JPS6021765B2 - Gas temperature and flow rate control device - Google Patents

Gas temperature and flow rate control device

Info

Publication number
JPS6021765B2
JPS6021765B2 JP55056757A JP5675780A JPS6021765B2 JP S6021765 B2 JPS6021765 B2 JP S6021765B2 JP 55056757 A JP55056757 A JP 55056757A JP 5675780 A JP5675780 A JP 5675780A JP S6021765 B2 JPS6021765 B2 JP S6021765B2
Authority
JP
Japan
Prior art keywords
gas
temperature
flow rate
air supply
exhaust
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
Application number
JP55056757A
Other languages
Japanese (ja)
Other versions
JPS56152733A (en
Inventor
昌弘 桑原
博通 金田
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.)
KUROI KOSAN KK
Original Assignee
KUROI KOSAN KK
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 KUROI KOSAN KK filed Critical KUROI KOSAN KK
Priority to JP55056757A priority Critical patent/JPS6021765B2/en
Publication of JPS56152733A publication Critical patent/JPS56152733A/en
Publication of JPS6021765B2 publication Critical patent/JPS6021765B2/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/80Forming a predetermined ratio of the substances to be mixed
    • B01F35/82Forming a predetermined ratio of the substances to be mixed by adding a material to be mixed to a mixture in response to a detected feature, e.g. density, radioactivity, consumed power or colour

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Accessories For Mixers (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) この発明は、気体特に加熱気体の流量と温度を一定にす
るための自動制御装置に関する。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to an automatic control device for keeping the flow rate and temperature of gas, particularly heated gas, constant.

(従来の技術) 従来、熱処理炉(塗工機、乾燥炉)の温度は、120〜
2000○で使用され、温度制御範囲は±5℃であるが
、排ガス中には有害ガス(可燃性ガス)と多くのタール
物質を含み、禾処理で循環すると省エネルギーにはなる
が、不純物を多く含むので、製品に悪影響を及ぼし、製
品の歩留りを悪くするものである。
(Prior art) Conventionally, the temperature of a heat treatment furnace (coating machine, drying furnace) is 120 to
2000○, and the temperature control range is ±5℃, but the exhaust gas contains harmful gas (flammable gas) and a lot of tar substances, and although it saves energy when it is circulated through slag treatment, it also contains a lot of impurities. This has an adverse effect on the product and reduces the yield of the product.

そこで、不純物を除去する方法として、触媒式、直接燃
焼法等による除去装置を設け、この装置を介して浄化し
た気体(空気)を熱処理炉に再循環して利用しようとし
たのであるが、不純物自体の酸化、分解熱のために温度
変動が大きく、排ガスは浄化されても実際に使用するこ
とができない。このために、再循環使用する場合には、
熱処理温度に影響がない範囲において、主燃料系統を制
御するか、若しくは高温排ガスの一部を排出し、温度の
みの制御(この場合、熱交換器を設ける。
Therefore, as a method of removing impurities, we installed a removal device using a catalytic type, direct combustion method, etc., and tried to recirculate the purified gas (air) through this device to the heat treatment furnace. Due to its own oxidation and decomposition heat, temperature fluctuations are large, and even if the exhaust gas is purified, it cannot be used. For this reason, when using recirculation,
The main fuel system is controlled within a range that does not affect the heat treatment temperature, or a portion of the high-temperature exhaust gas is discharged, and only the temperature is controlled (in this case, a heat exchanger is provided).

)をする方法が採用されているが、浄化された排ガス全
量を再利用するには、温度と流量をともに制御しなけれ
ば使用が困難となるものである。すなわち、流量と温度
をともに調整するには、流出側の検知部に流出する気体
が一定状態にあることが条件となるが、全体として不安
定な気体では検知も不可能であり制御も困難である。ま
た、これを一定とするには気体の流れる方向に長い距離
をもつ装置が必要となるなどの欠点があるものである。
(発明が解決しようとする問題点) この発明は、上記従釆のものの改良にかかり、再循環使
用する際の設置コストが安価であって、装置全体の容量
を小さいものとし、かつ、温度変動を±3%以内に、更
に流量、温度も3%以内に制御することにより、再循環
を可能にしようとするものである。
), but in order to reuse the entire amount of purified exhaust gas, it is difficult to use it unless both the temperature and flow rate are controlled. In other words, in order to adjust both the flow rate and temperature, it is necessary that the gas flowing out to the detection part on the outflow side be in a constant state, but if the gas is unstable as a whole, it is impossible to detect and control is difficult. be. Another drawback is that in order to keep this constant, a device having a long distance in the direction of gas flow is required.
(Problems to be Solved by the Invention) The present invention improves the above-mentioned subordinates, reduces the installation cost when using recirculation, reduces the overall capacity of the device, and reduces temperature fluctuations. The aim is to enable recirculation by controlling the flow rate and temperature within ±3%, and also by controlling the flow rate and temperature within 3%.

(問題点を解決するための手段) そこで、装置内部のほぼ中間に、熱処理炉より流入する
不純物を除いた気体(空気)と外部より供給される気体
(空気)を均一に混合してこの漁合気体を設定温度とし
た上、流量を一定にする隔壁部分を設け、流出側に温度
、流量を一定とした気体を流出させて、温度検知を容易
にし調整を可能としたものである。
(Means for solving the problem) Therefore, the gas (air) from which impurities flowing in from the heat treatment furnace and the gas (air) supplied from the outside are uniformly mixed approximately in the middle of the inside of the equipment, and the gas (air) supplied from outside is mixed uniformly. In addition to setting the temperature of the amalgam, a partition wall is provided to keep the flow rate constant, and gas with a constant temperature and flow rate flows out to the outflow side, making it easy to detect and adjust the temperature.

なお、流入側の気体はある圧力をもつものである。(作
用) 上記の構成とすることにより、装置の流入側より加圧気
体が流入すると、同時に給気側より気体が補給されて、
所定温度の気体となるように均一に混合された後、給気
量と同一質量が排気管より排出されて、この気体は定方
向、定温の一定流速の流れとして流出側より排出される
ものであり、流出側のどの位置でも同一条件で温度の検
知ができるので、これをどの位置においてでも検知して
、上記給気、排気量を調整することができる。
Note that the gas on the inflow side has a certain pressure. (Function) With the above configuration, when pressurized gas flows in from the inflow side of the device, gas is simultaneously replenished from the air supply side.
After being uniformly mixed to form a gas at a predetermined temperature, a mass equal to the amount of air supplied is discharged from the exhaust pipe, and this gas is discharged from the outflow side as a flow in a fixed direction, at a constant temperature, and at a constant flow rate. Since the temperature can be detected under the same conditions at any position on the outflow side, the air supply and exhaust amounts can be adjusted by detecting this at any position.

(実施例)これを図面に示す実施例により説明すると、
1は装置本体であり、装置1の内部を2区画に分け、そ
れぞれの中心部分に新規な空気を外部より導入する給気
管2と一部排気するための排気管3を設ける。
(Example) This will be explained using an example shown in the drawings.
Reference numeral 1 denotes a main body of the device, and the inside of the device 1 is divided into two sections, and the central portion of each section is provided with an air supply pipe 2 for introducing new air from the outside and an exhaust pipe 3 for partially exhausting air.

装置1の左方が流入側Aであり、右方が流出側Bで、矢
印方向に空気が流れるものである。4は流出側Bに設け
る温度検知部でCA線230保護管付熱電対を用いる。
The left side of the device 1 is an inflow side A, and the right side is an outflow side B, in which air flows in the direction of the arrow. 4 is a temperature detection section provided on the outflow side B, which uses a thermocouple with a CA wire 230 protection tube.

5は給気管2に設けるバタフライダンパーで、比例式コ
ントロールモータ6により作動される。
Reference numeral 5 denotes a butterfly damper provided in the air supply pipe 2, which is operated by a proportional control motor 6.

7は熱処理炉(乾燥炉)より送られた空気が浄化されて
流入側Aより流入し、給気管2より供給される空気と混
合する混合室であり、混合に当り、混合室7内は貧圧に
しているため、給気管2よりの導入は自然導入である。
7 is a mixing chamber where the air sent from the heat treatment furnace (drying furnace) is purified, flows in from the inflow side A, and is mixed with the air supplied from the air supply pipe 2. During mixing, the inside of the mixing chamber 7 is Since the pressure is maintained, the introduction from the air supply pipe 2 is a natural introduction.

したがって、混合室7内の圧力は、バタフライダンパー
5と微調整ダンパー8の圧力損失約1仇吻Ag(水柱)
以上の負圧としなければならない。9は調整室であり、
上部には前記一部排気用の排気管3を設け、比例式コン
トロールモータ6により作動されるバタフライダンパー
12、微調整ダンパ−13を設け、これよりは、流出側
の排出流量を一定とするため、給気管2より供給される
流量分を排出するようになっている。
Therefore, the pressure in the mixing chamber 7 is approximately 1 to 1 Ag (water column) due to the pressure loss between the butterfly damper 5 and the fine adjustment damper 8.
The negative pressure must be greater than or equal to 9 is a control room;
The exhaust pipe 3 for partial exhaust is provided in the upper part, and a butterfly damper 12 and a fine adjustment damper 13 operated by a proportional control motor 6 are provided to keep the discharge flow rate on the outflow side constant. , the amount of flow supplied from the air supply pipe 2 is discharged.

調整室9と混合室7間には、均一混合、定流量部として
の隔壁を設け、この実施例では、無孔鋼板よりなるそら
せ板10と多孔板11によりこれを構成する。そらせ板
10は、垂直方向、上端より約25%の面積を占め、こ
れは、給排気時のシートパス(給気管2より排気管3へ
の通過)を阻止し、両気体の混合方向を直角として混合
を有効にするためのものであり、多孔板11は上記そら
せ板10の下端より垂直方向の全てを占めており、流入
気体の勤圧の大きい場合や、高温気体の時には混合室7
での均一混合が困難であるので、気体流の動圧を静庄に
変換し、多孔板1 1よりの吹出速度分布を均一化する
ためのものである。外気温の変動により、流量が変化し
、設定温度に誤差が生じ、流量の調整が必要となる時に
は、バタフライダンパー5,12だけでは微調整が困難
となるので、給排気系の微調整ダンパー8.13により
徴調整を行い設定精度を向上させている。
A partition wall is provided between the adjustment chamber 9 and the mixing chamber 7 as a uniform mixing and constant flow section, and in this embodiment, it is constituted by a deflecting plate 10 made of a non-perforated steel plate and a perforated plate 11. The deflector plate 10 occupies approximately 25% of the area from the upper end in the vertical direction, and blocks the sheet pass (passage from the air supply pipe 2 to the exhaust pipe 3) during air supply and exhaust, and prevents the mixing direction of both gases from perpendicular to each other. The perforated plate 11 occupies the entire area in the vertical direction from the lower end of the baffle plate 10, and is used to close the mixing chamber 7 when the pressure of the incoming gas is high or when the gas is at a high temperature.
Since it is difficult to achieve uniform mixing in the perforated plate 11, the purpose is to convert the dynamic pressure of the gas flow into static pressure and make the blowing velocity distribution from the perforated plate 11 uniform. When the flow rate changes due to fluctuations in outside temperature and an error occurs in the set temperature, and the flow rate needs to be adjusted, fine adjustment is difficult with just the butterfly dampers 5 and 12, so the fine adjustment damper 8 of the air supply and exhaust system is used. .13 was used to improve the setting accuracy.

このような構成であるから、流入側Aの前方において気
体に温度変動が生じた場合、その気体の温度を流出部B
の温度検知部が温度検知し、装置制御系の温度指示調節
系にフィードバックし給気管2のコントロールダンパー
5を比例式コントロールモ−夕6により、作動させ、混
合室7に両気体を導入し、混合拡散を行う。
With this configuration, if a temperature change occurs in the gas in front of the inflow side A, the temperature of the gas is changed to the outflow side B.
The temperature detection unit detects the temperature, feeds it back to the temperature indication adjustment system of the device control system, operates the control damper 5 of the air supply pipe 2 by the proportional control motor 6, and introduces both gases into the mixing chamber 7. Perform mixed diffusion.

そらせ板10‘こより給気管2より導入する気体は、排
気管3に直接連絡して排気されることがなく、混合室7
内に給気を誘導し均一に混合させるものである。ここで
均一の温度となった気体(空気)は、多孔板11の孔よ
り噴出させられるが、これにより一定流量に強制させら
れ、余剰の流量分は、排気管3より排出されるので、流
出側より排出される気体は、流出側のすべての部分にお
いて均一の所定温度で、所定流量のものとなるものであ
る。第3図は、この菱贋を挿入する再循環システムを概
略示すものである。
The gas introduced from the air supply pipe 2 through the baffle plate 10' is not directly connected to the exhaust pipe 3 and exhausted, but instead flows into the mixing chamber 7.
This is to guide the supply air into the tank and mix it uniformly. The gas (air) that has reached a uniform temperature is ejected from the holes in the perforated plate 11, but is forced to maintain a constant flow rate. The gas discharged from the side has a uniform predetermined temperature and a predetermined flow rate in all parts of the outflow side. FIG. 3 schematically shows the recirculation system for inserting this diamond counterfeit.

1はこの発明の装置であり、Cは熱処理炉例えば乾燥炉
、Dは触媒装置、8はファン、Fは弁、Gは熱処理炉C
より触媒装置Dに、排ガスを案内する管路であり、この
管路G内を流れる気体は不純物を含有するものである。
1 is an apparatus of the present invention, C is a heat treatment furnace such as a drying furnace, D is a catalyst device, 8 is a fan, F is a valve, and G is a heat treatment furnace C.
This is a pipe that guides exhaust gas to the catalyst device D, and the gas flowing through this pipe G contains impurities.

日は設定温度と流量とされた気体を熱処理炉C内に再循
環するための管路である。熱処理炉Cより生ずる不純物
を含む排ガスは、触媒装置D内において、不純物を除去
されるが、上記のように酸化、分解熱のために高温とな
って排出されるので、これをこの発明の装置1の流入側
Aに送り込む。
The line is a pipe for recirculating gas at a set temperature and flow rate into the heat treatment furnace C. The exhaust gas containing impurities generated from the heat treatment furnace C has its impurities removed in the catalyst device D, but as mentioned above, it is discharged at a high temperature due to the heat of oxidation and decomposition. 1 into the inflow side A.

そして、外部よりの空気(oo〜40qo)を供給し、
均一混合した上、定流量の定方向の流れとして流出側よ
り排出する。そこで、これを再循環して乾燥炉に送り込
めば、一定温度であるから乾燥炉の加熱も設定温度とす
るだけでよく制御する必要がなく、排ガスを再利用する
ことができ、しかも、その装置は極めて小さいものとす
ることができる。(発明の効果) 以上のとおり、この発明は構成されるものであるから、
‘ィ’装置容量を小さくし、混合、拡散時間が短く、設
定値への復帰は短時間(実測では7分)である。
Then, supply air (oo~40qo) from the outside,
After uniform mixing, the mixture is discharged from the outflow side as a constant flow in a fixed direction. Therefore, if this is recirculated and sent to the drying oven, since the temperature is constant, there is no need to control the heating of the drying oven by just setting the temperature, and the exhaust gas can be reused. The device can be extremely small. (Effect of the invention) As described above, this invention consists of
'I' The capacity of the device is small, the mixing and diffusion times are short, and the return to the set value is short (actually measured in 7 minutes).

【oー 給排気管を設けているので設定温度を調整して
任意の温度に設定できる。
[o- Since the air supply and exhaust pipes are provided, the temperature setting can be adjusted and set to any desired temperature.

し一 高精度(±3%)の排ガスの再循環利用ができる
ので製品の歩留りを向上させる。
1. Since exhaust gas can be recirculated with high accuracy (±3%), product yield is improved.

B 設定値の変動が僅かなため、乾燥炉などの気体を加
熱するための燃料の消費を極力抑制することができる。
B: Since the set value fluctuates only slightly, consumption of fuel for heating gas in a drying oven or the like can be suppressed as much as possible.

偽 装置全体を小さくすることができるので、従来のも
のよりコストを低くすることができる。等の優れた効果
を具えるものである。
Since the entire device can be made smaller, the cost can be lower than that of conventional devices. It has excellent effects such as.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図はこの発明における1実施例の要都側断面図、第
2図は中間隔壁部分の正面図、第3図はこの発明の装置
を具える再循環システムを示す。 1……装置本体、2……給気管、3・・・…排気管、4
…・・・温度検知部、5,12・・・・・・バタフライ
ダンバ−、6・・・・・・比例式コントロールモータ、
7・・・…混合室、8,13・・・・・・微調整ダンパ
−、9・・・・・・調整室、10・・・・・・そらせ板
、11・・・・・・多孔板、A・・・・・・流入側、B
・・・・・・流出側、C・・・・・・乾燥炉、D・・・
・・・触媒袋贋、E・・・・・・ファン、F・・・・・
・弁、G,日・・・・・・管路。 第1図 第2図 第3図
FIG. 1 is a cross-sectional side view of an embodiment of the present invention, FIG. 2 is a front view of the intermediate wall section, and FIG. 3 is a recirculation system equipped with the device of the present invention. 1... Device body, 2... Air supply pipe, 3... Exhaust pipe, 4
...Temperature detection section, 5, 12 ... Butterfly damper, 6 ... Proportional control motor,
7... Mixing chamber, 8, 13... Fine adjustment damper, 9... Adjustment chamber, 10... Deflector plate, 11... Porous Plate, A...Inflow side, B
... Outlet side, C ... Drying oven, D ...
...Catalyst bag counterfeit, E...Fan, F...
・Valve, G, day...Pipeline. Figure 1 Figure 2 Figure 3

Claims (1)

【特許請求の範囲】[Claims] 1 流出側に設ける温度検知部により給排気量が調整さ
れる給排気管を具え、装置中間内部に気体流均一混合、
定流量隔壁部を設け、流入側よりの気体と給気管より供
給される気体を均一混合し、排気管より給気量と同一流
量を排出して、流入側における温度と温度調節のために
加えられる流量の変動を上記流出側において一定に制御
する気体の温度、流量制御装置。
1 Equipped with a supply and exhaust pipe whose supply and exhaust volume is adjusted by a temperature detection section installed on the outflow side, and a gas flow uniformly mixed inside the device,
A constant flow partition is provided to uniformly mix the gas from the inflow side and the gas supplied from the air supply pipe, and the same flow rate as the air supply is discharged from the exhaust pipe. A gas temperature and flow rate control device that controls fluctuations in the flow rate at a constant level on the outflow side.
JP55056757A 1980-04-28 1980-04-28 Gas temperature and flow rate control device Expired JPS6021765B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP55056757A JPS6021765B2 (en) 1980-04-28 1980-04-28 Gas temperature and flow rate control device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP55056757A JPS6021765B2 (en) 1980-04-28 1980-04-28 Gas temperature and flow rate control device

Publications (2)

Publication Number Publication Date
JPS56152733A JPS56152733A (en) 1981-11-26
JPS6021765B2 true JPS6021765B2 (en) 1985-05-29

Family

ID=13036372

Family Applications (1)

Application Number Title Priority Date Filing Date
JP55056757A Expired JPS6021765B2 (en) 1980-04-28 1980-04-28 Gas temperature and flow rate control device

Country Status (1)

Country Link
JP (1) JPS6021765B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62110966U (en) * 1985-12-27 1987-07-15
CN104492290A (en) * 2014-12-12 2015-04-08 中煤科工集团重庆研究院有限公司 Low-concentration coal gas blending device for coal mine

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62110966U (en) * 1985-12-27 1987-07-15
CN104492290A (en) * 2014-12-12 2015-04-08 中煤科工集团重庆研究院有限公司 Low-concentration coal gas blending device for coal mine

Also Published As

Publication number Publication date
JPS56152733A (en) 1981-11-26

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