JP2900033B2 - Method for injecting a metered amount of powder material into a chamber under variable pressure by pneumatic means - Google Patents
Method for injecting a metered amount of powder material into a chamber under variable pressure by pneumatic meansInfo
- Publication number
- JP2900033B2 JP2900033B2 JP62304405A JP30440587A JP2900033B2 JP 2900033 B2 JP2900033 B2 JP 2900033B2 JP 62304405 A JP62304405 A JP 62304405A JP 30440587 A JP30440587 A JP 30440587A JP 2900033 B2 JP2900033 B2 JP 2900033B2
- Authority
- JP
- Japan
- Prior art keywords
- conduit
- mixture
- injecting
- flow
- pneumatic means
- 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
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B5/00—Making pig-iron in the blast furnace
- C21B5/001—Injecting additional fuel or reducing agents
- C21B5/003—Injection of pulverulent coal
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K3/00—Feeding or distributing of lump or pulverulent fuel to combustion apparatus
- F23K3/02—Pneumatic feeding arrangements, i.e. by air blast
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K3/00—Feeding or distributing of lump or pulverulent fuel to combustion apparatus
- F23K3/06—Feeding or distributing of lump or pulverulent fuel to combustion apparatus for shaft-type furnaces
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Furnace Charging Or Discharging (AREA)
- Blast Furnaces (AREA)
- Air Transport Of Granular Materials (AREA)
- Manufacture Of Iron (AREA)
- Nozzles (AREA)
Description
【発明の詳細な説明】
本発明は、計量された量の粉末材料を可変圧力下の室
へ種々の点において空気的手段により注入する方法であ
って、推進ガス中に大きい含有量の粉末材料を含む空気
混合物を単一の計量装置で形成し、共通の一次導管を通
じてこの混合物を分配ヘッドまで推進し、ここで混合物
は二次流に分割され、各二次流は二次導管に通されて注
入点の一つへ送られるようにした方法に関する。
本発明は好適な用途に関して詳述されるが、これに限
定されるものでなく、この好適用途は、固体可燃材料、
特に粉末石炭を高炉の如き工業炉へ注入することであ
る。
固体可燃材料を高炉へ注入する周知の方法および設備
は、主に2つの型に分類される。第1のものは比較的に
『希薄な』空気流で機能し、第2のものでは空気流は比
較的に高い濃度の粉末石炭を有する。
第1の型の設備では、希薄流を用い、粉末石炭は圧力
下に解放されて分配ホッパから一連の計量装置に入り、
ここで粉末石炭と推進ガスとの混合物が形成され、この
ように形成された混合物は高炉内の注入点へ運ばれる。
これらの設備において、一つの計量装置が一般に各パイ
プまたは1対のパイプに用いられ、その結果パイプを通
じて注入される量は個々に計量される。使用される計量
装置は周知の型のものであり、ヨーロッパ特許願第0,12
6,917号に提案された如きスロット付き装置またはアル
ビオラ(alveolar)ロータを持つ計量装置である。これ
らの設備は分配ホッパと高炉との間に多数の比較的に長
い導管を必要とするという欠点がある。また、特に炉内
圧力の変動の如き種々の可変パラメータにより計量が困
難になる。
高濃度の空気流を採用する第2の型の設備では、単一
の計量装置が分配ホッパに、またはその下流に使用され
る。この計量装置において、粉末石炭の全流れを調整し
て単位時間当たり所定の量の粉末石炭が注入されるよう
にする。これらの設備は冒頭に述べた方法、即ち必要量
の石炭を含有する計量された流れを分配ヘッド中で互い
に等しい二次流に分割する方法を採用する。これらの設
備には、分割ヘッドが炉の近傍に配置され、而して二次
導管の長さ、故にまた炉の回りの混雑が減少するという
利点がある。これらの設備には、二次導管または分配ヘ
ッドに絞り区分が設けられ、ここで空気流を音速まで加
速するのに必要な圧力降下が生じる。空気流を音速にま
で加速することにより、超臨界速度が生じる場所の上流
の流動状態はこの場所の下流の流動状態にもはや影響さ
れないという利点がある。勿論、これは粉末材料を注入
する室の内部の圧力および他の可変パラメータをもはや
考慮する必要がないという利点がある。第1の型の設備
と比較して、上記型の濃縮された流れで働く設備は各パ
イプの流れを個々に調整することはもはやできないとい
う欠点がある。
本発明の目的は2つの周知の方法の利点を兼備した、
冒頭に記載の型の新しい方法を提供することである。
この目的を達成するために、本発明は冒頭に記載の型
のものであって、空気流の流量を各二次導管内で調整す
ることを主として特徴とする方法を提供する。
調整は、好ましくは、超臨界速度への流れの加速が生
じる可変絞り区分で行われる。
調整は、各二次導管に設けた流量検出器の制御下に自
動的にまたは手動で行うことができる。
好適実施例を添付図面について説明する。この図は高
炉への可燃材料の空気的注入の回路を模式的に示す。粉
末石炭と推進ガスとから成り、その流量が高炉により必
要とされる単位時間当たりの石炭の量に対応する空気混
合物は、計量装置12の助けにより一次導管10において形
成され、またこの計量装置は可動スロットを有する型の
計量装置にでき、または空気計量または他の型のホッパ
にできる。この計量装置12において、高濃度の石炭を有
する空気混合物が形成され、これは、必要であれば、分
配器の上流の導管14を通じて注入される可変量の不活性
ガスの添加により希釈できる。この空気混合物はルクセ
ンブルグ特許第86,034号に推奨された型の分配ヘッド16
へ送られる。この分配ヘッド16において、一次空気流は
二次流に分割され、各流れは二次導管を通じて高炉(図
示せず)のパイプ22の一つへ送られる。二次導管18の数
は、例えば、パイプの数、またはパイプの数の半分に対
応する。
本発明によれば、各二次導管18に可変区分の絞り20が
設けられる。この絞り18は、好ましくは、ルクセンブル
グ特許願第86,311号に推奨された型の弁により構成さ
れ、この弁では固定ソケット内での可動ソケットの回転
により通路が形成され、2つのソケットには大きいまた
は小さい通路を与えるよう一部重畳できる開口およびス
ロットが設けられる。二次空気流の加速は好ましくは絞
り20で行われる。
而して本発明による方法は音速での注入のシステムの
総ての利点を有する。即ち、二次導管は炉の回りの混雑
を減少するためにできるだけ短くできる。更に、計量装
置12における計量状態は絞り20の下流の圧力の変動、特
に高炉内の圧力の変動により影響されない。
弁20は炉内の状態を考慮するために手動で調整でき
る。而して種々の二次導出を通る流量は、絞り20の開口
の関数として確立され、また単位時間に注入される石炭
の全量は計量装置12により決められる。
而して分配器16の機能はルクセンブルグ特許願第86,0
34号に提案された分配器の機能と異なる。しかし、後者
では、分配器は実際に分配の機能を有しており、これは
均一な分配であり、同じ石炭の流量が各二次導管を通
る。これと異なり、本発明による方法では、分配器16は
単に一次流を二次流に分割するのに投立ち、二次流の流
量は絞り20の可変断面の関数として変化する。
各二次導管18の石炭の流量を測定し、弁20の通路断面
を自動的に調整し、各パイプ22に規定の注入流量が存在
するようにできる。この自動調整により二次導管18また
は分配器16の通路の部分的閉塞の如き妨害因子を補償ま
たは除去できる。The present invention relates to a method for injecting a metered amount of powdered material into a chamber under variable pressure by means of pneumatic means at various points, wherein the powdered material having a high content in the propellant gas is Is formed in a single metering device and this mixture is propelled through a common primary conduit to a distribution head, where the mixture is split into secondary streams, each secondary stream being passed through a secondary conduit. To one of the injection points. The present invention will be described in detail with respect to preferred applications, but is not limited to such preferred applications, including solid combustible materials,
In particular, pouring coal into an industrial furnace, such as a blast furnace. Known methods and equipment for injecting solid combustible materials into a blast furnace fall into two main types. The first works with a relatively "lean" air stream, while in the second the air stream has a relatively high concentration of pulverized coal. In the first type of installation, using a dilute stream, the pulverized coal is released under pressure and enters a series of metering devices from a distribution hopper,
Here, a mixture of pulverized coal and propellant gas is formed, and the mixture thus formed is conveyed to an injection point in the blast furnace.
In these installations, one metering device is generally used for each pipe or pair of pipes, so that the amount injected through the pipes is individually metered. The weighing device used is of a known type and is described in European Patent Application 0,12.
A metering device with a slotted device or an alveolar rotor as proposed in US Pat. No. 6,917. These installations have the disadvantage of requiring a number of relatively long conduits between the distribution hopper and the blast furnace. Also, metering becomes difficult due to various variable parameters such as fluctuations in furnace pressure. In a second type of installation that employs a concentrated air flow, a single metering device is used in or downstream of the distribution hopper. In this metering device, the total flow of the powdered coal is adjusted so that a predetermined amount of the powdered coal is injected per unit time. These installations employ the method described at the outset, i.e., the division of a metered stream containing the required amount of coal into equal secondary streams in a distribution head. These arrangements have the advantage that the split head is located close to the furnace, thus reducing the length of the secondary conduit and thus also the congestion around the furnace. These installations are provided with a throttle section in the secondary conduit or distribution head, where the pressure drop required to accelerate the air flow to sonic speed is created. By accelerating the air flow to sonic speed, the advantage is that the flow conditions upstream of the location where the supercritical velocity occurs are no longer affected by the flow conditions downstream of this location. Of course, this has the advantage that the pressure inside the chamber into which the powder material is injected and other variable parameters no longer need to be taken into account. Compared to the first type of equipment, equipment working with concentrated streams of the above type has the disadvantage that the flow of each pipe can no longer be regulated individually. The object of the present invention combines the advantages of two known methods,
It is to provide a new method of the type described at the outset. To this end, the present invention provides a method of the type described at the outset, which is mainly characterized by regulating the flow rate of the air flow in each secondary conduit. The adjustment is preferably made in a variable throttle section where acceleration of the flow to supercritical speed occurs. Adjustments can be made automatically or manually under the control of a flow detector on each secondary conduit. The preferred embodiment will be described with reference to the accompanying drawings. This figure schematically shows a circuit for pneumatic injection of combustible material into a blast furnace. An air mixture consisting of powdered coal and a propellant gas, the flow of which corresponds to the amount of coal per unit time required by the blast furnace, is formed in the primary conduit 10 with the aid of a metering device 12, which is It can be a metering device of the type with movable slots, or it can be an air metering or other type of hopper. In this metering device 12, an air mixture with a high concentration of coal is formed, which can be diluted, if necessary, by the addition of a variable amount of inert gas injected through a conduit 14 upstream of the distributor. This air mixture is applied to a dispensing head 16 of the type recommended in Luxembourg patent 86,034.
Sent to In this distribution head 16, the primary air stream is split into secondary streams, each stream being sent through a secondary conduit to one of the pipes 22 of a blast furnace (not shown). The number of secondary conduits 18 corresponds, for example, to the number of pipes, or half of the number of pipes. According to the present invention, each secondary conduit 18 is provided with a variable section restriction 20. The throttle 18 is preferably constituted by a valve of the type recommended in Luxembourg patent application 86,311 in which a passage is formed by the rotation of a movable socket in a fixed socket, and a large or large Openings and slots are provided that can partially overlap to provide a small passage. Acceleration of the secondary air flow is preferably performed at the throttle 20. Thus, the method according to the invention has all the advantages of a system for injection at the speed of sound. That is, the secondary conduit can be made as short as possible to reduce congestion around the furnace. Furthermore, the metering conditions in the metering device 12 are not affected by fluctuations in the pressure downstream of the throttle 20, especially in the blast furnace. Valve 20 can be manually adjusted to take into account conditions in the furnace. Thus, the flow rate through the various secondary derivations is established as a function of the opening of the restrictor 20, and the total amount of coal injected per unit time is determined by the metering device 12. Thus, the function of the distributor 16 is described in Luxembourg patent application 86,0.
Differs from the function of the distributor proposed in No. 34. However, in the latter, the distributor actually has the function of distribution, which is a uniform distribution, with the same coal flow passing through each secondary conduit. In contrast, in the method according to the invention, the distributor 16 stands alone to split the primary stream into secondary streams, the flow rate of the secondary stream varying as a function of the variable cross section of the restriction 20. The coal flow rate in each secondary conduit 18 can be measured and the passage cross-section of the valve 20 can be automatically adjusted so that a defined injection flow rate is present in each pipe 22. This automatic adjustment can compensate or eliminate interfering factors such as partial blockage of the secondary conduit 18 or the passage of the distributor 16.
【図面の簡単な説明】
図は高炉への可燃材料の空気的注入の回路を模式的に示
す。
10……一次導管、12……計量装置、14……導管、16……
分配ヘッド、20……絞り、22……パイプ。BRIEF DESCRIPTION OF THE DRAWINGS The figure schematically shows a circuit for pneumatic injection of combustible material into a blast furnace. 10… Primary conduit, 12… Measuring device, 14… Conduit, 16…
Dispensing head, 20 ... throttle, 22 ... pipe.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 ハンス−クラウス・スコツト ドイツ連邦共和国デー4220、デインスラ ケン、ベートホーベンシユトラーセ 3 アー (56)参考文献 特開 昭60−97121(JP,A) 実開 昭61−157533(JP,U) (58)調査した分野(Int.Cl.6,DB名) B65G 53/56 B65G 53/66 ──────────────────────────────────────────────────続 き Continuation of the front page (72) Inventor Hans-Klaus-Scott, Germany Day 4220, Deinslaken, Beethoven Shuttle 3a (56) References JP-A-60-97121 (JP, A) Shokai 61-157533 (JP, U) (58) Fields investigated (Int. Cl. 6 , DB name) B65G 53/56 B65G 53/66
Claims (1)
点において空気的手段により注入する方法であって、推
進ガス中に比較的高い含有量の粉末材料を含む空気混合
物を単一の計量装置で形成し、共通の一次導管を通じて
この混合物を分配ヘッドまで推進し、ここで混合物は二
次流に分割され、各二次流は二次導管に通されて注入点
の一つへ送られ、各二次導管内の可変絞り区分を有する
絞りにより空気流の流量を各二次導管内で調整するよう
にした方法において可変絞り区分において空気流れを臨
界速度にまで加速することを特徴とする方法。 2.可変絞り区分の調整は手動で行われることを特徴と
する特許請求の範囲第1項記載の方法。 3.可変絞り区分の調整は各二次導管に設けた流量検出
器の制御下で自動的に行われることを特徴とする特許請
求の範囲第1項または第2項に記載の方法。(57) [Claims] A method of injecting a metered amount of powdered material into a chamber under variable pressure at various points by pneumatic means, wherein a single mixture of an air mixture containing a relatively high content of powdered material in the propellant gas is obtained. Formed in the apparatus, this mixture is propelled through a common primary conduit to a dispensing head, where the mixture is split into secondary streams, each secondary stream being passed through a secondary conduit to one of the injection points. Accelerating the air flow to a critical speed in the variable throttle section in a manner wherein the flow rate of the air flow is adjusted in each secondary pipe by a throttle having a variable throttle section in each secondary conduit. Method. 2. 2. The method according to claim 1, wherein the adjustment of the variable throttle section is performed manually. 3. 3. The method according to claim 1, wherein the adjustment of the variable throttle section is performed automatically under the control of a flow detector provided in each secondary conduit.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
LU86701A LU86701A1 (en) | 1986-12-04 | 1986-12-04 | PROCESS FOR THE INJECTION BY PNEUMATIC ROUTE OF QUANTITIES OF POWDERED MATERIALS INTO AN ENCLOSURE UNDER VARIABLE PRESSURE |
LU86701 | 1986-12-04 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS63147723A JPS63147723A (en) | 1988-06-20 |
JP2900033B2 true JP2900033B2 (en) | 1999-06-02 |
Family
ID=19730834
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP62304405A Expired - Lifetime JP2900033B2 (en) | 1986-12-04 | 1987-12-01 | Method for injecting a metered amount of powder material into a chamber under variable pressure by pneumatic means |
Country Status (7)
Country | Link |
---|---|
EP (1) | EP0270013A3 (en) |
JP (1) | JP2900033B2 (en) |
AU (1) | AU603162B2 (en) |
BR (1) | BR8706640A (en) |
CA (1) | CA1315991C (en) |
LU (1) | LU86701A1 (en) |
ZA (1) | ZA878817B (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3813357A1 (en) * | 1988-04-21 | 1989-11-02 | Krupp Koppers Gmbh | DEVICE FOR THE GASIFICATION OF FINE-GRAIN TO DUST-SHAPED FUELS |
LU87453A1 (en) * | 1989-02-14 | 1990-09-19 | Wurth Paul Sa | PROCESS FOR THE PNEUMATIC INJECTION OF QUANTITIES OF POWDERED MATERIALS INTO A VARIABLE PRESSURE ENCLOSURE |
LU90150B1 (en) * | 1997-10-15 | 1999-04-16 | Kuettner Gmbh & Co Kg Dr | Method and device for blowing reducing agent into a shaft furnace |
US8951315B2 (en) | 2008-11-12 | 2015-02-10 | Exxonmobil Research And Engineering Company | Method of injecting fuel into a gasifier via pressurization |
AT510896B1 (en) | 2009-01-15 | 2013-08-15 | Kurt Himmelfreundpointner | METHOD AND DEVICE FOR PROMOTING ELIGIBLE MATERIALS |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3109111A1 (en) * | 1981-03-11 | 1982-09-23 | Fried. Krupp Gmbh, 4300 Essen | "PLANT FOR INPUTING COAL IN METALLURGICAL PROCESSING VESSELS WITH A VARIETY OF INLAY POINTS AND METHOD FOR OPERATING THE PLANT" |
JPS5869620A (en) * | 1981-09-14 | 1983-04-25 | Nippon Steel Corp | Pneumatic pulverized coal distributor |
LU84780A1 (en) * | 1983-04-28 | 1984-11-28 | Wurth Paul Sa | DEVICE FOR INTRODUCING QUANTITIES OF POWDERY MATERIALS INTO A PNEUMATIC PROPULSION FLUID AND APPLICATION TO A POWDERY MATERIAL DELIVERY TANK |
FR2549580A1 (en) * | 1983-07-19 | 1985-01-25 | Wurth Paul Sa | METHOD AND DEVICE FOR THE INJECTION OF PULVERIZED CHARCOAL IN AN INDUSTRIAL FURNACE |
JPS6097121A (en) * | 1983-11-02 | 1985-05-30 | Sumitomo Metal Ind Ltd | Powder flow distribution control method |
LU86034A1 (en) * | 1985-08-05 | 1987-03-06 | Wurth Paul Sa | METHOD AND DEVICE FOR INJECTING, BY PNEUMATIC ROUTE, QUANTITIES OF POWDERED MATERIALS INTO A VARIABLE PRESSURE ENCLOSURE |
DE3603078C1 (en) * | 1986-02-01 | 1987-10-22 | Kuettner Gmbh & Co Kg Dr | Method and device for the metered introduction of fine-grained solids into an industrial furnace, in particular a blast furnace or cupola furnace |
LU86311A1 (en) * | 1986-02-19 |
-
1986
- 1986-12-04 LU LU86701A patent/LU86701A1/en unknown
-
1987
- 1987-11-24 ZA ZA878817A patent/ZA878817B/en unknown
- 1987-11-27 EP EP87117523A patent/EP0270013A3/en not_active Withdrawn
- 1987-11-27 CA CA000553028A patent/CA1315991C/en not_active Expired - Fee Related
- 1987-12-01 JP JP62304405A patent/JP2900033B2/en not_active Expired - Lifetime
- 1987-12-03 BR BR8706640A patent/BR8706640A/en not_active IP Right Cessation
- 1987-12-04 AU AU82088/87A patent/AU603162B2/en not_active Ceased
Also Published As
Publication number | Publication date |
---|---|
ZA878817B (en) | 1988-08-31 |
CA1315991C (en) | 1993-04-13 |
JPS63147723A (en) | 1988-06-20 |
AU603162B2 (en) | 1990-11-08 |
BR8706640A (en) | 1988-07-19 |
LU86701A1 (en) | 1988-07-14 |
AU8208887A (en) | 1988-06-09 |
EP0270013A2 (en) | 1988-06-08 |
EP0270013A3 (en) | 1989-04-26 |
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