JPS6153390A - Temperature control for modification unit for low-quality coal - Google Patents
Temperature control for modification unit for low-quality coalInfo
- Publication number
- JPS6153390A JPS6153390A JP17493284A JP17493284A JPS6153390A JP S6153390 A JPS6153390 A JP S6153390A JP 17493284 A JP17493284 A JP 17493284A JP 17493284 A JP17493284 A JP 17493284A JP S6153390 A JPS6153390 A JP S6153390A
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- coal
- low
- cooling
- 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.)
- Pending
Links
Abstract
Description
【発明の詳細な説明】
〔発明の利用分野〕
本発明は低品位炭の高品質化装置の温度制御方法に係り
、特に各セクションにおける石炭の熱処理温度を制御す
るのに好適な低品位炭の高品質化装置の温度制御方法に
関するものである。[Detailed Description of the Invention] [Field of Application of the Invention] The present invention relates to a temperature control method for an apparatus for improving the quality of low-rank coal, and in particular to a method for controlling the temperature of a low-rank coal quality improvement device, and in particular, a method for controlling the temperature of a low-rank coal that is suitable for controlling the heat treatment temperature of coal in each section. The present invention relates to a temperature control method for a quality improvement device.
乾燥装置などの熱処理装置において、被熱処理物質の温
度を測定するのは非常にむずかしり、一般にはKV
Rock Ta1k Manual ニ示された例のご
とそ、熱処理装置内に取付けられた熱電対により熱処理
装置内の雰囲気濃度より被熱処理物質の温度を推定した
り、溶鉱炉のごとく、内部火炎を赤外線温度計により検
知したりするのが一般である。In heat treatment equipment such as drying equipment, it is very difficult to measure the temperature of the material to be heat treated, and generally KV
Rock Ta1k Manual 2 In each of the examples shown, the temperature of the material to be heat treated can be estimated from the atmospheric concentration inside the heat treatment equipment using a thermocouple installed in the heat treatment equipment, or the internal flame can be measured using an infrared thermometer, such as in a blast furnace. Generally, it is detected.
このように間接的に検知された温度をフィード・バック
して低品位炭の高品質化装置での低品位炭の温度の制御
を行うには、検知された温度の精度が低く問題である。In order to control the temperature of low-rank coal in an apparatus for improving the quality of low-rank coal by feeding back the indirectly detected temperature in this way, there is a problem in that the accuracy of the detected temperature is low.
本発明の目的は、低品位炭の高品質化装置での低品位炭
の温度を正確に検知することで、各装置)こおいて適切
に温度制御を行うことができる低品位炭の高品質化装置
の温度制御方法を提供することにある。The purpose of the present invention is to accurately detect the temperature of low-rank coal in equipment for improving the quality of low-rank coal. An object of the present invention is to provide a temperature control method for a temperature control device.
本発明は、乾燥装置、乾留装置並びに冷却・吸着装置お
のおのの内部の石炭層内の温度を検知し、該検知温度を
フィードバックして乾燥装置並びに乾留装置へ供給され
る熱媒の温度並びに冷却・吸S装置へ供給される冷却水
の水量を制御することを特徴とするもので、各装置にお
ける低品位炭の温度を正確に検知することで、適切に温
度制御を行えるようにしたものである。The present invention detects the temperature within the coal seam inside each of the drying equipment, carbonization equipment, and cooling/adsorption equipment, and feeds back the detected temperature to determine the temperature of the heating medium supplied to the drying equipment and carbonization equipment, and the cooling/adsorption equipment. It is characterized by controlling the amount of cooling water supplied to the S suction equipment, and by accurately detecting the temperature of the low-rank coal in each equipment, it is possible to appropriately control the temperature. .
前述したように熱処理装置内の石炭温度を正確に測定す
るのはむずかしい。特に熱処理装置がキルンのような回
転体の場合には、石炭自身の温度ではなく雰囲気温度を
測定してしまうことが多い。As mentioned above, it is difficult to accurately measure the temperature of coal in heat treatment equipment. Particularly when the heat treatment equipment is a rotating body such as a kiln, the ambient temperature is often measured rather than the temperature of the coal itself.
そこで、パイロット・プラントの各部に熱電対を埋め込
んでみた。そしてその結果を整理してみると、この装置
は緩慢な熱処理速度のため、熱処理炭が順次移動して行
っても、その中に熱電対を埋め込んでおけば、正確な石
炭温度を検知できることが分った。そこで、被熱処理物
質である石炭の温度を知りたい乾燥装置、乾留装置、並
びに冷却・吸着装置の排出口部に、常時熱処理炭が滞留
するようなスペースを設け、そしてその中に熱電対を埋
め込むことを考え出した。このようにして石炭温度が検
出できれば、パイロット試験結果得られた加熱、又は冷
却温度と石炭温度との関係をもとに温度制御するm;と
が可能である。Therefore, we embedded thermocouples in various parts of the pilot plant. Summarizing the results, we found that because this device has a slow heat treatment speed, even if the heat-treated coal moves one after another, by embedding a thermocouple in it, it is possible to accurately detect the temperature of the coal. I understand. Therefore, in order to know the temperature of the coal, which is the material to be heat treated, we create a space at the outlet of the drying equipment, carbonization equipment, and cooling/adsorption equipment where the heat-treated coal stays at all times, and embed a thermocouple in that space. I figured it out. If the coal temperature can be detected in this way, it is possible to control the temperature based on the relationship between the heating or cooling temperature and the coal temperature obtained as a result of a pilot test.
以下1本発明の一実施例を第1図、第2図により説明す
る。An embodiment of the present invention will be described below with reference to FIGS. 1 and 2.
第1図は本発明を組み込んだ低品位炭の高品質化装置の
温度制御方法のフローで、低品位炭1は乾燥装置2へ供
給され、ここで乾燥後、ロータリ・フィーダ3を介して
乾留装置4へ送られる。乾燥炭はここで乾留後、口でタ
リ・フィーダ5を介し′て、冷却・吸着装置6へ送られ
、ここで冷却。Figure 1 shows the flow of a temperature control method for a low-rank coal quality improvement device incorporating the present invention. Low-rank coal 1 is supplied to a drying device 2, where after drying, it is carbonized via a rotary feeder 3. It is sent to device 4. After the dry coal is carbonized here, it is sent to a cooling/adsorption device 6 via a tarry feeder 5, where it is cooled.
タール吸着後口ツク・ホブパフを介して系外へ改質炭8
として排出される。After tar adsorption, the reformed coal is sent out of the system via a hob puff.
It is discharged as.
乾燥装置2の排出口部9には常時乾燥炭が滞留するよう
にロータリ・フィーダ3の回転を制御する。そして排出
口部9には常時、乾燥炭のなかに熱電対が埋もれている
ような位置に熱電対10を埋め込む。このような方法に
すれば、熱電対lOは、はぼ正確な石炭温度を示す。ま
た、乾燥装置2には熱風炉11より熱媒である熱風がラ
イン四を介して間接的に供給され、加熱される。また、
このライン化には加熱後の降温した排ガスを希釈ガスと
して供給する希釈ガス・ライン13が設けられており、
このラインには流量制御弁14が取付けられている。こ
の流量制御弁14は熱電対10により制御装置1115
を介して制御されている。このようなフローにすること
により最適な乾燥炭の乾燥濃度を制御することが可能と
なる。なお、熱転対10が常時、石炭中に埋もれている
ようにロータリ・フィーダ3を制御されていることを確
認するためには、排出口部9の上下にレベル計を取付け
れば良い。The rotation of the rotary feeder 3 is controlled so that dry coal is always retained in the discharge port 9 of the drying device 2. A thermocouple 10 is embedded in the discharge port 9 at such a position that the thermocouple is always buried in the dry coal. In this way, the thermocouple lO indicates a very accurate coal temperature. Further, hot air, which is a heat medium, is indirectly supplied to the drying device 2 from the hot air stove 11 via a line 4, and the drying device 2 is heated. Also,
This line is provided with a dilution gas line 13 that supplies exhaust gas that has cooled down after heating as dilution gas.
A flow control valve 14 is attached to this line. This flow rate control valve 14 is controlled by a control device 1115 using a thermocouple 10.
controlled via. By using such a flow, it becomes possible to control the optimum drying concentration of drying coal. Incidentally, in order to confirm that the rotary feeder 3 is controlled so that the thermocouple 10 is always buried in the coal, level gauges may be installed above and below the discharge port 9.
上記と同様にして乾留装置4の排出口部16には常時乾
留炭が常留するように、ロータリ・フィーダ5でもって
制御する。そして、そのなかに熱電対17を埋め込み、
熱風ライン18に対する希釈ライン19の流量制御邦銀
を制御して最適な乾留温度に制御することが可能となる
。In the same manner as described above, the rotary feeder 5 is controlled so that carbonized coal always remains in the discharge port 16 of the carbonized distillation device 4. Then, a thermocouple 17 is embedded in it,
It becomes possible to control the flow rate control of the dilution line 19 to the hot air line 18 to the optimum carbonization temperature.
冷却・吸着装置6も全(同様で、排出口部21内に常時
改質炭が滞留するようにロブク・ホッパ7J:lJモ大
きなスペースを取り、常時、改質炭中に熱電対nが埋も
れるようにして温度を検知して、その結果を冷却水ライ
ン幻の流量制御弁2ヘフイード・バックして冷却水の流
量なm整し、最適な冷却温度に制御することが可能とな
る。The cooling/adsorption device 6 also takes up a large space so that the reformed coal always stays in the discharge port 21, and the thermocouple n is always buried in the reformed coal. In this way, the temperature is detected and the result is fed back to the flow rate control valve 2 in the cooling water line to adjust the flow rate of the cooling water and control the cooling temperature to the optimum level.
第2図は、第1図の回転式乾留装置の代りに移動層式乾
留装置6を取付けた場合を示す。この場合には常時、熱
電対あが石炭層内に埋もれているので特別な対策は必要
としない。FIG. 2 shows a case where a moving bed carbonization device 6 is installed in place of the rotary carbonization device shown in FIG. In this case, no special measures are required because the thermocouple is always buried within the coal seam.
以上述べたような方法で、各セクシ雪ンの石炭温度を測
定し、それを加熱、冷却回路へフィード・バックして制
御することにより、所作の温度に熱処理することが可能
となる。By measuring the coal temperature of each coal using the method described above and controlling it by feeding it back to the heating and cooling circuit, it becomes possible to heat-treat the coal to the desired temperature.
本発明によれば、乾燥、乾留、冷却、吸着の各セクシ■
ンにおいて被処理物である石炭の温度を正確に把握でき
、しかも、その結果を加熱、冷却回路へフィード・バッ
クして温度制御ができるので、最適条件で、安定した高
品質化された改質炭な産出する効果がある。According to the present invention, each of drying, carbonization, cooling, and adsorption
The temperature of the coal to be treated can be accurately determined in the process, and the temperature can be controlled by feeding back the results to the heating and cooling circuits, allowing stable and high-quality reforming to be achieved under optimal conditions. It has the effect of producing charcoal.
第1図は本発明を実施した低品位炭の高品質化装置の一
例を示すフロー図、第2図は第1図の回転形乾留装置の
代りに移動層式乾留装置を組込んだフロー図である。Figure 1 is a flow diagram showing an example of an apparatus for improving the quality of low-rank coal in which the present invention is implemented, and Figure 2 is a flow diagram in which a moving bed type carbonization apparatus is incorporated in place of the rotary type carbonization apparatus in Figure 1. It is.
Claims (1)
に冷却・吸着セクションより構成された低品位炭の高品
質化装置において、乾燥装置、乾留装置並びに冷却・吸
着装置おのおのの内部の石炭層内の温度を検知し、該検
知温度をフィード・バックして、乾燥装置、並びに乾留
装置へ供給される熱媒の温度並びに冷却・吸着装置へ供
給される冷却水の水量を制御することを特徴とする低品
位炭の高品質化装置の温度制御方法。1. In an equipment for improving the quality of low-rank coal, which is composed of a connected drying section, carbonization section, and cooling/adsorption section, the temperature within the coal seam inside each of the drying equipment, carbonization equipment, and cooling/adsorption equipment is controlled. A low-grade device characterized by detecting the temperature and feeding back the detected temperature to control the temperature of the heating medium supplied to the drying device and the carbonization device, and the amount of cooling water supplied to the cooling/adsorption device. Temperature control method for charcoal quality improvement equipment.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17493284A JPS6153390A (en) | 1984-08-24 | 1984-08-24 | Temperature control for modification unit for low-quality coal |
US06/768,114 US4668244A (en) | 1984-08-22 | 1985-08-21 | Method and apparatus for upgrading low rank coal |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17493284A JPS6153390A (en) | 1984-08-24 | 1984-08-24 | Temperature control for modification unit for low-quality coal |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6153390A true JPS6153390A (en) | 1986-03-17 |
Family
ID=15987239
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP17493284A Pending JPS6153390A (en) | 1984-08-22 | 1984-08-24 | Temperature control for modification unit for low-quality coal |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6153390A (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2011074279A1 (en) * | 2009-12-18 | 2011-06-23 | 三菱重工業株式会社 | Coal reforming equipment |
JP4939662B1 (en) * | 2011-03-22 | 2012-05-30 | 三菱重工業株式会社 | Coal reforming system |
WO2013125609A1 (en) * | 2012-02-24 | 2013-08-29 | 三菱重工業株式会社 | Reformed coal production equipment, and method for controlling same |
WO2013125608A1 (en) * | 2012-02-24 | 2013-08-29 | 三菱重工業株式会社 | Reformed coal production equipment |
WO2013136944A1 (en) * | 2012-03-12 | 2013-09-19 | 三菱重工業株式会社 | Coal dry distillation device |
WO2014024504A1 (en) * | 2012-08-06 | 2014-02-13 | 三菱重工業株式会社 | Coal dry-distillation device and modified coal production equipment using same |
JP2014074184A (en) * | 2014-01-27 | 2014-04-24 | Mitsubishi Heavy Ind Ltd | Coal carbonization apparatus |
JP2014114458A (en) * | 2014-01-27 | 2014-06-26 | Mitsubishi Heavy Ind Ltd | Coal carbonization apparatus |
-
1984
- 1984-08-24 JP JP17493284A patent/JPS6153390A/en active Pending
Cited By (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2011074279A1 (en) * | 2009-12-18 | 2011-06-23 | 三菱重工業株式会社 | Coal reforming equipment |
JP4939662B1 (en) * | 2011-03-22 | 2012-05-30 | 三菱重工業株式会社 | Coal reforming system |
US8821695B2 (en) | 2011-03-22 | 2014-09-02 | Mitsubishi Heavy Industries, Ltd. | Coal reforming system |
JP2013173831A (en) * | 2012-02-24 | 2013-09-05 | Mitsubishi Heavy Ind Ltd | Modified coal production facility |
WO2013125608A1 (en) * | 2012-02-24 | 2013-08-29 | 三菱重工業株式会社 | Reformed coal production equipment |
JP2013173833A (en) * | 2012-02-24 | 2013-09-05 | Mitsubishi Heavy Ind Ltd | Modified coal production facility and control method thereof |
WO2013125609A1 (en) * | 2012-02-24 | 2013-08-29 | 三菱重工業株式会社 | Reformed coal production equipment, and method for controlling same |
CN104066824A (en) * | 2012-02-24 | 2014-09-24 | 三菱重工业株式会社 | Reformed coal production equipment, and method for controlling same |
CN104066824B (en) * | 2012-02-24 | 2016-03-16 | 三菱重工业株式会社 | Modified coal producing apparatus and control method thereof |
WO2013136944A1 (en) * | 2012-03-12 | 2013-09-19 | 三菱重工業株式会社 | Coal dry distillation device |
JP2013189554A (en) * | 2012-03-12 | 2013-09-26 | Mitsubishi Heavy Ind Ltd | Coal dry distillation apparatus |
CN104066816A (en) * | 2012-03-12 | 2014-09-24 | 三菱重工业株式会社 | Coal dry distillation device |
WO2014024504A1 (en) * | 2012-08-06 | 2014-02-13 | 三菱重工業株式会社 | Coal dry-distillation device and modified coal production equipment using same |
JP2014031462A (en) * | 2012-08-06 | 2014-02-20 | Mitsubishi Heavy Ind Ltd | Coal carbonization apparatus and facility for producing modified coal by utilizing the same |
JP2014074184A (en) * | 2014-01-27 | 2014-04-24 | Mitsubishi Heavy Ind Ltd | Coal carbonization apparatus |
JP2014114458A (en) * | 2014-01-27 | 2014-06-26 | Mitsubishi Heavy Ind Ltd | Coal carbonization apparatus |
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