JPS5940499B2 - Equipment for mixing and dispensing solid granular materials - Google Patents

Equipment for mixing and dispensing solid granular materials

Info

Publication number
JPS5940499B2
JPS5940499B2 JP56116535A JP11653581A JPS5940499B2 JP S5940499 B2 JPS5940499 B2 JP S5940499B2 JP 56116535 A JP56116535 A JP 56116535A JP 11653581 A JP11653581 A JP 11653581A JP S5940499 B2 JPS5940499 B2 JP S5940499B2
Authority
JP
Japan
Prior art keywords
container
mixing
bed
granular
equipment
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP56116535A
Other languages
Japanese (ja)
Other versions
JPS57122927A (en
Inventor
バイマ−ル・ケイ・ビスワス
ジヨセフ・イ−・コ−キ−
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Foster Wheeler Energy Corp
Original Assignee
Foster Wheeler Energy Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Foster Wheeler Energy Corp filed Critical Foster Wheeler Energy Corp
Priority to GB08207898A priority Critical patent/GB2103326B/en
Priority to DE19823211082 priority patent/DE3211082A1/en
Publication of JPS57122927A publication Critical patent/JPS57122927A/en
Priority to US06/623,640 priority patent/US4541302A/en
Publication of JPS5940499B2 publication Critical patent/JPS5940499B2/en
Expired legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23KFEEDING FUEL TO COMBUSTION APPARATUS
    • F23K3/00Feeding or distributing of lump or pulverulent fuel to combustion apparatus
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00Other mixers; Mixing plants; Combinations of mixers
    • B01F33/40Mixers using gas or liquid agitation, e.g. with air supply tubes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24Chemical 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
    • B01J8/245Spouted-bed technique

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion & Propulsion (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Mixers With Rotating Receptacles And Mixers With Vibration Mechanisms (AREA)
  • Accessories For Mixers (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)

Description

【発明の詳細な説明】 本発明は、一種類または二種類以上の粒状材料を受入れ
、それを容器内で混合して複数の隔置された排出口を通
して該容器から例えば流動床式燃焼器などの他の使用場
所へ分配するための混合分配装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention receives one or more particulate materials, mixes them in a container, and exits the container through a plurality of spaced-apart outlets, such as in a fluidized bed combustor. The invention relates to a mixing and dispensing device for dispensing to other locations of use.

流動床式燃焼器は、熱を創生するための効果的な手段と
して古くから認められている。
Fluidized bed combustors have long been recognized as an effective means of generating heat.

この種の装置においては、粒状石炭等の燃料と、石炭の
燃焼の結果として放出される硫黄を吸着するための吸着
剤である粒状石灰石との混合物を含む粒状材フ 料の床
を格子または格子状の板の上に載置し、この床を通して
空気を吹込み、粒状材料をあたかも沸騰液のように流動
化させて燃料の燃焼を促進させる。この粒状材料床へは
、該床を収容している容器ワ の壁の周壁に周方向に間
隔を置いて透設した複数の供給管を通して連続的に粒状
燃料と粒状吸着剤の混合物を供給しなければならない。
In this type of equipment, a bed of granular material containing a mixture of a fuel, such as granular coal, and granular limestone, which is an adsorbent for adsorbing the sulfur released as a result of the combustion of the coal, is installed on a grid or grating. Air is blown through this bed to fluidize the particulate material like boiling liquid and accelerate the combustion of the fuel. A mixture of granular fuel and granular adsorbent is continuously supplied to this granular material bed through a plurality of supply pipes that are circumferentially spaced through the peripheral wall of the vessel wall containing the bed. There must be.

しかしながら、粒状燃料と粒状吸着剤の均一な混合物を
複数の供給管へ均一に分配することは、材料搬送の観フ
点からみて容易ではない。従つて、本発明の目的は、
一種類または二種類以上の粒状材料を複数の供給源から
受取り、それらの粒状材料をガス流により流動化させる
ことにより混合して均一な混合物とし、その混合物を複
5 数の排出管を通して例えば流動床式燃焼器の複数の
供給管へ均一に分配するための混合分配装置を提供する
ことである。
However, uniformly distributing a homogeneous mixture of granular fuel and granular adsorbent to multiple supply pipes is not easy from a material transportation standpoint. Therefore, the object of the present invention is to
One or more particulate materials are received from multiple sources, mixed into a homogeneous mixture by fluidizing the particulate materials with a gas stream, and the mixture is passed through a plurality of discharge pipes, e.g. It is an object of the present invention to provide a mixing and distribution device for uniformly distributing a plurality of feed pipes of a bed type combustor.

略述すれば、本発明の装置は、粒状材料床を支持するよ
うになされており、補給材料を受入れる0 ための導入
口手段を備えた容器から成る。
Briefly, the apparatus of the present invention comprises a container adapted to support a bed of granular material and provided with inlet means for receiving a make-up material.

加圧ガスを容器の下方部分へ導入する。その加圧ガスは
容器内の材料内を上向きに通つて噴射状態となり、容器
内に材料の流動を誘起してその混合を促進し材料を多数
の排出口ヘ均一に分配させるのに十分5 な速度で導入
する。第1および第2図を参照すると、例えば流動床の
ための破砕石炭供給源と、石炭の燃焼の結果として発生
する硫黄を吸着するための石灰石の供給源のような1つ
またはそれ以上の供給源(図示せず)から粒状材料を受
入れるようになされた開放上端12を有する細長い円筒
型容器10から成る本発明の混合分配装置が示されてい
る。
Pressurized gas is introduced into the lower part of the container. The pressurized gas is passed upwardly through the material in the container and into a jet, sufficient to induce a flow of the material within the container to promote its mixing and evenly distribute the material to a number of outlets. Deploy with speed. 1 and 2, one or more supplies, such as a source of crushed coal for the fluidized bed and a source of limestone for adsorbing sulfur generated as a result of combustion of the coal. The mixing and dispensing apparatus of the present invention is shown comprising an elongated cylindrical container 10 having an open top end 12 adapted to receive particulate material from a source (not shown).

容器10の下端部分14は、円錐状ホツパの形に形成し
、該ホツパの小径部分には、外部供給源から空気等の加
圧ガスを受入れ、それを点線で示される方向に容器内を
上向きに通すための導入口16を整合させる。4つの等
角度に離隔させた排出管18を容器10内の一点から容
器壁を貫通して容器の外部の一点にまで水平面に対して
鋭角に延長させる。
The lower end portion 14 of the container 10 is formed in the form of a conical hopper having a small diameter portion that receives pressurized gas, such as air, from an external source and directs it upwardly through the container in the direction shown by the dotted line. The inlet port 16 for passing through is aligned. Four equiangularly spaced outlet tubes 18 extend from a point within the container 10 through the container wall to a point outside the container at an acute angle to the horizontal plane.

これらの管には耐火材20を被覆する。第3図に示され
るように、導入口16からの空気を通す円筒状の中央孔
24を有する充填プラグ22を容器10内のホツパ14
の直ぐ上に挿入する。
These tubes are coated with a refractory material 20. As illustrated in FIG.
Insert it directly above.

孔24の上端は、容器10内を流下する材料を受容する
円錐形開口26に連通させる。作動において、上述の2
つの別個の供給源からの材料を容器10の上端12へ導
入し、重力によつて容器内を流下させ容器内に堆積させ
る。
The upper end of hole 24 communicates with a conical opening 26 that receives material flowing down within container 10 . In operation, the above two
Materials from two separate sources are introduced into the upper end 12 of the container 10 and allowed to flow down and deposit within the container by gravity.

空気を導入口16へ導入し、ホツパ14およびプラグ2
2の円筒孔24を通し、容器10内に堆積している粒状
材料内を通して上昇させる。この空気の速度および流量
は、「噴射状態」が生じるように、即ち、容器内の粒状
材料床からの材料の一部分が床の上面から上に吹上げら
れるように設定する。この空気流の結果として、容器の
軸線と同心関係をなし、粒状材料の密度が低く、粒状材
料の全体的流れ方向が上向きである中心帯域30が形成
される。中心帯域30の周りには、粒状材料の密度が高
く、その全体的流れ方向が下向きである環状帯域32が
形成される。中心帯域30へは、開口26の近傍におい
て環状帯域32から粒状材料が連続的に供給され、それ
らの粒状材料は、高圧空気によつて床の上方部分へ吹上
げられた後再び環状帯域32内へ落下し、このサイクル
を繰返す。かくして、床内の粒状材料(この実施例では
粒状石炭と粒状石灰石)が完全に混合される。粒状材料
は、環状帯域32内を流下する間にその一部が排出管1
8の上端に流入し、重力によつて管18内を通つて容器
の外部へ排出される。
Air is introduced into the inlet 16, the hopper 14 and the plug 2
2 through the cylindrical holes 24 and up through the particulate material deposited in the container 10. The velocity and flow rate of this air is set such that a "jet condition" occurs, ie, a portion of the material from the bed of particulate material in the vessel is blown upwardly from the top of the bed. As a result of this airflow, a central zone 30 is formed that is concentric with the axis of the container, has a low density of particulate material, and has a general direction of flow of the particulate material upward. Around the central zone 30 is formed an annular zone 32 having a high density of particulate material whose general direction of flow is downward. The central zone 30 is continuously supplied with granular material from an annular zone 32 in the vicinity of the opening 26, which granular material is blown up by high-pressure air to the upper part of the floor and then returned to the annular zone 32. and repeat the cycle. Thus, the granular materials in the bed (in this example granular coal and granular limestone) are thoroughly mixed. Part of the particulate material flows down the annular zone 32 into the discharge pipe 1.
8 and is discharged by gravity through the tube 18 to the outside of the container.

第1〜3図の実施例においては、4本の排出管が設けら
れているので、混合ずみ材料が4つの別個の部位へ正確
に分配される。この混合分配装置を上述した流動床式燃
焼器に接続して該燃焼器へ粒状材料の混合物を分配する
場合は、混合分配装置の4本の排出管18の出口端を該
燃焼器の流動床収容容器(図示せず)の壁に透設した4
本の材料供給管(図示せず)に接続するための配管を設
けることができる。もちろん、容器10の上端12への
粒状材料の供給量は、容器10内の粒状材料が連続的に
補充されるように排出管18からの排出量に応じて調節
する。
In the embodiment of Figures 1-3, four discharge pipes are provided so that the mixed material is accurately distributed to four separate sites. When this mixing/distributing device is connected to the fluidized bed combustor described above to distribute a mixture of particulate materials to the combustor, the outlet ends of the four discharge pipes 18 of the mixing/distributing device are connected to the fluidized bed combustor of the combustor. 4 installed transparently on the wall of the storage container (not shown)
Piping can be provided for connection to a book material supply pipe (not shown). Of course, the amount of particulate material supplied to the upper end 12 of the container 10 is adjusted in accordance with the amount discharged from the discharge pipe 18 so that the particulate material in the container 10 is continuously replenished.

第4〜5図の実施例においては、第1〜3図の実施例の
充填プラグ22を省除し、4本の等角度に離隔させた材
料導入管34を容器のホツパ部分14の壁を貫通して水
平面に対し角度をなして延長させる。
In the embodiment of FIGS. 4-5, the fill plug 22 of the embodiment of FIGS. Penetrate and extend at an angle to the horizontal plane.

これらの管34は、先の実施例の場合と同様に1つまた
はそれ以上の供給源から粒状材料を受入れてそれを空気
導入口16の直ぐ上のホツパ14の下方部分内へ供給す
る。かくして、中心帯域と環状帯域が形成され、容器内
に先の実施例の場合と同様な材料の流れパターンが設定
される。
These tubes 34 receive particulate material from one or more sources and feed it into the lower portion of the hopper 14 directly above the air inlet 16, as in the previous embodiment. A central zone and an annular zone are thus formed, setting up a material flow pattern within the container similar to that of the previous embodiment.

4本の等角度に離隔させた垂直排出管36を容器内の一
地点からホツパ14の傾斜壁を貫通して外部へ延長させ
、粒状材料を第1〜3図の実施例の場合と同様に4つの
別個の外部部位へ排出するようにする。
Four equiangularly spaced vertical discharge pipes 36 are extended from one point within the vessel through the sloping wall of hopper 14 to the outside to discharge particulate material as in the embodiment of FIGS. Provides drainage to four separate external sites.

かくして、簡単な構造により粒状材料を1つまたはそれ
以上の供給源から複数の排出点へ正確に混合して分配す
ることができる。
Thus, a simple construction allows for precise mixing and distribution of particulate material from one or more sources to multiple discharge points.

以上、本発明の好ましい実施例を説明したが、本発明は
これに限定されるものではなく、本発明の精神および範
囲から逸脱することなく、いろいろに変更することがで
きる。
Although preferred embodiments of the present invention have been described above, the present invention is not limited thereto and can be modified in various ways without departing from the spirit and scope of the present invention.

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

第1図は本発明の材料混合分配装置の正面図、第2図は
第1図の線2−2に沿つてみた横断面図、第3図は第2
図の線3−3に沿つてみた縦断面図、第4図は本発明の
別の実施例の正面図、第5図は第4図の線5−5に沿つ
てみた横断面図である。
FIG. 1 is a front view of the material mixing and dispensing device of the present invention, FIG. 2 is a cross-sectional view taken along line 2--2 in FIG. 1, and FIG.
FIG. 4 is a front view of another embodiment of the invention, and FIG. 5 is a cross-sectional view taken along line 5--5 of FIG. .

Claims (1)

【特許請求の範囲】[Claims] 1 固形粒状材料を混合し分配するための装置において
、前記粒状材料の床を支持するための容器と、該床への
追加材料を受入れるために該容器に設けられた材料導入
手段と、加圧ガスを、該容器内の材料内を通して上昇さ
せるのに十分な速度で該容器の下方部分内へ導入させる
ためのガス導入手段と、該ガスを該容器から排出させる
ように該容器の上方部分に形成された開口と、前記材料
を前記床の複数の部位から排出させるために該容器の周
りに間隔を置いて設けられた複数の排出手段とから成る
混合分配装置。
1. A device for mixing and dispensing solid particulate materials, comprising a container for supporting a bed of said particulate material, material introduction means provided on said container for receiving additional material to said bed, and a pressurized gas introduction means for introducing gas into a lower portion of the container at a velocity sufficient to cause the gas to rise through the material within the container; A mixing and dispensing device comprising an aperture formed therein and a plurality of ejection means spaced around the container for ejecting the material from a plurality of parts of the bed.
JP56116535A 1980-09-03 1981-07-27 Equipment for mixing and dispensing solid granular materials Expired JPS5940499B2 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
GB08207898A GB2103326B (en) 1981-07-27 1982-03-18 Vehicle support structure for push-pull cables
DE19823211082 DE3211082A1 (en) 1981-07-27 1982-03-25 SUPPORT STRUCTURE FOR TRANSMISSION SHIFT CABLES
US06/623,640 US4541302A (en) 1981-07-27 1984-06-26 Support structure for power transmission cables

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US18378180A 1980-09-03 1980-09-03
US183781 2008-07-31

Publications (2)

Publication Number Publication Date
JPS57122927A JPS57122927A (en) 1982-07-31
JPS5940499B2 true JPS5940499B2 (en) 1984-10-01

Family

ID=22674254

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56116535A Expired JPS5940499B2 (en) 1980-09-03 1981-07-27 Equipment for mixing and dispensing solid granular materials

Country Status (2)

Country Link
JP (1) JPS5940499B2 (en)
GB (1) GB2082931B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61155599U (en) * 1984-11-27 1986-09-26

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60212217A (en) * 1984-04-03 1985-10-24 フオスタ−・ホイ−ラ−・エナ−ジイ・コ−ポレイシヨン Apparatus and method for mixing and distributing granular material
GB2242370B (en) * 1990-03-30 1993-11-03 Donovan Graham Ellam Pneumatic mixer
CN103123120A (en) * 2011-11-17 2013-05-29 王景龙 Air mixer used in biomass energy blended fuel ignition system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61155599U (en) * 1984-11-27 1986-09-26

Also Published As

Publication number Publication date
GB2082931B (en) 1984-07-25
GB2082931A (en) 1982-03-17
JPS57122927A (en) 1982-07-31

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