JP2002046863A - Powder supply device and method - Google Patents
Powder supply device and methodInfo
- Publication number
- JP2002046863A JP2002046863A JP2000233639A JP2000233639A JP2002046863A JP 2002046863 A JP2002046863 A JP 2002046863A JP 2000233639 A JP2000233639 A JP 2000233639A JP 2000233639 A JP2000233639 A JP 2000233639A JP 2002046863 A JP2002046863 A JP 2002046863A
- Authority
- JP
- Japan
- Prior art keywords
- powder
- char
- powder supply
- cut
- differential pressure
- 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.)
- Pending
Links
Landscapes
- Air Transport Of Granular Materials (AREA)
- Filling Or Emptying Of Bunkers, Hoppers, And Tanks (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、ホッパ等に貯留さ
れた粉体を定量的に切り出して空気輸送する場合に用い
て好適な粉体供給装置及び方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a powder supply apparatus and a method suitable for use in a case where powder stored in a hopper or the like is quantitatively cut out and transported by air.
【0002】[0002]
【従来の技術】従来、ホッパ等に貯留された粉体を定量
的に切り出して空気輸送する方法として、例えばテーブ
ルフィーダ、ロータリーバルブ、スクリュウフィーダ等
の定量性を有する機種の切り出し装置が使用されてい
る。これらの定量切り出し装置は何れも定容積式の切り
出し装置であり、貯留量によって切り出し装置近傍の粉
体の圧密程度あるいはフラッシィング性が異なり、必ず
しも安定な定量性が得られるとは言い難い。特に、粉体
が、廃棄物を熱分解した際に生成される炭素を主成分と
するチャーである場合、チャーは圧密性あるいはフラッ
シィング性が大きく、非常に扱い難い粉体であるため、
安定な制御は非常に困難である。2. Description of the Related Art Conventionally, as a method of quantitatively cutting out powder stored in a hopper or the like and pneumatically transporting the same, for example, a cutting device of a model having a quantitative property such as a table feeder, a rotary valve, a screw feeder, or the like has been used. I have. Each of these quantitative cutout devices is a fixed-volume cutout device, and the degree of compaction or flushing property of the powder in the vicinity of the cutout device differs depending on the storage amount, and it cannot be said that stable quantitativeness can always be obtained. In particular, when the powder is a char whose main component is carbon generated when pyrolyzing waste materials, the char has a large compaction or flashing property and is a powder that is very difficult to handle.
Stable control is very difficult.
【0003】上記欠点を解決する方法として、従来より
貯留槽の重量を連続測定し、重量の減量から切り出し量
を算出して切り出し装置を制御する方法がある。また、
切り出した粉体の重量をインパクト流量計やベルトスケ
ール等で測定し、切り出し装置を制御する方法がある。As a method for solving the above-mentioned drawback, there has been a method in which the weight of a storage tank is continuously measured, and a cut-out amount is calculated from a weight reduction to control a cut-out device. Also,
There is a method of controlling the cutting device by measuring the weight of the cut powder with an impact flow meter, a belt scale, or the like.
【0004】[0004]
【発明が解決しようとする課題】しかしながら上述の前
者の方法は、貯留槽への粉体の供給と切り出しが同時に
行われている装置や、貯留槽からの粉体の切り出しが複
数の時は採用できないという問題があった。また後者の
方法は、設備機器が増加し経済的でないという問題があ
った。However, the former method described above is adopted in an apparatus in which powder supply and cutout to the storage tank are simultaneously performed, and when powder cutout from the storage tank is plural. There was a problem that it was not possible. In addition, the latter method has a problem that the equipment is increased and it is not economical.
【0005】本発明は上記の実情に鑑みてなされたもの
で、ホッパ等に貯留された圧密性あるいはフラッシィン
グ性があるチャー等の粉体を定量的に切り出して空気輸
送できる経済的な粉体供給装置及び方法を提供すること
を目的としている。The present invention has been made in view of the above circumstances, and is an economical powder capable of quantitatively cutting out powder such as char having compaction or flashing properties stored in a hopper or the like and transporting it pneumatically. It is an object to provide a supply device and method.
【0006】[0006]
【課題を解決するための手段】上記の目的を達成するた
めに、本発明による粉体供給装置においては、貯留槽か
ら粉体を切り出す切り出し装置と、前記切り出された粉
体を空気輸送する空気輸送配管と、前記空気輸送配管の
2カ所の圧力を検出する検出手段と、前記検出手段で検
出された各圧力の差圧を検出する差圧検出手段と、上記
差圧検出手段で検出された差圧に応じて前記切り出し装
置を制御し粉体の切り出し量を制御する制御手段とを設
けている。In order to achieve the above object, a powder supply device according to the present invention comprises a cutting device for cutting powder from a storage tank, and an air for pneumatically transporting the cut powder. A transport pipe, detecting means for detecting two pressures in the pneumatic transport pipe, differential pressure detecting means for detecting a differential pressure of each pressure detected by the detecting means, and a differential pressure detected by the differential pressure detecting means. Control means for controlling the cutting device in accordance with the differential pressure to control the amount of powder cut out.
【0007】また、本発明による粉体供給方法において
は、貯留槽から切り出された粉体を空気輸送する空気輸
送配管の2カ所の差圧を検出し、この差圧に応じて前記
粉体の切り出し量を制御するようにしている。Further, in the powder supply method according to the present invention, a pressure difference between two points of an air transport pipe for pneumatically transporting the powder cut from the storage tank is detected, and the pressure difference of the powder is detected in accordance with the differential pressure. The cutout amount is controlled.
【0008】[0008]
【発明の実施の形態】以下、本発明の実施の形態を図面
を参照して説明する。本発明者等は、粉体を空気輸送す
る際、輸送配管で発生する圧力損失が空気流量と粉体の
輸送量とに相関があるという知見に基づいて、空気流量
を一定にすることで、圧力損失と粉体の輸送量との相関
の知見を得た。このような知見に基づいて本実施の形態
においては、空気輸送配管の圧力損失を測定し、切り出
し装置を制御することによって、ホッパ等に貯留された
圧密性あるいはフラッシィング性がある粉体を定量的に
切り出して空気輸送することが可能となった。Embodiments of the present invention will be described below with reference to the drawings. The present inventors, when pneumatically transporting the powder, based on the knowledge that the pressure loss generated in the transport pipe is correlated with the air flow rate and the transport rate of the powder, by making the air flow rate constant, The knowledge of the correlation between the pressure loss and the amount of powder transported was obtained. In the present embodiment, based on such knowledge, the pressure loss of the pneumatic transportation pipe is measured, and the cutting device is controlled to quantify the powder having compaction or flushing properties stored in a hopper or the like. It has become possible to carry out pneumatic transportation by cutting out.
【0009】図1は本発明の実施の形態による粉体供給
装置を示す構成図である。図1において、1は廃棄物を
熱分解した際に生成されるチャーを貯留するチャーホッ
パである。チャーは、圧密性とフラッシィング性を兼ね
備えた非常に取り扱いが困難な粉体である。さらに廃棄
物の種類、熱分解温度によりチャーの見掛け密度等の物
性値も変化し、通常の定量切り出し装置での定量切り出
しは非常に困難である。FIG. 1 is a block diagram showing a powder supply apparatus according to an embodiment of the present invention. In FIG. 1, reference numeral 1 denotes a char hopper for storing char generated when pyrolysis of waste is performed. Char is a powder which has both consolidation and flashing properties and is very difficult to handle. Furthermore, the physical properties such as the apparent density of the char vary depending on the type of waste and the thermal decomposition temperature, and it is very difficult to perform quantitative extraction with a normal quantitative extraction device.
【0010】2は振動排出機、3は切り出し装置として
のテーブルフィーダ、11はテーブルフィーダ3を回転
させるモータ(VVVF)である。4は空気輸送用ブロ
ワであり、本実施の形態では定容積ブロワを用いてい
る。5はロータリバルブ、6は空気輸送配管である。空
気輸送配管6には高圧側圧力検出座7と低圧側圧力検出
座8とが、好ましくは両者とも垂直配管部6Aに取り付
けられている。Reference numeral 2 denotes a vibration discharger, 3 denotes a table feeder as a cutting device, and 11 denotes a motor (VVVF) for rotating the table feeder 3. Reference numeral 4 denotes a pneumatic transport blower, which uses a constant volume blower in the present embodiment. Reference numeral 5 denotes a rotary valve, and reference numeral 6 denotes a pneumatic transportation pipe. A high pressure side pressure detecting seat 7 and a low pressure side pressure detecting seat 8 are preferably attached to the vertical pipe portion 6A in the pneumatic transportation pipe 6.
【0011】9は差圧変換器で、高圧側圧力検出座7と
低圧側圧力検出座8で検出された圧力の差を電気信号に
変換する。供給量制御部12は、差圧変換器12からの
上記電気信号に応じてテーブルフィーダ3のモータ11
の回転数を制御することにより、チャーの切り出し量が
一定になるように制御する。Reference numeral 9 denotes a differential pressure converter, which converts the difference between the pressure detected by the high pressure side pressure detection seat 7 and the pressure detected by the low pressure side pressure detection seat 8 into an electric signal. The supply amount control unit 12 controls the motor 11 of the table feeder 3 according to the electric signal from the differential pressure converter 12.
By controlling the number of rotations, the amount of cut out of the char is controlled to be constant.
【0012】10は旋回式燃焼炉で、チャーを燃焼しチ
ャーに含有されている無機分を溶融処理する。この旋回
燃焼炉10でチャーを安定に燃焼させるためには、チャ
ーの安定供給が必須になる。Reference numeral 10 denotes a revolving combustion furnace, which burns the char and melts the inorganic components contained in the char. In order to stably burn char in the swirling combustion furnace 10, stable supply of char is essential.
【0013】上記構成において、チャーホッパ1から振
動排出機2及びテーブルフィーダ3を介して切り出され
たチャーは、ロータリーバルブ5を通じて空気輸送配管
6に送り込まれ、空気輸送用ブロア4からの空気により
輸送される。そして、上り垂直配管部6Aにおいて、高
圧側圧力検出座7と低圧側圧力検出座8により圧力が検
出され、各検出値の差圧が差圧変換器により電気信号に
変換される。供給量制御部12は、差圧変換器12から
の上記電気信号に応じてテーブルフィーダ3のモータ1
1の回転数を制御する。これによって、チャーホッパ1
からのチャーの切り出し量が一定になるように制御され
る。In the above configuration, the char cut out from the char hopper 1 through the vibration discharger 2 and the table feeder 3 is sent to the air transport pipe 6 through the rotary valve 5 and transported by the air from the air transport blower 4. You. Then, in the upward vertical pipe section 6A, the pressure is detected by the high pressure side pressure detection seat 7 and the low pressure side pressure detection seat 8, and the differential pressure of each detected value is converted into an electric signal by the differential pressure converter. The supply amount control unit 12 controls the motor 1 of the table feeder 3 according to the electric signal from the differential pressure converter 12.
1 is controlled. Thus, the char hopper 1
Is controlled so that the cut-out amount of the char from is constant.
【0014】次に、本実施の形態を実施例に基づいてさ
らに詳説する。本実施例で使用した廃棄物の熱分解生成
物のチャーの性状を記す。 ・見掛け比重:0.4 〜0.7 ・平均粒径 :30μm〜80μm ・発熱量:10,000MJ/kg 〜20,000MJ/kg ・噴流性指数:86 ・圧縮度:31% これらの数値は、チャーが、噴流性指数が大きくフラッ
シングしやすく、且つ圧縮度が大きく、圧密し易く架橋
現象を起こしやすい粉体であることを示している。Next, this embodiment will be described in more detail based on examples. The properties of the char of the thermal decomposition product of the waste used in this example are described. -Apparent specific gravity: 0.4 to 0.7-Average particle size: 30 to 80 µm-Calorific value: 10,000 MJ / kg to 20,000 MJ / kg-Jetability index: 86-Compressibility: 31% It shows that the powder has a large index, is easily flushed, has a high degree of compression, is easily compacted, and easily causes a crosslinking phenomenon.
【0015】このようなチャーをテーブルフィーダ3だ
けで切り出した時のテーブルフィーダの回転数と切り出
し量との関係を図2に示す。図2においては、テーブル
フィーダの回転数とチャー切り出し量との間にはある程
度の相関は見られるが、テーブルフィーダだけでは定量
性は無いと言える。FIG. 2 shows the relationship between the number of rotations of the table feeder and the cutting amount when such a char is cut out only by the table feeder 3. In FIG. 2, there is a certain degree of correlation between the number of rotations of the table feeder and the amount of char cut-out, but it can be said that there is no quantitative property using the table feeder alone.
【0016】次に本実施例による切り出し量の制御例を
示す。図3は切り出し量の設定値を150kg/hと1
00kg/hにした場合のチャー切り出し量とテーブル
フィーダの回転数の経時変化を示したものである。図3
において、0分から90分までは切り出し量の設定値を
150kg/hとし、90分から150分までは切り出
し量の設定値を100kg/hとして回転数を制御した
結果、略設定値通りの安定した切り出し量が得られ、初
期の目的を達成することができた。Next, an example of controlling the cutout amount according to this embodiment will be described. FIG. 3 shows that the set value of the cutting amount is 150 kg / h and 1
The graph shows the change over time in the char cutout amount and the rotation speed of the table feeder when the pressure is set to 00 kg / h. FIG.
, The cut-off amount is set to 150 kg / h from 0 minutes to 90 minutes, and the cut-off amount is set to 100 kg / h from 90 minutes to 150 minutes. The amount was obtained and the initial objectives could be achieved.
【0017】尚、図1の実施の形態においては、高圧側
圧力検出座7と低圧側圧力検出座8を空気輸送配管6の
上りの垂直配管部6Aに設けたが、水平配管部に設ける
ことも可能である。しかしながら、水平配管部に設ける
と、チャーの輸送を一旦止めた場合等にチャーの堆積が
生じやすく、検出精度を損なうおそれがあるので、垂直
配管部6Aに設けるのが好ましい。また、ある程度の上
り勾配がある配管部に設けてもよい。In the embodiment shown in FIG. 1, the high pressure side pressure detection seat 7 and the low pressure side pressure detection seat 8 are provided in the vertical pipe section 6A on the upside of the pneumatic transport pipe 6, but may be provided in the horizontal pipe section. Is also possible. However, if it is provided in the horizontal pipe section, it is easy to cause char accumulation when transport of the char is temporarily stopped, and the detection accuracy may be impaired. Therefore, it is preferably provided in the vertical pipe section 6A. Further, it may be provided in a pipe portion having a certain upward slope.
【0018】また、図1の実施の形態では、切り出し装
置としてテーブルフィーダ3を用いているが、ロータリ
バルブやスクリューフィーダ等を用いることもできる。In the embodiment shown in FIG. 1, the table feeder 3 is used as a cutting device, but a rotary valve, a screw feeder, or the like may be used.
【0019】[0019]
【発明の効果】以上説明したように本発明によれば、粉
体の空気輸送管の2カ所の差圧を検出し、この差圧に応
じて切り出し装置を制御し、粉体の切り出し量を制御す
るようにしたので、粉体の切り出し量を略一定に安定し
て制御することができる。特に、チャーのように圧密性
あるいはフラッシィング性のある非常に扱い難い粉体の
場合に優れた効果を発揮することができる。As described above, according to the present invention, the differential pressure of two places in the pneumatic transport pipe of powder is detected, and the cutting device is controlled in accordance with the differential pressure to reduce the amount of powder cut. Since the control is performed, the cut-out amount of the powder can be stably controlled to be substantially constant. In particular, an excellent effect can be exhibited in the case of a powder which is very difficult to handle such as a char and has a compacting property or a flashing property.
【図1】 本発明の実施の形態による粉体供給装置を示
す構成図である。FIG. 1 is a configuration diagram showing a powder supply device according to an embodiment of the present invention.
【図2】 チャーをテーブルフィーダだけで切り出した
場合のテーブルフィーダの回転数と切り出し量との関係
を示す特性図である。FIG. 2 is a characteristic diagram showing a relationship between the number of rotations of a table feeder and a cutout amount when a char is cut out only by a table feeder.
【図3】 切り出し量の設定値を150kg/hと10
0kg/hにした時のチャー切り出し量とテーブルフィ
ーダの回転数の経時変化を示す特性図である。[FIG. 3] The set values of the cutout amount are 150 kg / h and 10
FIG. 9 is a characteristic diagram showing a change over time in the amount of char cut-out and the number of rotations of the table feeder at 0 kg / h.
1 チャーホッパ 2 振動排出機 3 テーブルフィーダ 4 空気輸送用ブロワ 5 ロータリバルブ 6 空気輸送配管 6A 垂直配管部 7 高圧側圧力検出座 8 低圧側圧力検出座 9 差圧変換器 10 旋回燃焼炉 11 モータ 12 供給量制御部 DESCRIPTION OF SYMBOLS 1 Char hopper 2 Vibration discharger 3 Table feeder 4 Pneumatic transportation blower 5 Rotary valve 6 Pneumatic transportation piping 6A Vertical piping part 7 High pressure side pressure detection seat 8 Low pressure side pressure detection seat 9 Differential pressure converter 10 Rotating combustion furnace 11 Motor 12 Supply Quantity control unit
───────────────────────────────────────────────────── フロントページの続き (72)発明者 矢澤 伸弘 東京都中央区佃2丁目17番15号 月島機械 株式会社内 Fターム(参考) 3F047 AA11 AB02 CC01 3F075 BA02 BB01 CA02 CA09 CB12 CB14 CB15 CB16 CC04 CC15 CC24 CD04 DA08 ──────────────────────────────────────────────────続 き Continued on the front page (72) Nobuhiro Yazawa 2-17-15 Tsukuda, Chuo-ku, Tokyo Tsukishima Machinery Co., Ltd. F-term (reference) 3F047 AA11 AB02 CC01 3F075 BA02 BB01 CA02 CA09 CB12 CB14 CB15 CB16 CC04 CC15 CC24 CD04 DA08
Claims (7)
と、 前記切り出された粉体を空気輸送する空気輸送配管と、 前記空気輸送配管の2カ所の圧力を検出する検出手段
と、 前記検出手段で検出された各圧力の差圧を検出する検出
手段と、 前記差圧検出手段で検出された差圧に応じて前記切り出
し装置を制御し粉体の切り出し量を制御する制御手段と
を設けたことを粉体供給装置。1. A cutting device for cutting powder from a storage tank, an air transport pipe for pneumatically transporting the cut powder, a detecting means for detecting two pressures of the pneumatic transport pipe, and the detecting means Detecting means for detecting the differential pressure of each pressure detected in the above, and control means for controlling the cutting device in accordance with the differential pressure detected by the differential pressure detecting means to control the amount of powder cut out. That the powder supply device.
り勾配部分に設けることを特徴とする請求項1記載の粉
体供給装置。2. The powder supply apparatus according to claim 1, wherein said detection means is provided in an upwardly sloped portion of said pneumatic transportation pipe.
垂直な上り部分に設けることを特徴とする請求項1記載
の粉体供給装置。3. The powder supply device according to claim 1, wherein said detection means is provided in a substantially vertical ascending portion of said pneumatic transportation pipe.
成される炭素を主成分とするチャーであることを特徴と
する請求項1記載の粉体供給装置。4. The powder supply apparatus according to claim 1, wherein the powder is a char whose main component is carbon generated when pyrolyzing waste material.
あり、前記制御手段は、前記テーブルフィーダを回転さ
せるモータの回転数を制御することを特徴とする請求項
1記載の粉体供給装置。5. The powder supply device according to claim 1, wherein the cutting device is a table feeder, and the control unit controls a rotation speed of a motor that rotates the table feeder.
用ブロワが定容積式ブロワであることを特徴とする請求
項1記載の粉体供給装置。6. The powder supply apparatus according to claim 1, wherein the blower for pneumatic transportation used for the pneumatic transportation pipe is a fixed displacement blower.
する空気輸送配管の2カ所の差圧を検出し、この差圧に
応じて前記粉体の切り出し量を制御することを特徴とす
る粉体供給方法。7. The method according to claim 1, further comprising detecting a pressure difference between two points of a pneumatic transportation pipe for pneumatically transporting the powder cut from the storage tank, and controlling a cut-out amount of the powder according to the pressure difference. Powder supply method.
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JP2000233639A JP2002046863A (en) | 2000-08-01 | 2000-08-01 | Powder supply device and method |
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JP2012041192A (en) * | 2011-09-30 | 2012-03-01 | Daio Paper Corp | Powder supply apparatus and absorber fabrication facility |
JP2012188282A (en) * | 2011-03-14 | 2012-10-04 | Kajima Corp | Powder volumetric feeding method |
CN102849463A (en) * | 2012-09-11 | 2013-01-02 | 四川玖玖爱食品有限公司 | Positive-pressure conveying device applicable to mixed flour of various grain raw materials |
KR101521856B1 (en) * | 2012-11-15 | 2015-05-29 | 한국에너지기술연구원 | Fuel quantity sensing device and method using pressure sensor |
JP2019167244A (en) * | 2018-02-27 | 2019-10-03 | ピアブ エイビーPiab Ab | Conveyer system |
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JP2012188282A (en) * | 2011-03-14 | 2012-10-04 | Kajima Corp | Powder volumetric feeding method |
JP2012041192A (en) * | 2011-09-30 | 2012-03-01 | Daio Paper Corp | Powder supply apparatus and absorber fabrication facility |
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