[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

JP5397996B2 - Pulverized coal distribution and supply equipment - Google Patents

Pulverized coal distribution and supply equipment Download PDF

Info

Publication number
JP5397996B2
JP5397996B2 JP2009158936A JP2009158936A JP5397996B2 JP 5397996 B2 JP5397996 B2 JP 5397996B2 JP 2009158936 A JP2009158936 A JP 2009158936A JP 2009158936 A JP2009158936 A JP 2009158936A JP 5397996 B2 JP5397996 B2 JP 5397996B2
Authority
JP
Japan
Prior art keywords
flow rate
pulverized coal
distribution
distribution branch
absolute value
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 - Fee Related
Application number
JP2009158936A
Other languages
Japanese (ja)
Other versions
JP2011012323A (en
Inventor
典正 前川
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.)
Nippon Steel Engineering Co Ltd
Original Assignee
Nippon Steel and Sumikin Engineering Co Ltd
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 Nippon Steel and Sumikin Engineering Co Ltd filed Critical Nippon Steel and Sumikin Engineering Co Ltd
Priority to JP2009158936A priority Critical patent/JP5397996B2/en
Publication of JP2011012323A publication Critical patent/JP2011012323A/en
Application granted granted Critical
Publication of JP5397996B2 publication Critical patent/JP5397996B2/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Measuring Volume Flow (AREA)
  • Blast Furnaces (AREA)
  • Air Transport Of Granular Materials (AREA)
  • Manufacture Of Iron (AREA)

Description

本発明は、高炉の羽口から微粉炭を吹き込む際に、複数ある高炉の羽口に微粉炭を分配供給する微粉炭の分配供給設備に関する。   The present invention relates to a pulverized coal distribution and supply facility that distributes and supplies pulverized coal to a plurality of blast furnace tuyere when blowing pulverized coal from the blast furnace tuyere.

近年、高炉の羽口から微粉炭を吹き込む操業方法が広く採用されている(例えば特許文献1)。微粉炭はコークスの代替燃料としてコスト的にメリットが大きくかつ発熱量が良好なため、微粉炭の吹き込み量は増加する傾向にある。   In recent years, an operation method in which pulverized coal is blown from the tuyere of a blast furnace has been widely adopted (for example, Patent Document 1). Since pulverized coal has great cost advantages and good calorific value as an alternative fuel for coke, the amount of pulverized coal injected tends to increase.

高炉には多数、例えば16〜42個の羽口が配置されており、各羽口から、系外から搬送されてきた微粉炭が吹き込まれるが、各羽口からの微粉炭の吹き込み量が均一にならないと、高炉内での均一な精錬反応が起こらず、生産性の低下要因となる。したがって、微粉炭の吹き込みにおいては、各羽口からの微粉炭の吹き込み量を均一にすることが重要な課題であり、この課題を解決するために従来から種々の研究・改良が図られている。   A large number, for example, 16 to 42 tuyere are arranged in the blast furnace, and pulverized coal transported from outside the system is blown from each tuyere, but the amount of pulverized coal blown from each tuyere is uniform. Otherwise, a uniform refining reaction will not occur in the blast furnace, leading to a decrease in productivity. Therefore, in pulverized coal blowing, it is an important issue to make the amount of pulverized coal blown from each tuyere uniform, and various studies and improvements have been made in the past to solve this problem. .

その一例を図6を参照して説明する。図6において、微粉炭は、供給タンク1から図示しない気体圧送装置により供給管2を介して分配器3に圧送される。分配器3は、その下部の受入部3aから微粉炭を受け入れ、その側面の分配支管3bから微粉炭を排出する。分配支管3bの先端には吹き込みノズル4が設けられており、この吹き込みノズル4の先端から微粉炭が吹き込まれる。吹き込みノズル4の先端は、熱風環状管5から分岐した送風支管5a内に位置しており、微粉炭は送風支管5aから供給される熱風と共に、高炉6の下部に配置した羽口6aから高炉6内に吹き込まれる。   One example will be described with reference to FIG. In FIG. 6, pulverized coal is pumped from the supply tank 1 to the distributor 3 via the supply pipe 2 by a gas pumping device (not shown). The distributor 3 receives the pulverized coal from the lower receiving portion 3a and discharges the pulverized coal from the distribution branch 3b on the side surface thereof. A blowing nozzle 4 is provided at the tip of the distribution branch pipe 3 b, and pulverized coal is blown from the tip of the blowing nozzle 4. The tip of the blowing nozzle 4 is located in the blower branch pipe 5a branched from the hot air annular pipe 5, and the pulverized coal together with the hot air supplied from the blower branch pipe 5a, from the tuyere 6a disposed at the lower part of the blast furnace 6 to the blast furnace 6 Be blown into.

上述のとおり高炉には多数、例えば16〜42個の羽口が配置されており、分配支管3b、吹き込みノズル4及び送風支管5aは各羽口に対応させて羽口の数と同数設けられる。つまり、分配器3は、複数の分配支管3bを介して高炉の複数の羽口6に微粉炭を供給する。   As described above, many, for example, 16 to 42 tuyere are arranged in the blast furnace, and the distribution branch pipe 3b, the blowing nozzle 4 and the blower branch pipe 5a are provided in the same number as the tuyere corresponding to each tuyere. That is, the distributor 3 supplies pulverized coal to the plurality of tuyere 6 of the blast furnace through the plurality of distribution branch pipes 3b.

ここで、分配器3から吹き込みノズル4までの分配支管3bは、例えば、高炉6及び分配器3が配置されている当該設備のレイアウト、周囲の関連設備の設置状況等により、その長さ、形状(直線・曲線)が相違し、それぞれの分配支管3aにおける圧力損失が相違するため流量が一定ではない。   Here, the distribution branch pipe 3b from the distributor 3 to the blowing nozzle 4 has its length and shape depending on, for example, the layout of the equipment in which the blast furnace 6 and the distributor 3 are arranged, the installation status of surrounding related equipment, and the like. The flow rate is not constant because the (straight line / curve) is different and the pressure loss in each distribution branch pipe 3a is different.

このため図6の例では、複数の分配支管3bのそれぞれに粉体流量測定手段7及び粉体流量調整手段8を設け、粉体流量測定手段7によってそれぞれの分配支管3bにおける微粉炭流量の絶対値を把握し、粉体流量調整手段8によってそれぞれの分配支管3bにおける微粉炭流量を均一になるように調整している。   For this reason, in the example of FIG. 6, the powder flow rate measuring means 7 and the powder flow rate adjusting means 8 are provided in each of the plurality of distribution branch pipes 3b, and the absolute flow rate of pulverized coal in each distribution branch pipe 3b is measured by the powder flow rate measurement means 7. The value is grasped, and the pulverized coal flow rate in each distribution branch pipe 3b is adjusted by the powder flow rate adjusting means 8 to be uniform.

粉体流量測定手段7としては、微粉炭流量の絶対値を把握する必要があることから、従来から測定精度が高いものが使用されている。高精度の粉体流量測定手段としては、特許文献2に開示されているような透過及び位相差型のマイクロ波式の粉体流量測定装置が知られている。このほか、静電容量式の粉体流量測定装置が知られている。   As the powder flow rate measuring means 7, since it is necessary to know the absolute value of the pulverized coal flow rate, one having a high measurement accuracy has been conventionally used. As a highly accurate powder flow rate measuring means, a transmission and phase difference type microwave powder flow rate measuring device as disclosed in Patent Document 2 is known. In addition, a capacitance-type powder flow measuring device is known.

一方、粉体流量調整手段8としては、一般的な粉体流量調整バルブのほか、特許文献3に開示されているような分配支管進退手段が知られている。図6の例は分配支管進退手段を適用したものである。この分配支管進退手段は分配器3内部に分配支管3bの端部を中心方向に進退させ、分配支管3bの吸い込み点を中心方向に変えることで、その分配支管3bの固気濃度を調整し、粉体流量を調整するものである。   On the other hand, as the powder flow rate adjusting means 8, in addition to a general powder flow rate adjusting valve, a distribution branch advance / retreat means as disclosed in Patent Document 3 is known. The example of FIG. 6 is an application of distribution branch advance / retreat means. This distribution branch advancement / retraction means adjusts the solid gas concentration of the distribution branch 3b by moving the end of the distribution branch 3b in the distributor 3 in the central direction and changing the suction point of the distribution branch 3b in the central direction. It adjusts the powder flow rate.

ここで、従来、粉体流量測定手段7として使用されている透過及び位相差型のマイクロ波式、あるいは静電容量式の粉体流量測定装置はいずれも高価な計器である。したがって、従来の微粉炭の分配供給設備においては図6で説明したようにすべての分配支管3bに粉体流量測定手段7を設けるようにしていることから、設備コストが多大になるという問題があった。   Here, the transmission and phase difference type microwave type or electrostatic capacitance type powder flow rate measuring devices conventionally used as the powder flow rate measuring means 7 are all expensive instruments. Therefore, in the conventional pulverized coal distribution and supply equipment, as described with reference to FIG. 6, since the powder flow rate measuring means 7 is provided in all the distribution branch pipes 3b, there is a problem that the equipment cost increases. It was.

特開2004−27265号公報JP 2004-27265 A 特開2000−146646号公報JP 2000-146646 A 特開平3−26609号公報JP-A-3-26609

本発明が解決しようとする課題は、高炉の羽口への微粉炭の分配供給設備において、微粉炭の流量測定及び流量調整の機能を維持しつつ、そのコストを低減することにある。   The problem to be solved by the present invention is to reduce the cost while maintaining the functions of flow rate measurement and flow rate adjustment of pulverized coal in the distribution and supply facility of pulverized coal to the tuyere of the blast furnace.

本発明は、微粉炭を受け入れる受入部と複数の分配支管とを有する分配器を備え、前記複数の分配支管を介して高炉の複数の羽口に微粉炭を供給する微粉炭の分配供給設備において、前記複数の分配支管の少なくとも一つに、基準となる微粉炭流量の絶対値測定手段を設け、前記複数の分配支管の全数に、微粉炭流量の大小のみを検知する簡易測定手段と、微粉炭の流量を調整する流量調整手段とを設け、前記絶対値測定手段による微粉炭流量の測定値が、前記分配器から供給される微粉炭の総量を分配支管の全本数で割ることにより算出された目標値となるように、当該分配支管に設けた前記流量調整手段によって微粉炭流量を調整するとともに、前記複数の分配支管の全数に設けた簡易測定手段によって検知した測定値を比較手段により比較し、前記絶対値測定手段を設けた分配支管の前記簡易測定手段による測定値を目標値として、各分配支管に設けた前記簡易測定手段による測定値が全て同一となるように、前記流量調整手段によって微粉炭流量を調整するようにしたことを特徴とする。 The present invention relates to a pulverized coal distribution and supply facility that includes a distributor having a receiving portion that receives pulverized coal and a plurality of distribution branches, and supplies the pulverized coal to a plurality of tuyere of a blast furnace through the plurality of distribution branches. The at least one of the plurality of distribution branch pipes is provided with an absolute value measurement means for a pulverized coal flow rate serving as a reference, and the simple measurement means for detecting only the magnitude of the pulverized coal flow rate in the total number of the plurality of distribution branch pipes, A flow rate adjusting means for adjusting the flow rate of charcoal, and the measured value of the pulverized coal flow rate by the absolute value measuring means is calculated by dividing the total amount of pulverized coal supplied from the distributor by the total number of distribution branches. was such that the target value, with adjusting the pulverized coal flow rate by the flow rate adjusting means provided in the distribution branch pipe, by comparison means the measurement value detected by a simple measuring means provided on the total number of the plurality of distribution branch pipes And compare the absolute value target value measurements by the simple measurement means distributed branch pipes provided with measuring means, so that the measured value by the simple measuring means provided in each distribution branch pipe is all the same, the flow rate adjustment The pulverized coal flow rate is adjusted by means .

本発明では、基準となる微粉炭流量を測定する絶対値測定手段を複数の分配支管の少なくとも一つに設け、分配支管の全数に微粉炭流量の大小のみを検知する簡易測定手段を設け、それぞれの分配支管における微粉炭流量を比較し流量調整手段によって調整することで、それぞれの分配支管における微粉炭流量が均一になるように調整できる。また、絶対値測定手段によって基準となる微粉炭流量を測定するから、それぞれの分配支管における微粉炭流量の絶対値も把握し調整できる。   In the present invention, the absolute value measuring means for measuring the reference pulverized coal flow rate is provided in at least one of the plurality of distribution branch pipes, the simple measurement means for detecting only the magnitude of the pulverized coal flow rate is provided in the total number of distribution branch pipes, By comparing the pulverized coal flow rates in the distribution branch pipes and adjusting the flow rate by the flow rate adjusting means, the pulverized coal flow rates in the respective distribution branch pipes can be adjusted to be uniform. Moreover, since the pulverized coal flow rate serving as a reference is measured by the absolute value measuring means, the absolute value of the pulverized coal flow rate in each distribution branch can be grasped and adjusted.

このように本発明によれば、微粉炭流量の絶対値を把握するために高い測定精度が求められる絶対値測定手段を少なくとも一つの分配支管に設けるだけで、測定精度の高い流量測定手段をすべての分配支管に設けていた従来の設備と同様の微粉炭の流量測定及び流量調整の機能を発揮できる。   As described above, according to the present invention, all the flow measurement means with high measurement accuracy can be obtained only by providing at least one distribution branch with absolute value measurement means that requires high measurement accuracy in order to grasp the absolute value of the pulverized coal flow rate. The function of flow rate measurement and flow rate adjustment of pulverized coal similar to the conventional equipment provided in the distribution branch pipe can be exhibited.

そして、高価な絶対値測定手段は少なくとも一つの分配支管に設けるだけで、あとは微粉炭流量の大小のみを検知する安価な簡易測定手段、及び同様に安価な比較手段を設ければよいので、設備コストを低減できる。   And, it is only necessary to provide an expensive absolute value measuring means in at least one distribution branch, and then provide an inexpensive simple measuring means for detecting only the magnitude of the pulverized coal flow rate, and similarly an inexpensive comparing means. Equipment costs can be reduced.

本発明に係る微粉炭の分配供給設備の一実施例を示す。An example of the distribution supply equipment of pulverized coal concerning the present invention is shown. 分配支管の配置例を示す。An arrangement example of distribution branch pipes will be shown. 流量調整手段の一例を示す。An example of the flow rate adjusting means is shown. 流量調整手段の他の例を示す。The other example of a flow volume adjustment means is shown. 比較手段による比較表示例を示す。The example of a comparison display by a comparison means is shown. 従来の微粉炭の分配供給設備を示す。A conventional pulverized coal distribution and supply facility is shown.

以下、図面に示す実施例に基づき本発明の実施の形態を説明する。   Embodiments of the present invention will be described below based on examples shown in the drawings.

図1は本発明に係る微粉炭の分配供給設備の一実施例を示す。図1において、微粉炭は、供給タンク1から図示しない気体圧送装置により供給管2を介して分配器3に圧送される。分配器3は、その下部の受入部3aから微粉炭を受け入れ、その側面の分配支管3bから微粉炭を排出する。分配支管3bの先端部分の構成は図6と同様である。すなわち、分配支管3bの先端には吹き込みノズル4が設けられており、この吹き込みノズル4の先端から微粉炭が吹き込まれる。吹き込みノズル4の先端は、熱風環状管5から分岐した送風支管5a内に位置しており、微粉炭は送風支管5aから供給される熱風と共に、高炉6の下部に配置した羽口6aから高炉6内に吹き込まれる。   FIG. 1 shows an embodiment of a pulverized coal distribution and supply facility according to the present invention. In FIG. 1, pulverized coal is pumped from a supply tank 1 to a distributor 3 through a supply pipe 2 by a gas pumping device (not shown). The distributor 3 receives the pulverized coal from the lower receiving portion 3a and discharges the pulverized coal from the distribution branch 3b on the side surface thereof. The configuration of the distal end portion of the distribution branch pipe 3b is the same as that shown in FIG. That is, a blowing nozzle 4 is provided at the tip of the distribution branch pipe 3 b, and pulverized coal is blown from the tip of the blowing nozzle 4. The tip of the blowing nozzle 4 is located in the blower branch pipe 5a branched from the hot air annular pipe 5, and the pulverized coal together with the hot air supplied from the blower branch pipe 5a, from the tuyere 6a disposed at the lower part of the blast furnace 6 to the blast furnace 6 Be blown into.

高炉には多数、例えば16〜42個の羽口が配置されており、分配支管3bは各羽口に対応させて羽口の数と同数設けられる。つまり、分配器3は、複数の分配支管3bを介して高炉の複数の羽口に微粉炭を供給する。分配支管3bは図2に示すように、分配器3の本体部分から例えば放射状に延びるように設けられる(図2は分配支管3bを16本設けた例を示す。)。   A large number, for example, 16 to 42 tuyere are arranged in the blast furnace, and the distribution branch pipes 3b are provided in the same number as the tuyere corresponding to each tuyere. That is, the distributor 3 supplies pulverized coal to the plurality of tuyere of the blast furnace through the plurality of distribution branch pipes 3b. As shown in FIG. 2, the distribution branch pipe 3b is provided so as to extend radially from the main body portion of the distributor 3, for example (FIG. 2 shows an example in which 16 distribution branch pipes 3b are provided).

再度図1を参照すると、複数の分配支管3bの少なくとも一つに、基準となる微粉炭流量を測定する微粉炭流量の絶対値測定手段9が設けられている。また、複数の分配支管3bの全数に、微粉炭流量の大小のみを検知できる簡易測定手段10と、微粉炭の流量を調整する流量調整手段11とが設けられている。さらに、複数の分配支管3bのそれぞれに設けた簡易測定手段10によって検知した測定値を相互に比較する比較手段12が設けられている。   Referring to FIG. 1 again, at least one of the plurality of distribution branch pipes 3b is provided with a pulverized coal flow rate absolute value measuring means 9 for measuring a pulverized coal flow rate serving as a reference. Moreover, the simple measuring means 10 which can detect only the magnitude of the pulverized coal flow rate, and the flow rate adjusting means 11 for adjusting the pulverized coal flow rate are provided in the total number of the plurality of distribution branch pipes 3b. Further, a comparison means 12 for comparing the measurement values detected by the simple measurement means 10 provided in each of the plurality of distribution branch pipes 3b is provided.

絶対値測定手段9としては、分配支管3bにおける微粉炭流量の絶対値を把握する必要があることから、測定精度の高いものを使用する。具体的には、特許文献2に開示されているような透過及び位相差型のマイクロ波式の粉体流量測定装置、又は静電容量式の粉体流量測定装置が適当である。   As the absolute value measuring means 9, since it is necessary to grasp the absolute value of the pulverized coal flow rate in the distribution branch pipe 3b, one having high measurement accuracy is used. Specifically, a transmission and phase difference type microwave powder flow rate measuring device or a capacitance type powder flow rate measuring device as disclosed in Patent Document 2 is suitable.

透過及び位相差型のマイクロ波式の粉体流量測定装置は、粉体搬送管に沿って設置した2ヶ所の検出部にて粉体にマイクロ波を作用させた際の当該マイクロ波の位相変化量と粉体重量嵩密度との関係係数を予め設定し、この関係係数、粉体の流通速度、粉体の流路の断面積及びマイクロ波の位相変化量に基づいて粉体の流量を測定する粉体流量測定装置であって、測定対象である粉体の重量嵩密度とこの粉体に作用させたマイクロ波の位相変化量とを実測して前記関係係数を設定する関係係数設定手段を設けているものである。   Transmission and phase difference type microwave powder flow rate measuring device is the phase change of the microwave when the microwave is applied to the powder at two detection parts installed along the powder transfer tube. The flow rate of powder is measured based on the relationship coefficient, the flow rate of the powder, the cross-sectional area of the flow path of the powder, and the amount of phase change of the microwave. A flow rate measuring device for measuring the relationship between the weight bulk density of the powder to be measured and the phase change amount of the microwave applied to the powder, and setting the relationship coefficient It is provided.

静電容量式の粉体流量測定装置は、粉体搬送管に沿って設置した2ヶ所の検出部にて静電容量を測定し、粉体密度及び測定波形の検出部管の移動速度から粉体流量を測定するものである。   Capacitance-type powder flow rate measurement equipment measures the capacitance at two detectors installed along the powder transfer tube, and determines the powder density and the measurement waveform from the moving speed of the detector tube. It measures body flow.

なお、本発明の微粉炭の分配供給設備における絶対値測定手段の設置数量は、当該設備においていずれか1本の分配支管に1個あれば良いが、使用による故障等を考慮すると、さらに1〜2本の他の分配支管にそれぞれ設置してもよい。   In addition, the installation quantity of the absolute value measuring means in the pulverized coal distribution and supply facility of the present invention may be one in any one distribution branch in the facility, but further considering the failure due to use, etc. You may install in two other distribution branches, respectively.

一方、簡易測定手段10としては、絶対値測定手段9によって測定される基準となる微粉炭流量と対応する相対的な微粉炭流量を測定できれば良く。微粉炭流量の絶対値を精度良く測定する必要はないので、簡易的で安価な粉体流量測定装置を使用できる。具体的には、ドップラー型のマイクロ波式の粉体流量測定装置を使用できる。   On the other hand, the simple measuring means 10 only needs to be able to measure the relative pulverized coal flow rate corresponding to the reference pulverized coal flow rate measured by the absolute value measuring means 9. Since it is not necessary to accurately measure the absolute value of the pulverized coal flow rate, a simple and inexpensive powder flow rate measuring device can be used. Specifically, a Doppler microwave powder flow rate measuring device can be used.

ドップラー型のマイクロ波式の粉体流量測定装置は、粉体搬送管に設置した1ヶ所の検出部にてμ波ドップラー効果を利用し、流体粒子によって反射された周波数及び振幅の計測値から粉体流量を測定するものである。   The Doppler-type microwave powder flow rate measurement device uses the μ-wave Doppler effect at one detection unit installed in the powder transport tube, and uses the frequency and amplitude measurement values reflected by the fluid particles to measure the powder. It measures body flow.

図3は、図1の実施例で採用した流量調整手段11を示す。この流量調整手段11は、分配器3内部に分配支管3bの端部を中心方向に進退させる分配支管進退手段からなる。すなわち、この分配支管進退手段は分配器3内部に分配支管3bの端部を中心方向に進退させ、分配支管3bの吸い込み点を中心方向に変えることで、その分配支管3bの固気濃度を調整し、粉体流量を調整する。分配支管3bの端部を中心方向に進退させる機構としては、手動ジャッキ等を使用して分配支管3bを伸縮させるようにすることができる。   FIG. 3 shows the flow rate adjusting means 11 employed in the embodiment of FIG. The flow rate adjusting means 11 includes distribution branch pipe advance / retreat means for moving the end of the distribution branch pipe 3b in the distributor 3 in the central direction. That is, the distribution branch advance / retreat means adjusts the solid gas concentration of the distribution branch 3b by moving the end of the distribution branch 3b in the distributor 3 in the central direction and changing the suction point of the distribution branch 3b in the central direction. And adjust the powder flow rate. As a mechanism for moving the end portion of the distribution branch pipe 3b back and forth in the center direction, the distribution branch pipe 3b can be expanded and contracted using a manual jack or the like.

なお、流量調整手段としては、上述の分配支管進退手段を設けるほか、図4に示すように一般的な粉体流量調整バルブ11aを設けることもできる。   As the flow rate adjusting means, a general powder flow rate adjusting valve 11a can be provided as shown in FIG.

比較手段12は、それぞれの分配支管3bに設けた簡易測定手段10によって検知した測定値を相互に比較する。実施例では、図5に示すようにそれぞれの分配支管3bに設けた簡易測定手段10によって検知した微粉炭流量の大小のみの測定値をレーダーチャートとして表示し、比較するようにしている。ここで、図5中のAの測定値は、絶対値測定手段9を設けた分配支管3bにおける簡易測定手段10による測定値である。このAの微粉炭流量は、絶対値測定手段9によって正確な絶対値が把握されており、当該分配支管3bに設けられた流量調整手段11によって所望の流量に調整されている。その他の分配支管3bについては、図5のような比較表示結果に基づき、当該分配支管3bにおける簡易測定手段10により検知された測定値が基準となるAの値になるように流量調整手段11によって調整する。そうすると、すべての分配支管3bにおける微粉炭流量が揃って均一となり、しかもその絶対値も所望の流量になる。   The comparison means 12 compares the measured values detected by the simple measurement means 10 provided in each distribution branch pipe 3b with each other. In the embodiment, as shown in FIG. 5, only measured values of the pulverized coal flow rate detected by the simple measuring means 10 provided in each distribution branch pipe 3b are displayed as a radar chart for comparison. Here, the measured value A in FIG. 5 is a measured value by the simple measuring means 10 in the distribution branch pipe 3 b provided with the absolute value measuring means 9. An accurate absolute value of the pulverized coal flow rate of A is grasped by the absolute value measuring means 9, and is adjusted to a desired flow rate by the flow rate adjusting means 11 provided in the distribution branch pipe 3b. For the other distribution branch 3b, based on the comparison display result as shown in FIG. 5, the flow rate adjustment unit 11 adjusts the measurement value detected by the simple measurement unit 10 in the distribution branch 3b to the reference value A. adjust. If it does so, the pulverized coal flow rate in all the distribution branch pipes 3b will become uniform, and the absolute value will also become a desired flow rate.

すなわち、本発明に係る微粉炭の分配供給設備では以下の工程1〜3により、微粉炭の分配供給を行う。
工程1:絶対値測定手段9を設けた分配支管3bにおいて、絶対値測定手段9によって測定した微粉炭流量の絶対値が所望の流量となるように、当該分配支管3bに設けた流量調整手段11によって微粉炭流量を調整する。
工程2:それぞれの分配支管3bに設けた簡易測定手段10によって、微粉炭流量の大小のみを検知・測定し、比較手段12によって比較する。
工程3:比較手段12による比較結果に基づき、絶対値測定手段9を設けていない分配支管3bにおける簡易測定手段10による大小の測定値が、絶対値測定手段9を設けた分配支管3bにおける簡易測定手段10による大小の測定値と同一になるように、それぞれの分配支管3bに設けた流量調整手段11によって微粉炭流量を調整する。
That is, in the pulverized coal distribution and supply facility according to the present invention, the pulverized coal is distributed and supplied by the following steps 1 to 3.
Step 1: In the distribution branch pipe 3b provided with the absolute value measurement means 9, the flow rate adjustment means 11 provided in the distribution branch pipe 3b so that the absolute value of the pulverized coal flow rate measured by the absolute value measurement means 9 becomes a desired flow rate. To adjust the pulverized coal flow rate.
Step 2: Only the magnitude of the pulverized coal flow rate is detected and measured by the simple measuring means 10 provided in each distribution branch pipe 3b, and compared by the comparing means 12.
Step 3: Based on the comparison result by the comparison means 12, the large and small measured values by the simple measuring means 10 in the distribution branch 3b not provided with the absolute value measuring means 9 are simplified measurements in the distribution branch 3b provided with the absolute value measuring means 9. The pulverized coal flow rate is adjusted by the flow rate adjusting means 11 provided in each distribution branch pipe 3b so as to be the same as the magnitude measured by the means 10.

本発明に係る微粉炭の分配供給設備では上記工程1〜3による分配供給方法を行うことで、それぞれの分配支管3bにおける微粉炭流量を±5%の精度で均一に調整することができた。   In the pulverized coal distribution and supply facility according to the present invention, the pulverized coal flow rate in each of the distribution branch pipes 3b can be uniformly adjusted with an accuracy of ± 5% by performing the distribution and supply method according to the above steps 1 to 3.

1 供給タンク
2 供給管
3 分配器
3a 受入部
3b 分配支管
4 吹き込みノズル
5 熱風環状管
5a 送風支管
6 高炉
6a 羽口
7 粉体流量測定手段
8 粉体流量調整手段
9 絶対値測定手段
10 簡易測定手段
11 流量調整手段(分配支管進退手段)
11a 粉体流量調整バルブ(流量調整手段)
12 比較手段
DESCRIPTION OF SYMBOLS 1 Supply tank 2 Supply pipe 3 Distributor 3a Receiving part 3b Distribution branch 4 Blowing nozzle 5 Hot-air annular pipe 5a Blower branch 6 Blast furnace 6a Tuyere 7 Powder flow rate measurement means 8 Powder flow rate adjustment means 9 Absolute value measurement means 10 Simple measurement Means 11 Flow rate adjusting means (distribution branch pipe advance / retreat means)
11a Powder flow rate adjusting valve (flow rate adjusting means)
12 Comparison means

Claims (3)

微粉炭を受け入れる受入部と複数の分配支管とを有する分配器を備え、前記複数の分配支管を介して高炉の複数の羽口に微粉炭を供給する微粉炭の分配供給設備において、
前記複数の分配支管の少なくとも一つに、基準となる微粉炭流量の絶対値測定手段を設け、
前記複数の分配支管の全数に、微粉炭流量の大小のみを検知する簡易測定手段と、微粉炭の流量を調整する流量調整手段とを設け、
前記絶対値測定手段による微粉炭流量の測定値が、前記分配器から供給される微粉炭の総量を分配支管の全本数で割ることにより算出された目標値となるように、当該分配支管に設けた前記流量調整手段によって微粉炭流量を調整するとともに、前記複数の分配支管の全数に設けた簡易測定手段によって検知した測定値を比較手段により比較し、前記絶対値測定手段を設けた分配支管の前記簡易測定手段による測定値を目標値として、各分配支管に設けた前記簡易測定手段による測定値が全て同一となるように、前記流量調整手段によって微粉炭流量を調整するようにしたことを特徴とする微粉炭の分配供給設備。
In a distribution facility for pulverized coal, comprising a distributor having a receiving part for receiving pulverized coal and a plurality of distribution branches, and supplying pulverized coal to a plurality of tuyere of a blast furnace through the plurality of distribution branches,
At least one of the plurality of distribution branch pipes is provided with an absolute value measuring means for a pulverized coal flow rate serving as a reference,
A simple measuring means for detecting only the magnitude of the pulverized coal flow rate and a flow rate adjusting means for adjusting the pulverized coal flow rate are provided in the total number of the plurality of distribution branch pipes,
Provided in the distribution branch so that the measured value of the pulverized coal flow rate by the absolute value measuring means becomes a target value calculated by dividing the total amount of pulverized coal supplied from the distributor by the total number of distribution branches. In addition to adjusting the pulverized coal flow rate by the flow rate adjusting means, the measured values detected by the simple measuring means provided in the total number of the plurality of distribution branch pipes are compared by the comparison means, and the distribution branch pipe provided with the absolute value measurement means The flow rate adjustment means adjusts the pulverized coal flow rate so that the measurement values by the simple measurement means provided in each distribution branch are all the same, with the measurement value by the simple measurement means as a target value. A pulverized coal distribution and supply facility.
前記絶対値測定手段として、透過及び位相差型のマイクロ波式、又は静電容量式の粉体流量測定装置を設け、
前記簡易測定手段として、ドップラー型のマイクロ波式の粉体流量測定装置を設けた請求項1に記載の微粉炭の分配供給設備。
As the absolute value measuring means, a transmission and phase difference type microwave type, or a capacitance type powder flow rate measuring device is provided,
The distribution supply equipment for pulverized coal according to claim 1, wherein a Doppler type microwave powder flow rate measuring device is provided as the simple measuring means.
前記流量調整手段として、粉体流量調整バルブ、又は前記分配器内部に前記分配支管の端部を中心方向に進退させる分配支管進退手段を設けた請求項1又は2に記載の微粉炭の分配供給設備。   The distribution supply of pulverized coal according to claim 1 or 2, wherein the flow rate adjusting means is provided with a powder flow rate adjusting valve or a distribution branch pipe advance / retreat means for moving the end of the distribution branch pipe in the center direction inside the distributor. Facility.
JP2009158936A 2009-07-03 2009-07-03 Pulverized coal distribution and supply equipment Expired - Fee Related JP5397996B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2009158936A JP5397996B2 (en) 2009-07-03 2009-07-03 Pulverized coal distribution and supply equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2009158936A JP5397996B2 (en) 2009-07-03 2009-07-03 Pulverized coal distribution and supply equipment

Publications (2)

Publication Number Publication Date
JP2011012323A JP2011012323A (en) 2011-01-20
JP5397996B2 true JP5397996B2 (en) 2014-01-22

Family

ID=43591505

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2009158936A Expired - Fee Related JP5397996B2 (en) 2009-07-03 2009-07-03 Pulverized coal distribution and supply equipment

Country Status (1)

Country Link
JP (1) JP5397996B2 (en)

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6031438A (en) * 1983-08-01 1985-02-18 Denka Consult & Eng Co Ltd High accurate exhausting device for pulverized or granular objects
JPS6144778A (en) * 1984-08-03 1986-03-04 株式会社デンソー Manufacture of porous ceramic body
JPS6341808A (en) * 1986-08-07 1988-02-23 Furukawa Electric Co Ltd:The Terminal part for optical fiber
JPH01230706A (en) * 1988-03-09 1989-09-14 Sumitomo Metal Ind Ltd Method for blowing powdered coal into blast furnace
JP3083593B2 (en) * 1991-07-16 2000-09-04 ダイヤモンドエンジニアリング株式会社 Pulverized coal emission control device
JP4799904B2 (en) * 2005-05-19 2011-10-26 新日本製鐵株式会社 Pneumatic pulverized coal distribution method
JP2007031040A (en) * 2005-07-25 2007-02-08 Nippon Steel Corp Flow rate control device for distribution of coal particulates
JP4855002B2 (en) * 2005-07-25 2012-01-18 新日本製鐵株式会社 Blast furnace operation method with pulverized coal injection

Also Published As

Publication number Publication date
JP2011012323A (en) 2011-01-20

Similar Documents

Publication Publication Date Title
JP5397997B2 (en) How to distribute and supply pulverized coal
US8225677B2 (en) Capacitive sensor, system, and method for measuring parameters of a two-phase flow
US6868741B2 (en) Device and method enabling fluid characteristic measurement utilizing fluid acceleration
CA2040944C (en) Method and apparatus for the combined use of dual density measurements to achieve a fast and accurate density measurement in pneumatically transported solids
Park et al. The evaluation of critical pressure ratios of sonic nozzles at low Reynolds numbers
CN101477074A (en) Two-phase flow parameter monitoring method and system
JPH05209219A (en) Equipment and method for shot peening
JP2009524058A (en) A reduced-bore vortex flowmeter with a stepped inlet.
Coombes et al. Experimental investigations into the flow characteristics of pneumatically conveyed biomass particles using an electrostatic sensor array
Lu et al. Design optimization of a venturi tube geometry in dense-phase pneumatic conveying of pulverized coal for entrained-flow gasification
KR102017769B1 (en) Boiler steam amount measuring method, boiler load analyzing method, boiler steam amount measuring apparatus, and boiler load analyzing apparatus
JP5397996B2 (en) Pulverized coal distribution and supply equipment
CN104406646A (en) Measurement device of pulverized coal mass flow meter
US20100316964A1 (en) Solids flow meter for integrated boiler control system
CN202471144U (en) High-precision wide-range flowmeter
Mohadikar et al. Improvement in the performance of the vortex flowmeter using contraction cone
CN112218727A (en) Flow balance in coating circulation systems
CN102589623A (en) High-accuracy wide-range flow meter
Yan et al. Measurement of particulate velocity under stack-flow conditions
JP2007031040A (en) Flow rate control device for distribution of coal particulates
KR101291691B1 (en) Cone type differential pressure flow measuring apparatus
CN207050788U (en) A kind of new online throttling flow meter
JP2019163111A (en) Powder blowing system
CN105091967B (en) A kind of flow-measuring method using barrier in pipeline itself or pipeline
CN211785607U (en) Measuring device for measuring flow velocity of fluid in pipeline

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20120411

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20130628

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20130808

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20130924

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20131018

R150 Certificate of patent or registration of utility model

Ref document number: 5397996

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

Free format text: JAPANESE INTERMEDIATE CODE: R150

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees