JPH0733266B2 - Jet fluidized bed granulator - Google Patents
Jet fluidized bed granulatorInfo
- Publication number
- JPH0733266B2 JPH0733266B2 JP36048992A JP36048992A JPH0733266B2 JP H0733266 B2 JPH0733266 B2 JP H0733266B2 JP 36048992 A JP36048992 A JP 36048992A JP 36048992 A JP36048992 A JP 36048992A JP H0733266 B2 JPH0733266 B2 JP H0733266B2
- Authority
- JP
- Japan
- Prior art keywords
- diameter
- nozzle
- furnace
- dispersion plate
- fluidized bed
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
- B01J8/44—Fluidisation grids
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Crucibles And Fluidized-Bed Furnaces (AREA)
- Glanulating (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
Description
【０００１】[0001]
【産業上の利用分野】本発明は、多孔板型分散板を改善
した噴流流動層造粒炉に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a jet fluidized bed granulation furnace having an improved perforated plate type dispersion plate.
【０００２】[0002]
【従来の技術】造粒炉の多孔板型分散板においては、同
一径のノズルを分散板全域にわたって均一になるように
配置している。（例えば、実開昭６０−１０１９８号公
報，特開平１−２５４２４２号公報，特開平１−２８４
５０９号公報参照）2. Description of the Related Art In a perforated plate type dispersion plate of a granulating furnace, nozzles having the same diameter are arranged so as to be uniform over the entire area of the dispersion plate. (For example, JP-B-60-10198, JP-A-1-254242, and JP-A-1-284.
(See Japanese Patent Publication No. 509)
【０００３】[0003]
【発明が解決しようとする課題】実開昭６０−１０１９
８号公報に示す粉末原料の流動焼成炉にあっては、ノズ
ルが分散板全域にわたって均一になるよう配置されてい
る。このような分散板の構成は造粒炉にも適応されてお
り、そのため造粒炉の層温度は均一となっている。その
結果図８，図９で示すように、造粒炉層内部分の壁面に
コーチングが発生しやすい。即ち、図９から明らかなよ
うに、最外周のノズル径のジェット径がノズルピッチよ
り小さいことが原因であり、図のようにコーチングが発
生する。また、造粒炉にて一旦大径粒子が生成される
と、造粒炉から排出できずに分散板上に堆積し、流動化
に異常が発生し、長期安定運転に支障をきたすという課
題がある。[Problems to be solved by the invention]
In the fluidized-bed firing furnace for powder raw material shown in Japanese Patent No. 8, the nozzles are arranged so as to be uniform over the entire dispersion plate. Such a configuration of the dispersion plate is also applied to the granulation furnace, and therefore the bed temperature of the granulation furnace is uniform. As a result, as shown in FIGS. 8 and 9, coating is likely to occur on the wall surface inside the granulation furnace layer. That is, as is clear from FIG. 9, the cause is that the jet diameter of the outermost peripheral nozzle diameter is smaller than the nozzle pitch, and thus coaching occurs as shown in the figure. In addition, once large particles are generated in the granulation furnace, they cannot be discharged from the granulation furnace and are deposited on the dispersion plate, causing abnormal fluidization, which hinders long-term stable operation. is there.
【０００４】また、造粒炉とは異るが特開平１−２５４
２４２号公報に示す流動層反応装置のように、外周部で
上昇し中心部で下降する粒子循環流を形成するために、
外周部のノズル開口率を大きくしている。しかしながら
造粒炉による造粒のためには、炉構造の外周部がコーン
状で粒子の移動層下降流が必要であって、ある程度の下
降速度を確保するには、外周部ノズルの開口率は中心部
と同じか、あるいは、それ以下とする必要がある。Further, although different from the granulating furnace, it is disclosed in Japanese Patent Laid-Open No. 1-254.
As in the fluidized bed reactor shown in Japanese Patent No. 242, in order to form a particle circulation flow that rises at the outer peripheral portion and descends at the central portion,
The nozzle opening ratio of the outer peripheral portion is increased. However, for granulation by the granulation furnace, the outer peripheral part of the furnace structure is cone-shaped and a moving bed descending flow of particles is required, and in order to secure a certain descending speed, the aperture ratio of the outer peripheral nozzle is It must be equal to or less than the center.
【０００５】前記特開平１−２８４５０９号公報に示さ
れるガス分散板は、流動層全体の粒子が渦流となるよう
各ノズル上にガスが一方向から吹き出すキャップを設け
ている。このような手段では、噴流ガスのジェット長さ
は数１００mmなので、分散板直上面は粒子の渦流により
付着防止は可能であるが、側壁面への付着は防止できな
い。The gas dispersion plate disclosed in the above-mentioned Japanese Patent Laid-Open No. 1-284509 is provided with a cap that blows out gas from one direction on each nozzle so that particles in the entire fluidized bed form a vortex. With such a means, since the jet length of the jet gas is several hundreds mm, the particles can be prevented from adhering to the surface directly above the dispersion plate by the vortex flow of particles, but cannot be prevented from adhering to the side wall surface.
【０００６】本発明の目的は、簡単な手段により造粒炉
層内壁面へのコーチング発生を防止し、造粒効率の向
上、大径粒子の排出処理を合理的に行うことにある。An object of the present invention is to prevent the occurrence of coating on the inner wall surface of the granulating furnace layer by a simple means, improve the granulating efficiency, and rationally perform the discharging process of large-diameter particles.
【０００７】[0007]
【課題を解決するための手段】従来技術の課題を解決す
る本発明の構成は、造粒炉の多孔板型分散板に形成した
最外周のノズル径を中央部のノズル径より小径とし、最
外周ノズルのジェット径をノズルピッチより大きくした
ものであり、また、造粒炉の多孔板型分散板の中央部に
大径ノズルを、周辺部に複数の小径ノズルを形成し、前
記大径ノズル近傍に燃料吹き込みノズルを配設したもの
である。The structure of the present invention which solves the problems of the prior art is such that the outermost peripheral nozzle diameter formed in the perforated plate type dispersion plate of the granulation furnace is smaller than the central nozzle diameter. The jet diameter of the outer peripheral nozzle is made larger than the nozzle pitch, and a large diameter nozzle is formed in the central portion of the perforated plate type dispersion plate of the granulation furnace, and a plurality of small diameter nozzles are formed in the peripheral portion. A fuel injection nozzle is arranged in the vicinity.
【０００８】[0008]
【作用】請求項１においては、分散板外周部におけるジ
ェット径が互いに干渉してデッドゾーンがなくなり、層
内コーン部のコーチングが防止できる。分散板中心部の
ジェット長さが大になり、噴流層により近いので造粒性
も向上する。請求項２においては、分散板中心部に燃料
を吹き込み、中心部の温度をより高くすると、造粒性は
さらに向上するとともに、コーン部壁面の粒子降下速度
が大きくなり、コーチングの発生が防止できる。また、
造粒炉で生成された大径の造粒物が大径ノズルを経て焼
成炉に排出され、造粒炉において流動化異常が起らな
い。According to the first aspect of the invention, the jet diameters in the outer peripheral portion of the dispersion plate interfere with each other to eliminate the dead zone, and the coating of the inner layer cone portion can be prevented. Since the jet length in the central part of the dispersion plate becomes large and it is closer to the spouted bed, granulation is also improved. In the second aspect, when the fuel is blown into the central portion of the dispersion plate and the temperature of the central portion is made higher, the granulating property is further improved, and the particle descent rate on the wall surface of the cone portion is increased, so that the occurrence of coating can be prevented. . Also,
The large-diameter granulated product generated in the granulation furnace is discharged to the firing furnace through the large-diameter nozzle, and no fluidization abnormality occurs in the granulation furnace.
【０００９】[0009]
【実施例】次に、図面について本発明実施例の詳細を説
明する。図１は本願発明造粒炉が使用される流動床セメ
ント焼成設備の概略図、図２は造粒炉の縦断正面図、図
３は分散板の平面図、図４は分散板中心部近傍に燃料吹
き込みノズルを設けた造粒炉の縦断正面図、図５は図４
における分散板の第１実施例の平面図、図６は図４にお
ける分散板の第２実施例の平面図、図７は図４における
分散板の第３実施例の平面図である。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Next, details of embodiments of the present invention will be described with reference to the drawings. FIG. 1 is a schematic view of a fluidized bed cement burning facility in which the granulating furnace of the present invention is used, FIG. 2 is a vertical sectional front view of the granulating furnace, FIG. 3 is a plan view of a dispersion plate, and FIG. FIG. 4 is a vertical sectional front view of a granulation furnace provided with a fuel injection nozzle.
6 is a plan view of a first embodiment of the dispersion plate in FIG. 6, FIG. 6 is a plan view of a second embodiment of the dispersion plate in FIG. 4, and FIG. 7 is a plan view of a third embodiment of the dispersion plate in FIG.
【００１０】図１について装置の全体系統を説明する
と、１はサスペンションプレヒータで、該サスペンショ
ンプレヒータ１は、サイクロンＣ1，Ｃ2，Ｃ3によって
構成されている。原料投入シュート２から系内に投入さ
れたセメント原料粉は、サイクロンＣ3→Ｃ2→Ｃ1を経
て予熱されたのち流動層型式の造粒炉３内に投入され
る。造粒炉３内で流動整粒された造粒物は、オーバーフ
ロー排出孔から排出され排出シュート４からＬバルブ
（気密排出装置）５を経て流動層焼成炉６に投入せしめ
られ、焼成炉６において焼成せしめられたのち、流動床
クーラ７，移動床クーラ８を経てセメントクリンカとし
て回収される。図中９は微粉炭燃料供給ライン，１０は
重油バーナである。The entire system of the apparatus will be described with reference to FIG. 1. 1 is a suspension preheater, and the suspension preheater 1 is composed of cyclones C 1 , C 2 and C 3 . The cement raw material powder fed into the system from the raw material feeding chute 2 is preheated through a cyclone C 3 → C 2 → C 1 and then fed into a fluidized bed type granulating furnace 3. The granulated material that has been fluidized and granulated in the granulating furnace 3 is discharged from the overflow discharge hole, and is introduced into the fluidized bed calcining furnace 6 from the discharging chute 4 through the L valve (airtight discharging device) 5, and in the calcining furnace 6. After being fired, it is recovered as cement clinker through the fluidized bed cooler 7 and the moving bed cooler 8. In the figure, 9 is a pulverized coal fuel supply line, and 10 is a heavy oil burner.
【００１１】次に図２，図３について請求項１に対応す
る噴流流動層造粒炉３について説明する。前記造粒炉３
に形成されたスロート部１１の上部に、上面が造粒炉３
のコーン部３ａの下端部近傍に対応する多孔板型の分散
板１２を配設する。そして、該分散板１２の中央部に複
数の大径ノズル１２ａを形成するとともに、外周部に多
数の小径ノズル１２ｂを設け、最外周の小径ノズル１２
ｂのジェット径ｄｊをノズルピッチより大きく形成した
ものである。分散板中心部のノズルは少数，大径程、大
径造粒物の流動層焼成炉への排出が円滑に行われ、流動
化の異常発生を防止し長期安定運転が可能であり、分散
板の強度上も向上されるように構成したものである。Next, a jet fluidized bed granulation furnace 3 corresponding to claim 1 will be described with reference to FIGS. The granulating furnace 3
The upper surface of the throat portion 11 formed on the
A perforated plate type dispersion plate 12 corresponding to the vicinity of the lower end of the cone portion 3a is disposed. A plurality of large-diameter nozzles 12a are formed in the central portion of the dispersion plate 12, and a large number of small-diameter nozzles 12b are provided in the outer peripheral portion, so that the outermost peripheral small-diameter nozzle 12 is provided.
The jet diameter dj of b is formed larger than the nozzle pitch. The number of nozzles in the center of the dispersion plate is small, the diameter is large, and the large-diameter granules are smoothly discharged to the fluidized bed firing furnace, which prevents abnormal occurrence of fluidization and enables stable operation for a long time. Is also configured to be improved in strength.
【００１２】次に、図４〜図７について請求項２に対応
する噴流流動層造粒炉３について説明する。図４，図５
は分散板１２の中心部に１個の大径ノズル１２ａを形成
し、小径ノズル１２ｂを均一に分散形成するとともに、
前記大径ノズル１２ａの近傍に燃料吹き込みノズル（バ
ーナ）１３を配設したものである。また、図６に示す実
施例は、分散板１２の中央部に複数の大径ノズル１２ａ
を設け、外周に適当ピッチごとに小径ノズル１２ｂを形
成し、中心の大径ノズル１２ａの近傍に燃料吹き込みノ
ズル（バーナ）１３を配設したものである。図７の実施
例は、分散板１２の中央部に複数の大径ノズル１２ａを
設け、小径ノズル１２ｂを均一に分散形するとともに、
中心の大径ノズル１２ａの近傍に燃料吹き込みノズル
（バーナ）１３を配設したものである。Next, the jet fluidized bed granulation furnace 3 corresponding to claim 2 will be described with reference to FIGS. 4 and 5
Forms one large diameter nozzle 12a at the center of the dispersion plate 12 and forms small diameter nozzles 12b uniformly and
A fuel injection nozzle (burner) 13 is arranged near the large diameter nozzle 12a. Further, in the embodiment shown in FIG. 6, a plurality of large-diameter nozzles 12a are provided at the center of the dispersion plate 12.
, Small-diameter nozzles 12b are formed on the outer periphery at appropriate pitches, and a fuel injection nozzle (burner) 13 is arranged near the central large-diameter nozzle 12a. In the embodiment of FIG. 7, a plurality of large-diameter nozzles 12a are provided in the central portion of the dispersion plate 12, and small-diameter nozzles 12b are uniformly dispersed.
A fuel injection nozzle (burner) 13 is arranged near the central large-diameter nozzle 12a.
【００１３】[0013]
【作用の説明】造粒炉分散板１２の中央部に大径ノズル
１２ａを配置し、小径ノズル１２ｂを周辺部に配置する
ことにより、層内粒子の挙動は次のようになる。 （ａ）周辺部の小径ノズル１２ｂからの流動化ガス量よ
り、大径ノズル１２ａからの流動化ガス量が多い。その
結果、造粒炉３の中央部での粒子上昇エネルギーが炉周
辺部より大きく、従って、中央部の粒子は大径ノズル１
２ａから流動化ガスによって上昇流を形成し、周辺部の
粒子は下降流を形成する層内粒子循環流を形成する。 （ｂ）燃料吹き込みノズルを大径ノズル１２ａの近傍に
設置すると、層内中央部の温度が高く、周辺部の温度が
低くなるような温度分布が層内に形成され、その結果、
造粒の場が炉中央部に限定され、壁面へのコーチングが
防止できる。 （ｃ）分散板１２の中央部に設置した大径ノズル１２ａ
は、造粒炉３で生成された大径の造粒物を焼成炉６に排
出させ、造粒炉３における流動化異常発生を防止する。[Description of Action] By arranging the large-diameter nozzle 12a in the central part of the granulating furnace dispersion plate 12 and arranging the small-diameter nozzle 12b in the peripheral part, the behavior of in-layer particles becomes as follows. (A) The fluidizing gas amount from the large diameter nozzle 12a is larger than the fluidizing gas amount from the small diameter nozzle 12b in the peripheral portion. As a result, the particle rising energy in the central part of the granulation furnace 3 is larger than that in the peripheral part of the furnace, and therefore the particles in the central part are larger in diameter than the large diameter nozzle
An upward flow is formed by the fluidizing gas from 2a, and the particles in the peripheral portion form an intra-layer particle circulation flow forming a downward flow. (B) When the fuel injection nozzle is installed in the vicinity of the large-diameter nozzle 12a, a temperature distribution is formed in the layer such that the temperature in the center of the layer is high and the temperature of the peripheral portion is low.
The granulation site is limited to the central part of the furnace, and the coating on the wall surface can be prevented. (C) Large diameter nozzle 12a installed in the center of the dispersion plate 12
Discharges the large-diameter granules generated in the granulation furnace 3 to the firing furnace 6 to prevent fluidization abnormality from occurring in the granulation furnace 3.
【００１４】[0014]
【発明の効果】上述のように本発明の構成によれば、次
のような効果が得られる。 （ａ）分散板最外周に配置したノズルのジェット径を、
ノズルピッチより大きく形成したことにより、分散板外
周部のデッドゾーンがなくなり、層内コーン部のコーチ
ング発生，付着が合理的に防止しうる。（請求項１） （ｂ）分散板中央部に大径ノズルを配置し、周辺部に小
径ノズルを配置したことにより、層内粒子は大径ノズル
から流動化ガスによって上昇流を形成し、周辺部の粒子
は下降流となる層内粒子循環流を形成し、層内コーン部
におけるコーチングの発生，付着が防止しうる。（請求
項１，請求項２） （ｃ）大径ノズルが配置してあるため、造粒炉で生成さ
れた大径の造粒物が大径ノズルを経由して焼成炉に排出
され、造粒炉における流動化の異常発生が合理的に防止
でき、長期安定運転の向上が図れる。（請求項１，請求
項２） （ｄ）分散板中央部に配置した大径ノズルの近傍に、燃
料吹き込みノズルを設置したことにより、層内中央部の
温度が高く、周辺部の温度が低くなるような温度分布を
層内に形成することができ、その結果、造粒の場が炉中
央部に限定され、層内コーン部へのコーチングが防止で
きる。（請求項２）As described above, according to the structure of the present invention, the following effects can be obtained. (A) The jet diameter of the nozzle arranged on the outermost periphery of the dispersion plate is
By forming it larger than the nozzle pitch, the dead zone on the outer peripheral portion of the dispersion plate is eliminated, and it is possible to rationally prevent the occurrence and adhesion of coating on the inner cone portion. (Claim 1) (b) A large-diameter nozzle is arranged in the central part of the dispersion plate, and a small-diameter nozzle is arranged in the peripheral part, whereby the in-layer particles form an upward flow by the fluidizing gas from the large-diameter nozzle, Partial particles form an in-layer particle circulation flow that is a downward flow, and the occurrence and adhesion of coating at the in-layer cone part can be prevented. (Claims 1 and 2) (c) Since the large-diameter nozzle is arranged, the large-diameter granules produced in the granulation furnace are discharged to the firing furnace via the large-diameter nozzle, Abnormal occurrence of fluidization in the granulator can be reasonably prevented, and long-term stable operation can be improved. (Claims 1 and 2) (d) Since the fuel injection nozzle is installed in the vicinity of the large-diameter nozzle arranged in the center of the dispersion plate, the temperature in the center of the layer is high and the temperature in the periphery is low. Such a temperature distribution can be formed in the bed, and as a result, the granulation field is limited to the central part of the furnace, and coating to the in-layer cone part can be prevented. (Claim 2)
【図１】本願発明造粒炉が使用される流動床セメント焼
成設備の概略図である。FIG. 1 is a schematic view of a fluidized bed cement burning facility in which a granulating furnace of the present invention is used.
【図２】造粒炉の縦断正面図である。FIG. 2 is a vertical sectional front view of a granulating furnace.
【図３】分散板の平面図である。FIG. 3 is a plan view of a dispersion plate.
【図４】分散板中心部近傍に燃料吹き込みノズルを設け
た造粒炉の縦断正面図である。FIG. 4 is a vertical cross-sectional front view of a granulation furnace in which a fuel injection nozzle is provided near the center of a dispersion plate.
【図５】図４における分散板の第１実施例の平面図であ
る。5 is a plan view of a first embodiment of the dispersion plate in FIG.
【図６】図４における分散板の第２実施例の平面図であ
る。FIG. 6 is a plan view of a second embodiment of the dispersion plate in FIG.
【図７】図４における分散板の第３実施例の平面図であ
る。FIG. 7 is a plan view of a third embodiment of the dispersion plate in FIG.
【図８】従来造粒炉の縦断正面図である。FIG. 8 is a vertical sectional front view of a conventional granulating furnace.
【図９】従来造粒炉の分散板平面図である。FIG. 9 is a plan view of a dispersion plate of a conventional granulation furnace.
３ 造粒炉 ３ａ コーン部 １１ スロート部 １２ 分散板 １２ａ 大径ノズル １２ｂ 小径ノズル １３ 燃料吹き込みノズル 3 Granulator 3a Cone part 11 Throat part 12 Dispersion plate 12a Large diameter nozzle 12b Small diameter nozzle 13 Fuel injection nozzle
───────────────────────────────────────────────────── フロントページの続き (72)発明者 石鉢 俊幸 東京都千代田区神田美土代町１番地 住友 セメント株式会社内 (72)発明者 橋本 勲 兵庫県明石市川崎町１番１号 川崎重工業 株式会社 明石工場内 (72)発明者 村尾 三樹雄 兵庫県神戸市中央区東川崎町３丁目１番１ 号 川崎重工業株式会社 神戸工場内 (72)発明者 熊谷 親徳 兵庫県明石市川崎町１番１号 川崎重工業 株式会社 明石工場内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Toshiyuki Ishibachi No. 1 Kanda Midoshiro-cho, Chiyoda-ku, Tokyo Sumitomo Cement Co., Ltd. (72) Inventor Isao Hashimoto 1-1 Kawasaki-cho, Akashi-shi, Hyogo Kawasaki Heavy Industries Inside the Akashi Plant (72) Inventor Mikio Murao 3-1-1 Higashikawasaki-cho, Chuo-ku, Kobe City, Hyogo Prefecture Kawasaki Heavy Industries Ltd. Inside the Kobe Plant (72) Inventor Chikunori Kumagai 1-1 Kawasaki-cho, Akashi City, Hyogo Prefecture Kawasaki Heavy Industries Ltd. Akashi Factory
Claims (2)
周のノズル径を中央部のノズル径より小径とし、最外周
ノズルのジェット径をノズルピッチより大きくしたこと
を特徴とする噴流流動層造粒炉。1. A jet flow characterized in that the outermost peripheral nozzle diameter formed in a perforated plate type dispersion plate of a granulating furnace is smaller than the central nozzle diameter, and the outermost peripheral nozzle has a jet diameter larger than the nozzle pitch. Fluidized bed granulation furnace.
ノズルを、周辺部に複数の小径ノズルを形成し、前記大
径ノズル近傍に燃料吹き込みノズルを配設したことを特
徴とする噴流流動層造粒炉。2. A large-diameter nozzle is formed in a central portion of a perforated plate type dispersion plate of a granulating furnace, a plurality of small-diameter nozzles are formed in a peripheral portion, and a fuel injection nozzle is arranged in the vicinity of the large-diameter nozzle. And a jet fluidized bed granulator.
Priority Applications (9)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP36048992A JPH0733266B2 (en) | 1992-12-28 | 1992-12-28 | Jet fluidized bed granulator |
| TW082110601A TW290530B (en) | 1992-12-28 | 1993-12-14 | |
| DK93120421T DK0605832T3 (en) | 1992-12-28 | 1993-12-17 | Apparatus for making cement clinker |
| EP93120421A EP0605832B1 (en) | 1992-12-28 | 1993-12-17 | Apparatus for manufacturing cement clinker |
| DE69330940T DE69330940T2 (en) | 1992-12-28 | 1993-12-17 | Apparatus for the production of cement clinker |
| US08/174,693 US5478234A (en) | 1992-12-28 | 1993-12-27 | Apparatus for manufacturing cement clinker |
| CN93119976A CN1055755C (en) | 1992-12-28 | 1993-12-28 | Apparatus for manufacturing cement clinker |
| KR1019930030196A KR970001243B1 (en) | 1992-12-28 | 1993-12-28 | Cement Clinker Manufacturing Equipment |
| US08/469,198 US5944513A (en) | 1992-12-28 | 1995-06-06 | Apparatus for manufacturing cement clinker |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP36048992A JPH0733266B2 (en) | 1992-12-28 | 1992-12-28 | Jet fluidized bed granulator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH06198159A JPH06198159A (en) | 1994-07-19 |
| JPH0733266B2 true JPH0733266B2 (en) | 1995-04-12 |
Family
ID=18469621
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP36048992A Expired - Lifetime JPH0733266B2 (en) | 1992-12-28 | 1992-12-28 | Jet fluidized bed granulator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0733266B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5322454B2 (en) * | 2008-02-12 | 2013-10-23 | ホソカワミクロン株式会社 | Spouted bed granulator |
| CN102534127A (en) * | 2011-12-30 | 2012-07-04 | 苏州新锐工程工具有限公司 | Heat treatment charging basket for up-pushing zipper chamber furnace |
-
1992
- 1992-12-28 JP JP36048992A patent/JPH0733266B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH06198159A (en) | 1994-07-19 |
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