧ recess

110‧‧‧軸承孔 110‧‧‧ bearing hole

200‧‧‧側壁 200‧‧‧ side wall

300‧‧‧外周面 300‧‧‧ outer perimeter

301‧‧‧輥軸 301‧‧‧ Roller

401、402、403‧‧‧環狀溝 401, 402, 403‧‧ ‧ annular groove

A‧‧‧熔渣液滯留部 A‧‧‧ slag liquid retention

S‧‧‧熔化熔渣 S‧‧‧melting slag

Sx‧‧‧熔渣 Sx‧‧‧ slag

t‧‧‧間隔 T‧‧‧ interval

圖1為本發明的熔化熔渣之冷卻處理裝置及冷卻處理方法一實施形態的示意正視圖。 Fig. 1 is a schematic front view showing an embodiment of a cooling treatment device and a cooling treatment method for molten slag according to the present invention.

圖2為本發明的熔化熔渣之冷卻處理裝置及冷卻處理方法另一實施形態的示意正視圖。 Fig. 2 is a schematic front elevational view showing another embodiment of a cooling treatment apparatus and a cooling treatment method for molten slag according to the present invention.

圖3為本發明的熔化熔渣之冷卻處理裝置及冷卻處理方法另一實施形態的示意正視圖。 Fig. 3 is a schematic front elevational view showing another embodiment of a cooling treatment apparatus and a cooling treatment method for molten slag according to the present invention.

圖4為本發明的熔化熔渣之冷卻處理裝置及冷卻處理方法另一實施形態的示意正視圖。 Fig. 4 is a schematic front elevational view showing another embodiment of a cooling treatment apparatus and a cooling treatment method for molten slag according to the present invention.

圖5為圖4所示實施形態之平面圖。 Figure 5 is a plan view of the embodiment shown in Figure 4.

圖6為圖4所示實施形態之附設冷卻滾筒的拉伸輥之作用說明圖。 Fig. 6 is an explanatory view of the action of a stretching roll provided with a cooling drum in the embodiment shown in Fig. 4.

圖7為本發明的熔化熔渣之冷卻處理裝置及冷卻處理方法另一實施形態的示意平面圖。 Fig. 7 is a schematic plan view showing another embodiment of a cooling treatment apparatus and a cooling treatment method for molten slag according to the present invention.

圖8為本發明的熔化熔渣之冷卻處理裝置及冷卻處理方法另一實施形態的示意正視圖。 Fig. 8 is a schematic front elevational view showing another embodiment of a cooling treatment apparatus and a cooling treatment method for molten slag according to the present invention.

圖9為本發明的熔化熔渣之冷卻處理裝置及冷卻處理方法另一實施形態的示意正視圖。 Fig. 9 is a schematic front elevational view showing another embodiment of a cooling treatment apparatus and a cooling treatment method for molten slag according to the present invention.

圖10為本發明的熔化熔渣之冷卻處理裝置及冷卻處理方法另一實施形態其中一部分的示意正視圖。 Fig. 10 is a schematic front elevational view showing a part of another embodiment of a cooling treatment device and a cooling treatment method for molten slag according to the present invention.

圖11為圖10所示實施形態其中一部分的示意側視圖。 Figure 11 is a schematic side elevational view of a portion of the embodiment of Figure 10.

圖12為本發明的熔化熔渣之冷卻處理裝置及冷卻處理方法另一實施形態其中一部分的示意正視圖。 Fig. 12 is a schematic front elevational view showing a part of another embodiment of a cooling treatment device and a cooling treatment method for molten slag according to the present invention.

圖13為圖12所示實施形態其中一部分的示意側視圖。 Figure 13 is a schematic side elevational view of a portion of the embodiment of Figure 12;

圖14為本發明的熔化熔渣之冷卻處理裝置及冷卻處理方法另一實施形態其中一部分的示意正視圖。 Fig. 14 is a schematic front elevational view showing a part of another embodiment of a cooling treatment apparatus and a cooling treatment method for molten slag according to the present invention.

圖15為圖14所示實施形態其中一部分的示意側視圖。 Figure 15 is a schematic side elevational view of a portion of the embodiment of Figure 14.

圖16為本發明的熔化熔渣之冷卻處理裝置及冷卻處理方法另一實施形態其中一部分的示意正視圖。 Fig. 16 is a schematic front view showing a part of another embodiment of a cooling treatment apparatus and a cooling treatment method for molten slag according to the present invention.

圖17為圖16所示實施形態其中一部分的示意側視圖。 Figure 17 is a schematic side elevational view of a portion of the embodiment of Figure 16;

圖18為本發明的熔化熔渣之冷卻處理裝置及冷卻處理方法另一實施形態其中一部分的示意正視圖。 Fig. 18 is a schematic front view showing a part of another embodiment of a cooling treatment device and a cooling treatment method for molten slag according to the present invention.

圖19為圖18所示實施形態其中一部分的示意側視圖。 Figure 19 is a schematic side elevational view of a portion of the embodiment of Figure 18.

圖20為本發明的熔化熔渣之冷卻處理裝置及冷卻處理方法另一實施形態的示意正視圖。 Fig. 20 is a schematic front elevational view showing another embodiment of a cooling treatment apparatus and a cooling treatment method for molten slag according to the present invention.

圖21為本發明的熔化熔渣之冷卻處理裝置及冷卻處理方法另一實施形態的示意正視圖。 Fig. 21 is a schematic front elevational view showing another embodiment of a cooling treatment apparatus and a cooling treatment method for molten slag according to the present invention.

圖22為本發明的熔化熔渣之冷卻處理裝置及冷卻處理方法另一實施形態的示意正視圖。 Fig. 22 is a schematic front elevational view showing another embodiment of a cooling treatment apparatus and a cooling treatment method for molten slag according to the present invention.

圖23為本發明的熔化熔渣之冷卻處理裝置及冷卻處理方法另一實施形態的示意正視圖。 Fig. 23 is a schematic front elevational view showing another embodiment of a cooling treatment apparatus and a cooling treatment method for molten slag according to the present invention.

圖24為本發明的熔化熔渣之冷卻處理裝置及冷卻處理方法另一實施形態的示意正視圖。 Fig. 24 is a schematic front elevational view showing another embodiment of a cooling treatment apparatus and a cooling treatment method for molten slag according to the present invention.

圖25為圖4~圖6等所示拉伸輥所使用之內部冷卻機構一實施形態的示意剖視圖。 Fig. 25 is a schematic cross-sectional view showing an embodiment of an internal cooling mechanism used in the stretching rolls shown in Figs. 4 to 6 and the like.

圖26為本發明裝置的冷卻滾筒旋轉數與熔渣處理量之關係圖。 Figure 26 is a graph showing the relationship between the number of rotations of the cooling drum and the amount of slag treatment in the apparatus of the present invention.

1‧‧‧橫式冷卻滾筒 1‧‧‧Horizontal cooling drum

2‧‧‧盛桶 2‧‧‧ barrel

7‧‧‧冷卻手段 7‧‧‧cooling means

8‧‧‧搬送輸送帶 8‧‧‧Transport conveyor belt

9‧‧‧熔渣桶 9‧‧‧ slag bucket

100‧‧‧滾筒面 100‧‧‧ Roller surface

Sx‧‧‧熔渣 Sx‧‧‧ slag

Claims (11)

一種熔化熔渣之冷卻處理裝置,其特徵為,以使盛桶(2)之前端部鄰接或靠近於橫式冷卻滾筒(1)之滾筒面(100)之方式,設置使熔化熔渣附著於外周滾筒面(100)並予以冷卻,且可旋轉的單一橫式冷卻滾筒(1)、及對該橫式冷卻滾筒(1)供應熔化熔渣的盛桶(2);僅由該盛桶(2)與該橫式冷卻滾筒(1)形成熔渣液滯留部(A);在隨該橫式冷卻滾筒(1)的旋轉,而熔渣液滯留部(A)內的熔化熔渣附著於滾筒面(100)上並被帶出之後,從滾筒面(100)剝離並朝一方向被排出。 A cooling treatment device for melting slag, characterized in that the molten slag is attached to the front side of the tub (2) adjacent to or close to the drum surface (100) of the horizontal cooling drum (1) a peripheral roller surface (100) and cooled, and a rotatable single horizontal cooling drum (1), and a barrel (2) for supplying molten slag to the horizontal cooling drum (1); 2) forming a slag liquid retention portion (A) with the horizontal cooling drum (1); and the molten slag in the slag liquid retention portion (A) adheres to the rotation of the horizontal cooling drum (1) After being taken out on the drum surface (100), it is peeled off from the drum surface (100) and discharged in one direction. 如申請專利範圍第1項之熔化熔渣之冷卻處理裝置,其中,具有用於將橫式冷卻滾筒(1)的滾筒面(100)上所附著之熔化熔渣施行軋延,並朝滾筒寬度方向拉伸的拉伸輥(3)。 A cooling treatment apparatus for molten slag according to claim 1, wherein the molten slag attached to the drum surface (100) of the horizontal cooling drum (1) is rolled and oriented toward the drum width Stretching roller (3) in the direction of stretching. 如申請專利範圍第1或2項之熔化熔渣之冷卻處理裝置,其中,作成為在上述盛桶(2)下方設置氣體噴射手段(10),對盛桶(2)之前端部與滾筒面(100)之間隙部分噴射迫淨氣體,以防止熔化熔渣洩漏。 A cooling treatment device for molten slag according to claim 1 or 2, wherein a gas injection means (10) is provided below the barrel (2), and a front end portion and a drum surface of the barrel (2) are provided. The gap portion of (100) is sprayed with a forced gas to prevent the molten slag from leaking. 如申請專利範圍第1或2項之熔化熔渣之冷卻處理裝置,其中,具有用於將流體吹入至熔渣液滯留部(A)內的流體供應手段(6)。 A cooling treatment apparatus for melting slag according to claim 1 or 2, further comprising a fluid supply means (6) for blowing a fluid into the slag liquid retention portion (A). 如申請專利範圍第1或2項之熔化熔渣之冷卻處理裝置,其中,具有用於將從橫式冷卻滾筒(1)的滾筒面(100) 剝離的熔渣施行冷卻的冷卻手段(7)。 A cooling treatment apparatus for melting slag according to claim 1 or 2, wherein there is a drum surface (100) for cooling the drum (1) from the horizontal direction The stripped slag is subjected to cooling means (7) for cooling. 一種熔化熔渣之冷卻處理方法,係使用申請專利範圍第1至5項中任一項之冷卻處理裝置,對熔化熔渣施行冷卻處理。 A method for cooling a molten slag, which is subjected to a cooling treatment using a cooling treatment apparatus according to any one of claims 1 to 5. 如申請專利範圍第6項之熔化熔渣之冷卻處理方法,係使用具有拉伸輥(3)之冷卻處理裝置者,將熔渣鹼度[質量比:%CaO/%SiO2]為2以上的熔化熔渣作為處理對象,並將滾筒面(100)上所附著之熔化熔渣以拉伸輥(3)施行軋延而朝滾筒寬度方向拉伸。 For the cooling treatment method of the molten slag according to item 6 of the patent application, the slag basicity [mass ratio: %CaO/%SiO 2 ] is 2 or more, using a cooling treatment apparatus having a stretching roll (3). The molten slag is treated as a treatment object, and the molten slag adhering to the drum surface (100) is rolled by the stretching roll (3) to be stretched in the drum width direction. 如申請專利範圍第6或7項之熔化熔渣之冷卻處理方法,其係使用具有熔渣液滯留部(A)的冷卻處理裝置者,在熔渣液滯留部(A)內的熔化熔渣中添加粉體。 The method for cooling a molten slag according to claim 6 or 7, which is a molten slag in a slag liquid retention portion (A) using a cooling treatment device having a slag liquid retention portion (A) Add powder to it. 如申請專利範圍第6或7項之熔化熔渣之冷卻處理方法,係使用具有熔渣液滯留部(A)的冷卻處理裝置者,對熔渣液滯留部(A)內的熔化熔渣中吹入流體。 The cooling treatment method of the molten slag according to the sixth or seventh aspect of the patent application is the use of the cooling treatment device having the slag liquid retention portion (A) in the molten slag in the slag liquid retention portion (A) Blow in the fluid. 如申請專利範圍第6或7項之熔化熔渣之冷卻處理方法,係進行下述(i)~(iv)中至少一者的熱回收:(i)從通過橫式冷卻滾筒(1)內部的冷媒施行熱回收;(ii)在使用了具有堰(4)的冷卻處理裝置的熔化熔渣之冷卻處理中,從通過堰(4)內部的冷媒進行熱回收;(iii)使藉橫式冷卻滾筒(1)冷卻的熔渣進一步與冷媒相接觸而冷卻,從該冷媒施行熱回收; (iv)在使用了具有熔渣液滯留部(A)的冷卻處理裝置的熔化熔渣之冷卻處理中,於在熔渣液滯留部(A)內的熔化熔渣中吹入流體時,將所吹入的流體回收,從該流體施行熱回收。 The method for cooling a molten slag according to claim 6 or 7 is to perform heat recovery of at least one of the following (i) to (iv): (i) from the inside of the horizontal cooling drum (1) The refrigerant is subjected to heat recovery; (ii) in the cooling treatment using the molten slag having the enthalpy (4) cooling treatment device, heat recovery is performed from the refrigerant passing through the ruthenium (4); (iii) The slag cooled by the cooling drum (1) is further cooled by contact with the refrigerant, and heat recovery is performed from the refrigerant; (iv) in the cooling treatment of the molten slag using the cooling treatment device having the slag liquid retention portion (A), when the fluid is blown into the molten slag in the slag liquid retention portion (A), The blown fluid is recovered and heat recovery is performed from the fluid. 一種熔渣製品之製造方法,係將以申請專利範圍第6至10項中任一項之冷卻處理方法進行冷卻而凝固的熔渣,施行破碎處理或/及磨碎處理,而獲得粒狀熔渣製品。 A method for producing a slag product, which is obtained by cooling and solidifying a slag which is cooled by a cooling treatment method according to any one of claims 6 to 10, and is subjected to a crushing treatment and/or a grinding treatment to obtain a granular melting. Slag products.
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