JPH0331609A - Fuel switching for heating furnace, and the like - Google Patents
Fuel switching for heating furnace, and the likeInfo
- Publication number
- JPH0331609A JPH0331609A JP16369989A JP16369989A JPH0331609A JP H0331609 A JPH0331609 A JP H0331609A JP 16369989 A JP16369989 A JP 16369989A JP 16369989 A JP16369989 A JP 16369989A JP H0331609 A JPH0331609 A JP H0331609A
- Authority
- JP
- Japan
- Prior art keywords
- fuel
- switching
- flow rate
- time
- burner
- 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.)
- Granted
Links
- 239000000446 fuel Substances 0.000 title claims abstract description 50
- 238000010438 heat treatment Methods 0.000 title claims abstract description 20
- 238000000034 method Methods 0.000 claims description 12
- 101150001783 fic1 gene Proteins 0.000 abstract description 9
- 238000011144 upstream manufacturing Methods 0.000 abstract description 2
- 230000001105 regulatory effect Effects 0.000 abstract 6
- 238000010586 diagram Methods 0.000 description 4
- 230000005856 abnormality Effects 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000000629 steam reforming Methods 0.000 description 2
- BDLWRIAFNYVGTC-UHFFFAOYSA-N 2-[bis(2-chloroethyl)amino]ethyl 3-(acridin-9-ylamino)propanoate Chemical compound C1=CC=C2C(NCCC(=O)OCCN(CCCl)CCCl)=C(C=CC=C3)C3=NC2=C1 BDLWRIAFNYVGTC-UHFFFAOYSA-N 0.000 description 1
- 102000051619 SUMO-1 Human genes 0.000 description 1
- 108700038981 SUMO-1 Proteins 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 238000002407 reforming Methods 0.000 description 1
- RSAQARAFWMUYLL-UHFFFAOYSA-N tic-10 Chemical compound CC1=CC=CC=C1CN1C(CCN(CC=2C=CC=CC=2)C2)=C2C(=O)N2CCN=C21 RSAQARAFWMUYLL-UHFFFAOYSA-N 0.000 description 1
Abstract
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は加熱炉等の燃料切替方法に関するものである。[Detailed description of the invention] (Industrial application field) The present invention relates to a fuel switching method for a heating furnace or the like.
(従来技術)
ナフサ、LPG等の炭化水素を原料にして、水蒸気改質
反応により都市ガスを製造する装置には。(Prior art) For equipment that uses hydrocarbons such as naphtha and LPG as raw materials to produce city gas through a steam reforming reaction.
原料の炭化水素を予熱する加熱炉及び水蒸気改質反応を
行う改質炉が設置されている。そしてこれらの炉におい
ては製品の都市ガスを確実且つ安定して製造できるよう
、二種類の燃料を別個にそれぞれ供給できる2系統の燃
料供給システムが設置されている。A heating furnace for preheating raw material hydrocarbons and a reforming furnace for carrying out a steam reforming reaction are installed. These furnaces are equipped with two fuel supply systems that can separately supply two types of fuel so that city gas can be reliably and stably produced.
第2図は加熱炉の燃料として都市ガスとLPGの2系統
を採用した場合の従来の燃料供給システムの系統図であ
る9図においてFIC−10゜FIC−20はそれぞれ
都市ガス、LPGの流量指示調節計であり、燃料流量の
フィードバック制御を行うとともに、加熱炉を出るプロ
セス流体の温度を所定温度に制御する温度指示調節計T
lC−10によりカスケード制御される。PIC−10
゜PIC−20はそれぞれFIC−10,FIC−20
の1次圧を一定に維持するための圧力指示調節計であり
、Hv −10、Hv −20はそれぞれ都市ガス流路
、LPG流路の遮断弁である。Figure 2 is a system diagram of a conventional fuel supply system when city gas and LPG are used as fuel for the heating furnace. In Figure 9, FIC-10 and FIC-20 indicate the flow rates of city gas and LPG, respectively Temperature indicating controller T, which is a controller and performs feedback control of the fuel flow rate and controls the temperature of the process fluid exiting the heating furnace to a predetermined temperature.
Cascade control is provided by IC-10. PIC-10
゜PIC-20 is FIC-10 and FIC-20 respectively
Hv-10 and Hv-20 are cutoff valves for the city gas flow path and LPG flow path, respectively.
以上の従来の2系統燃料供給システムにおける使用燃料
の切替方法は次の通りである0例えば都市ガスからLP
Gに切替える場合について説明する。最初に加熱炉の負
荷を一定にしておきTIC−40のカスケード制御を外
し、LPGの遮断弁Hv−20を開にする。次に都市ガ
スの流量をFIC−10により若干量減量するとともに
、発熱量換算で同量に相当するLPGttFIC−20
により供給する。以上の操作を何回か繰り返しLPGの
みになる迄行うが、この間都市ガスとLPGの合計熱量
が一定になるよう、且つ安定燃焼が維持できるよう留意
しながら操作するが、実際には数十分間(例えば30分
)以上要している。The method of switching the fuel used in the conventional two-line fuel supply system described above is as follows.0For example, from city gas to LP
The case of switching to G will be explained. First, the load on the heating furnace is kept constant, the cascade control of TIC-40 is removed, and the LPG cutoff valve Hv-20 is opened. Next, the flow rate of city gas is slightly reduced using FIC-10, and LPGttFIC-20, which is equivalent to the same amount in terms of calorific value, is used.
Supplied by The above operation is repeated several times until only LPG is left.During this time, care is taken to keep the total calorific value of city gas and LPG constant and to maintain stable combustion, but in reality it takes several minutes. It takes more than 30 minutes (for example, 30 minutes).
切替が終り運転が安定すれば、T I C−10のカス
ケード制御を生かし通常運転に復帰する。When the switching is completed and the operation becomes stable, the cascade control of TIC-10 is utilized to return to normal operation.
以上説明した従来の燃料の切替方法では、切替に必要な
時間が長く、しかもこの間都市ガスとLPGのように燃
料の単位容積当りの発熱量が5〜6倍と大きく異る場合
には燃焼状態も大きく変化するため、この間の種々監視
業務、その他の操作等に多くの労力が必要であるという
問題があった。In the conventional fuel switching method explained above, the time required for switching is long, and during this time, the combustion state is There is a problem in that a large amount of effort is required for various monitoring tasks and other operations during this period, as the amount of data changes greatly.
(発明が解決しようとする課題)
本発明は叙上の事情に鑑みてなさ九たものであって、切
替作業を自動的にしかも短時間に行うことができる省力
化した加熱炉等の燃料切替方法を提供することを課題と
するものである。(Problems to be Solved by the Invention) The present invention has been devised in view of the above circumstances, and is a labor-saving fuel switching device for heating furnaces, etc., which can perform the switching operation automatically and in a short time. The objective is to provide a method.
(課題を解決するための手段)
本発明の要旨とするところは、二種類の燃料を交互に切
替えて使用する加熱炉等に於て、切替え後の新しい燃料
が切替弁からバーナ迄到達する時間を求め、切替弁を切
替えた時からこの到達時間経過時に燃料の流量調節弁の
弁開度を新しい燃料の流量に必要な開度に瞬時に調整す
ることを特徴とする加熱炉等の燃料切替方法である。(Means for Solving the Problems) The gist of the present invention is that in a heating furnace or the like in which two types of fuel are alternately switched, the time taken for new fuel to reach the burner from the switching valve after switching is , and instantaneously adjusts the valve opening of the fuel flow rate control valve to the opening required for the new fuel flow rate when this arrival time has elapsed from the time the changeover valve is switched. It's a method.
すなわち切替弁を操作してから新しい燃料がバーナに到
達する時間を切替弁とバーナ間の幾何容積、流量調節弁
のCv値、新しい燃料の圧力及び流量等から電子計算機
により総合的に求め、切替弁を操作時からこの到達時間
を経過した時に、燃料の流量調節弁を新しい燃料の所定
流量に相当する弁開度に瞬時に調整することが特徴であ
る。これにより新しい燃料がバーナに到達すると同時に
燃料の調節弁の弁開度が調整されるので、この後は所定
流量でバーナに供給することができる。In other words, the time it takes for new fuel to reach the burner after operating the switching valve is comprehensively determined by a computer from the geometric volume between the switching valve and the burner, the Cv value of the flow rate control valve, the pressure and flow rate of new fuel, etc. A feature of the present invention is that when this time has elapsed since the valve was operated, the fuel flow rate control valve is instantly adjusted to the valve opening corresponding to a predetermined flow rate of new fuel. As a result, the valve opening of the fuel control valve is adjusted at the same time that new fuel reaches the burner, so that it can thereafter be supplied to the burner at a predetermined flow rate.
切替弁としては三方弁が好適であるが、それぞれの流路
に遠隔操作の開閉弁を設けてもよい。流量調節計の測定
端としては燃料種類が変って比重。Although a three-way valve is suitable as the switching valve, a remote-controlled on-off valve may be provided in each flow path. The measuring end of the flow rate controller changes the specific gravity depending on the type of fuel.
容積流量が大きく変動しても正確に測定できる型式の流
量計1、例えばカルマン渦式流量計等が好適である。A type of flowmeter 1 that can accurately measure even if the volumetric flow rate varies greatly, such as a Karman vortex flowmeter, is suitable.
本方法によれば従来方法に較べて非常に短時間に、且つ
自動的に行うことができ、しかも切替え中何等の異常を
来すことなく、W4調に切替えを行うことができる。According to this method, it is possible to perform the switching automatically and in a much shorter time than the conventional method, and moreover, the switching to the W4 key can be performed without any abnormality occurring during the switching.
(実施例) 以下実施例に基づいて本発明の内容をさらに説明する。(Example) The content of the present invention will be further explained below based on Examples.
第1図は本発明を加熱炉に実施した場合の系統図である
。FIG. 1 is a system diagram when the present invention is implemented in a heating furnace.
図においてPIC−1,PIC−2はそれぞれ都市ガス
、LPGの供給圧力の圧力指示調節計であり、この調節
計により後記する流量調節計の一次圧力が所定圧力に維
持される。Hv−1は三方ロボール弁であり、弁軸の回
転により都市ガス→LPG、LPG→都市ガスの流路切
換が行い得る構造になっている。FIC−1は都市ガス
、LPGいずれにも使用できる流量指示調節計であり。In the figure, PIC-1 and PIC-2 are pressure indicating regulators for the supply pressures of city gas and LPG, respectively, and these regulators maintain the primary pressure of the flow rate regulator, which will be described later, at a predetermined pressure. Hv-1 is a three-way Robor valve, and has a structure in which the flow path can be switched from city gas to LPG and from LPG to city gas by rotating the valve shaft. FIC-1 is a flow rate indicator controller that can be used for both city gas and LPG.
ガスの物性や流量が大きく変動しても測定できるカルマ
ン渦式流量計等が好適である。TlC−1は加熱炉を出
るプロセス流体の温度指示調節計であり、前記の流量指
示調節計FIC−1とカスケードして燃料流量の制御に
使用される。以上の構成からなる本発明の燃料の切換方
法は次の通りである。切換に先立って加熱炉の負荷を一
定とし、TlC−1のカスケードも外し、そしてFIC
−1の調節弁の弁開度は一定に保持する。Hv−1の切
替操作に先立ち、電子計算機により次の項目を求める。A Karman vortex flowmeter or the like is suitable, since it can measure even when the physical properties and flow rate of the gas vary greatly. TIC-1 is a temperature indicating controller for the process fluid exiting the heating furnace, and is used in cascade with the flow rate indicating controller FIC-1 to control the fuel flow rate. The fuel switching method of the present invention having the above configuration is as follows. Prior to switching, the load on the heating furnace was made constant, the TLC-1 cascade was also removed, and the FIC
The opening degree of the -1 control valve is kept constant. Prior to the Hv-1 switching operation, the following items are determined using a computer.
切換時の加熱炉の負荷から燃料LPGの所要流量と、こ
の流量に調節できるFIC−1調節弁の弁開度。The required flow rate of fuel LPG based on the load on the heating furnace at the time of switching, and the valve opening degree of the FIC-1 control valve that can be adjusted to this flow rate.
燃料LPGの1次圧力とHV−1からバーナ迄の容積及
びFIC−1調節弁のCv等からLPGがHV−1を出
てバーナに到達する迄の時間。The time it takes for LPG to leave HV-1 and reach the burner based on the primary pressure of the fuel LPG, the volume from HV-1 to the burner, and the Cv of the FIC-1 control valve.
以上の計算が終れば三方弁を切替操作しLPGを燃料管
路に導入する管路内は上流部からLPGによりピストン
フロー的に置換され、前記の計算で求めた到達時間後に
バーナに到達するが、この時点でFIC−1の調節弁の
弁開度は前記の計算で求めた開度に調整されるので、加
熱炉負荷に相当するLPGの流量がバーナに供給される
。燃料切替後、加熱炉周りの運転状態に異常がなく正常
運転が確認されれば、FIC−1のフィードバック制御
及びTlC−1によるカスケード制御を復帰する。切替
に要する時間は従来法に較べれば非常に短く数10秒以
下であり、切替中も特に異常は見られなかった。Once the above calculations are completed, the three-way valve is switched and LPG is introduced into the fuel pipe.The inside of the pipe is replaced by LPG from the upstream part in a piston flow manner, and it reaches the burner after the arrival time determined by the above calculation. At this point, the opening degree of the control valve of FIC-1 is adjusted to the opening degree determined by the above calculation, so that the flow rate of LPG corresponding to the heating furnace load is supplied to the burner. After switching the fuel, if there is no abnormality in the operating state around the heating furnace and normal operation is confirmed, the feedback control of FIC-1 and the cascade control by TIC-1 are restored. The time required for switching was very short compared to the conventional method, less than several tens of seconds, and no abnormalities were observed during the switching.
以上の実施例は都市ガスからLPGへの切替の例である
が、LPGから都市ガスへの切替の場合も全く同じ手順
で行い得るし、本発明はその他の種類の化石燃料につい
ても適用できることは言う迄もない。Although the above embodiment is an example of switching from city gas to LPG, switching from LPG to city gas can be performed using exactly the same procedure, and the present invention can also be applied to other types of fossil fuels. Needless to say.
(効果)
以上説明した本発明の燃料切替方法によれば、従来の方
法に較べて非常に短い時間で、しかも自動的に切替える
ことができるので、運転の省力化を図りつるという効果
が得られる。(Effects) According to the fuel switching method of the present invention described above, the fuel switching can be performed automatically in a much shorter time than the conventional method, so that the effect of saving labor in driving can be obtained. .
第1図は本発明を加熱炉に実施した場合の系統図であり
、第2図は従来の2系統の燃料供給システムの系統図で
ある。
以上FIG. 1 is a system diagram when the present invention is implemented in a heating furnace, and FIG. 2 is a system diagram of a conventional two-system fuel supply system. that's all
Claims (1)
、切替え後の新しい燃料が切替弁からバーナ迄到達する
時間を求め、切替弁を切替えた時からこの到達時間経過
時に燃料の流量調節弁の弁開度を新しい燃料の所定流量
に必要な開度に瞬時に調整することを特徴とする加熱炉
等の燃料切替方法。In heating furnaces, etc. that use two types of fuel by switching them alternately, find the time it takes for new fuel to reach the burner from the switching valve after switching, and calculate the fuel flow rate when this arrival time has elapsed from the time the switching valve was switched. A fuel switching method for a heating furnace, etc., characterized in that the opening degree of a control valve is instantly adjusted to the opening degree required for a predetermined flow rate of new fuel.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16369989A JPH0754177B2 (en) | 1989-06-28 | 1989-06-28 | Fuel switching method for heating furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16369989A JPH0754177B2 (en) | 1989-06-28 | 1989-06-28 | Fuel switching method for heating furnace |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0331609A true JPH0331609A (en) | 1991-02-12 |
JPH0754177B2 JPH0754177B2 (en) | 1995-06-07 |
Family
ID=15778934
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP16369989A Expired - Fee Related JPH0754177B2 (en) | 1989-06-28 | 1989-06-28 | Fuel switching method for heating furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0754177B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2013076510A (en) * | 2011-09-30 | 2013-04-25 | Miura Co Ltd | Gas supplying apparatus and combustion system |
-
1989
- 1989-06-28 JP JP16369989A patent/JPH0754177B2/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2013076510A (en) * | 2011-09-30 | 2013-04-25 | Miura Co Ltd | Gas supplying apparatus and combustion system |
Also Published As
Publication number | Publication date |
---|---|
JPH0754177B2 (en) | 1995-06-07 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
LAPS | Cancellation because of no payment of annual fees |