JP7832012B2 - Intake and exhaust system for sintered ore cooler - Google Patents
Intake and exhaust system for sintered ore coolerInfo
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- JP7832012B2 JP7832012B2 JP2022023395A JP2022023395A JP7832012B2 JP 7832012 B2 JP7832012 B2 JP 7832012B2 JP 2022023395 A JP2022023395 A JP 2022023395A JP 2022023395 A JP2022023395 A JP 2022023395A JP 7832012 B2 JP7832012 B2 JP 7832012B2
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B1/00—Preliminary treatment of ores or scrap
- C22B1/26—Cooling of roasted, sintered, or agglomerated ores
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27B—FURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
- F27B21/00—Open or uncovered sintering apparatus; Other heat-treatment apparatus of like construction
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D3/00—Charging; Discharging; Manipulation of charge
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/25—Process efficiency
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Description
本発明は、複数のトラフ台車上に焼結機で焼結された焼結鉱を積層させ、前記複数のトラフ台車を移動させながら前記焼結鉱の層中に冷却ガスを通気することで連続的に前記焼結鉱を冷却する焼結鉱冷却機の給排気装置に関する。 This invention relates to a supply and exhaust system for a sintered ore cooling machine, which stacks sintered ore, sintered in a sintering machine, onto multiple trough troughs, and continuously cools the sintered ore by passing a cooling gas through the layers of sintered ore while moving the multiple trough troughs.
従来、複数のトラフ台車上に焼結機で焼結された焼結鉱を積層させ、これら複数のトラフ台車を移動させながら焼結鉱の層中に下方から上方に向けて冷却ガスを通気することで連続的に焼結鉱を冷却する焼結鉱冷却機が知られている。 Conventionally, a sintered ore cooling system is known that stacks sintered ore produced by a sintering machine onto multiple trough troughs, and continuously cools the sintered ore by passing a cooling gas from bottom to top through the layers of sintered ore while moving these trough troughs.
このような焼結鉱冷却機においては、昨今の環境規制の高まりから、焼結鉱粉塵の系外への漏洩を抑制するために、トラフ台車の上方の少なくとも一部をフードで覆い、密封を保つべくフードとトラフ台車との間にシール機構を設けるようになっている。 In such sintered ore coolers, due to recent increases in environmental regulations, at least a portion of the upper part of the trough carriage is covered with a hood to suppress leakage of sintered ore dust outside the system, and a sealing mechanism is provided between the hood and the trough carriage to maintain airtightness.
トラフ台車はレール上を走行する可動体であり、他方、フードは移動するトラフ台車上に固定設置される固定体であるため、シール機構はこれらが相対移動可能なように設けられる必要がある。このようなシール機構としては、例えば、長尺のクロス等のシール材の幅方向片側をシール材が下側に垂れ下がるように固定側のフードに取り付け、このシール材の下側をトラフ台車の側面に面接触させてフードとトラフ台車との隙間をシールする方法がある。また、特許文献1に開示されているように、水封ボックス内に溜めた水を用いてシールする水封式シールとするものもある。 The trough bogie is a movable body that travels on rails, while the hood is a fixed body that is permanently installed on the moving trough bogie. Therefore, the sealing mechanism needs to be designed to allow for relative movement between these two components. One such sealing mechanism involves attaching a long piece of sealing material, such as a cross-section, to the fixed hood so that one side of the sealing material hangs downwards, and then sealing the gap between the hood and the trough bogie by making surface contact with the side of the trough bogie. Another method, as disclosed in Patent Document 1, uses a water-seal type seal that utilizes water stored in a water-seal box.
しかし、クロスを用いる場合、経年劣化によるクロスの擦り切れやフードとトラフ台車との間の高さ方向、幅方向の隙間発生によりガスや粉塵が漏洩することがあった。特に、トラフ台車の側壁が変形したり、車輪の摩耗でトラフ台車が沈んだり、トラフ台車の車軸方向における偏心が発生して、トラフ台車とフードとの間の隙間が拡大すると、漏洩量が増加することになる。なお、機械的にこのようなシール材(クロス等)を常にシール面(トラフ台車)に押しあてる方法もあるが、シール面が波うち状に変形した場合、隙間が発生してガスや粉塵が漏洩しやすくなる。 However, when using cloth sealant, gas and dust could leak due to wear and tear of the cloth over time, or due to gaps developing in the height and width directions between the hood and the trough bogie. In particular, if the side walls of the trough bogie deform, the trough bogie sinks due to wheel wear, or the trough bogie becomes eccentric in the axle direction, the gap between the trough bogie and the hood widens, increasing the amount of leakage. While there are methods to mechanically press such sealing material (cloth, etc.) against the sealing surface (trough bogie), if the sealing surface deforms into a wavy shape, gaps will develop, making gas and dust more likely to leak.
また、水封式シールの場合、漏洩した焼結鉱が水封ボックス内に堆積すると、クーラ回転時の抵抗となったり、水封機能自体が失われたりすることがあった。 Furthermore, in the case of water-sealed seals, if leaked sintered ore accumulated inside the water-seal box, it could create resistance during cooler rotation or even cause the water-seal function itself to be lost.
本発明はかかる課題を解決するためになされたものであり、経年劣化等でトラフ台車側壁が沈んだり変形等してシール機構のシール効果が低下し、トラフ台車とフードの間に隙間が発生した場合にも、トラフ台車側(可動側)とフード側(固定側)との間のシール部分からガスや粉塵が系外に漏洩することを防止できる焼結鉱冷却機の給排気装置を提供することを目的としている。 This invention was made to solve the aforementioned problems, and aims to provide a supply and exhaust system for a sintered ore cooler that can prevent gas and dust from leaking out of the system from the sealing portion between the trough bogie side (movable side) and the hood side (fixed side), even when the sealing effect of the sealing mechanism decreases due to aging or other deterioration, resulting in a gap between the trough bogie and the hood.
(1)本発明に係る焼結鉱冷却機の給排気装置は、上方の少なくとも一部がフードで覆われた複数のトラフ台車上に焼結機で焼結された焼結鉱を積層させ、前記複数のトラフ台車を移動させながら前記焼結鉱の層中に冷却ガスを通気することで連続的に前記焼結鉱を冷却する焼結鉱冷却機の給排気装置であって、
前記冷却ガスを前記複数のトラフ台車の下方に供給するための冷却ガス圧送装置と、
前記フードで覆われた空間から排気ガスを吸引して外部に排出するための排気ガス吸引装置と、
前記冷却ガスの流量が前記排気ガスの流量よりも小さくなるように、前記冷却ガス圧送装置及び前記排気ガス吸引装置のうちの少なくともいずれか一方を制御するよう構成された制御装置と、
を備えることを特徴とするものである。
(1) The sintered ore cooling machine supply and exhaust device according to the present invention is a sintered ore cooling machine supply and exhaust device that stacks sintered ore sintered by a sintering machine on a plurality of trough troughs, at least a part of which is covered from above by a hood, and continuously cools the sintered ore by passing a cooling gas through the layers of sintered ore while moving the plurality of trough troughs,
A cooling gas pumping device for supplying the cooling gas to the lower part of the plurality of trough trolleys,
An exhaust gas suction device for drawing exhaust gas from the space covered by the aforementioned hood and discharging it to the outside,
A control device configured to control at least one of the cooling gas pumping device and the exhaust gas suction device such that the flow rate of the cooling gas is less than the flow rate of the exhaust gas,
It is characterized by having the following features.
(2)また、上記(1)に記載のものにおいて、前記冷却ガス圧送装置は、前記冷却ガスの流量を計測する冷却ガス流量計が設けられた圧送管を有し、
前記排気ガス吸引装置は、前記排気ガスの流量を計測する排気ガス流量計が設けられた排気管を有し、
前記圧送管と前記排気管のうちの少なくともいずれか一方に流量調整弁が設けられており、
前記制御装置は、前記冷却ガス流量計の計測値及び前記排気ガス流量計の計測値に基づいて、前記流量調整弁を制御するよう構成されていることが好ましい。
(2) In addition, in the case described in (1) above, the cooling gas pumping device has a pumping pipe equipped with a cooling gas flow meter for measuring the flow rate of the cooling gas,
The exhaust gas suction device has an exhaust pipe equipped with an exhaust gas flow meter for measuring the flow rate of the exhaust gas,
A flow control valve is provided in at least one of the pressure pipe and the exhaust pipe.
Preferably, the control device is configured to control the flow rate adjustment valve based on the measured values of the cooling gas flow meter and the exhaust gas flow meter.
(3)また、上記(2)に記載のものにおいて、前記制御装置が、漏風量に基づいて、(前記排気ガスの流量)≧(前記冷却ガスの流量)-(前記漏風量)の関係を満たすように前記冷却ガス流量調整弁と前記排気ガス流量調整弁とを制御するよう構成されていることが好ましい。 (3) Furthermore, in the device described in (2) above, it is preferable that the control device is configured to control the cooling gas flow rate control valve and the exhaust gas flow rate control valve based on the amount of air leakage, such that the relationship (flow rate of exhaust gas) ≥ (flow rate of cooling gas) - (amount of air leakage) is satisfied.
(4)また、上記(1)~(3)のいずれかに記載のものにおいて、前記複数のトラフ台車のうちの少なくとも1つからなるトラフ台車群ごとに、前記フードで覆われた空間内の圧力を測定するための圧力計と、前記流量調整弁とが設けられ、
前記制御装置は、前記圧力計から得られた圧力値に基づいて、フードで覆われた空間内の圧力が大気圧以上となった前記トラフ台車群について、前記排気ガスの流量を大きくするように前記流量調整弁を制御するよう構成されていることが好ましい。
(4) In addition, in any of the above (1) to (3), each trough trough group consisting of at least one of the plurality of trough troughs is provided with a pressure gauge for measuring the pressure in the space covered by the hood and the flow control valve,
Preferably, the control device is configured to control the flow rate adjustment valve to increase the flow rate of the exhaust gas for the trough trolley group when the pressure in the space covered by the hood exceeds atmospheric pressure, based on the pressure value obtained from the pressure gauge.
(5)また、上記(1)~(4)のいずれかに記載のものにおいて、前記フードに接続され、前記フードで覆われた空間内に空気を取り込むガス流入管を更に備えていることが好ましい。 (5) Furthermore, in any of the above descriptions (1) to (4), it is preferable that a gas inlet pipe is further provided, which is connected to the hood and draws air into the space covered by the hood.
(6)また、上記(5)に記載のものにおいて、前記ガス流入管に、前記フードで覆われた空間から外部に向かう方向のガスの流れを防ぐ逆止弁が設けられていることが好ましい。 (6) Furthermore, in the device described in (5) above, it is preferable that the gas inlet pipe is provided with a check valve to prevent the flow of gas from the space covered by the hood toward the outside.
(7)また、上記(5)又は(6)に記載のものにおいて、前記ガス流入管は、内径、前記フード内の部分の長さ及び肉厚のそれぞれが所定の範囲内の寸法であることが好ましい。 (7) Furthermore, in the case described in (5) or (6) above, it is preferable that the inner diameter, the length of the portion within the hood, and the wall thickness of the gas inlet pipe are all within a predetermined range.
本発明によれば、トラフ台車とフードとの間の空間全体を安定して負圧に維持することが可能となり、経年劣化等でトラフ台車側壁が沈んだり変形したりしてトラフ台車とフードの間に隙間が発生した場合にも、トラフ台車側(可動側)とフード側(固定側)との間のシール部分からガスや粉塵が系外に漏洩することを防止することができる。 According to the present invention, it is possible to maintain a stable negative pressure throughout the entire space between the trough trough and the hood. Even if the trough trough sidewalls sink or deform due to aging or other factors, creating a gap between the trough trough and the hood, it is possible to prevent gas and dust from leaking out of the system through the seal between the trough trough side (movable side) and the hood side (fixed side).
本実施の形態に係る焼結鉱冷却機1の給排気装置3は、図1に示すように、冷却ガスをトラフ台車5の下方に供給するための冷却ガス圧送装置7と、排気ガスを吸引して外部に排出するための排気ガス吸引装置9と、冷却却ガスの流量と排気ガスの流量を制御する制御装置11とを備えている。本実施形態においては、DCS(Distributed Control System)である。
以下、各装置構成を詳細に説明する。
As shown in Figure 1, the supply and exhaust device 3 of the sintered ore cooler 1 according to this embodiment includes a cooling gas pumping device 7 for supplying cooling gas to the lower part of the trough carriage 5, an exhaust gas suction device 9 for sucking in exhaust gas and discharging it to the outside, and a control device 11 for controlling the flow rate of the cooling gas and the flow rate of the exhaust gas. In this embodiment, it is a DCS (Distributed Control System).
The configuration of each device will be described in detail below.
<焼結鉱冷却機>
焼結鉱冷却機1は、上方の少なくとも一部がフード13で覆われた複数のトラフ台車5上に焼結機で焼結された焼結鉱15を積層させ、複数のトラフ台車5を移動させながら焼結鉱15の層中に冷却ガスを通気することで連続的に焼結鉱15を冷却するものである。
<Sintered Ore Cooler>
The sintered ore cooler 1 stacks sintered ore 15, which has been sintered in a sintering machine, on a plurality of trough troughs 5, at least a portion of which is covered by a hood 13, and continuously cools the sintered ore 15 by passing cooling gas through the layers of sintered ore 15 while moving the plurality of trough troughs 5.
トラフ台車5は、車輪17と、トラフ19と、内側側壁21および外側側壁23と、風箱25と、通気板27とを備えており、通気板27の上方に粉砕された焼結鉱15が積層されている。
トラフ台車5は、円環状に区画された領域を、レール(図示なし)に沿って、給鉱装置側から排鉱装置側へと移動する。
固定体であるフード13と可動体であるトラフ台車5との間にはシール機構28が設けられており、この部分がシール部分となる。
The trough bogie 5 is equipped with wheels 17, a trough 19, an inner side wall 21 and an outer side wall 23, a wind box 25, and a ventilation plate 27, with crushed sintered ore 15 stacked above the ventilation plate 27.
The trough carriage 5 moves along the rails (not shown) within a circularly partitioned area, from the ore supply unit side to the ore discharge unit side.
A sealing mechanism 28 is provided between the fixed hood 13 and the movable trough bogie 5, and this part constitutes the sealing portion.
<冷却ガス圧送装置>
冷却ガス圧送装置7は、冷却ガスの流量を計測する冷却ガス流量計F1が設けられた圧送管29を有し、冷却ガスを複数のトラフ台車5の下方に供給するためのものである。
圧送管29の上流側には冷却ガスを圧送して供給するための供給ブロワ8が設けられ、その下流側は、図1に示すように、固定側環状エアダクト31に接続され、固定側環状エアダクト31は水封ボックス33を介して可動側環状エアダクト35と接続され、可動側環状エアダクト35は連結エアダクト37を介して内側側壁21に接続されている。
<Cooling gas pumping system>
The cooling gas pumping device 7 has a pumping pipe 29 equipped with a cooling gas flow meter F1 for measuring the flow rate of the cooling gas, and is for supplying cooling gas to the lower part of multiple trough trolleys 5.
Upstream of the pressure pipe 29 is a supply blower 8 for supplying cooling gas under pressure. Downstream of the supply blower 8 is connected to a fixed annular air duct 31, as shown in Figure 1. The fixed annular air duct 31 is connected to a movable annular air duct 35 via a water seal box 33, and the movable annular air duct 35 is connected to the inner side wall 21 via a connecting air duct 37.
圧送管29から固定側環状エアダクト31に供給された冷却ガスは、水封ボックス33によってシールされて可動側環状エアダクト35、連結エアダクト37を介して風箱25に供給される。 The cooling gas supplied from the pressure pipe 29 to the fixed annular air duct 31 is sealed by the water seal box 33 and supplied to the wind box 25 via the movable annular air duct 35 and the connecting air duct 37.
圧送管29に設けられた冷却ガス流量計F1の計測値は、制御装置11に入力される。 The measured value from the cooling gas flow meter F1 installed in the pressure pipe 29 is input to the control device 11.
<排気ガス吸引装置>
排気ガス吸引装置9は、排気ガスの流量を計測する排気ガス流量計F2が設けられた排気管41を有し、フード13で覆われた空間から排気ガスを吸引して外部に排出するためのものである。排気管41には、排気ガスの流量を調整する流量調整弁39が設けられている。
排気管41の下流側には排気ガスを吸引して排出するための排出ブロワ10が設けられている。排気管41に設けられた排気ガス流量計F2の計測値も、制御装置11に入力される。
<Exhaust gas suction device>
The exhaust gas suction device 9 has an exhaust pipe 41 equipped with an exhaust gas flow meter F2 for measuring the flow rate of exhaust gas, and is designed to suck exhaust gas from the space covered by the hood 13 and discharge it to the outside. The exhaust pipe 41 is equipped with a flow control valve 39 for adjusting the flow rate of exhaust gas.
A discharge blower 10 is provided downstream of the exhaust pipe 41 to draw in and discharge exhaust gas. The measured value from the exhaust gas flow meter F2 installed on the exhaust pipe 41 is also input to the control device 11.
<制御装置>
制御装置11は、冷却ガスの流量が排気ガスの流量よりも小さくなるように流量調整弁39を制御するよう構成されている。
具体的には、流量計F1、F2の計測値を入力し、その計測値に基づいて、排気管41を流れる排気ガスの流量が圧送管29から供給される冷却ガス流量よりも大きくなるように流量調整弁39を制御する。
<Control device>
The control device 11 is configured to control the flow control valve 39 so that the flow rate of the cooling gas is less than the flow rate of the exhaust gas.
Specifically, the measured values from flow meters F1 and F2 are input, and based on these measured values, the flow control valve 39 is controlled so that the flow rate of exhaust gas flowing through the exhaust pipe 41 is greater than the flow rate of cooling gas supplied from the pressure pipe 29.
集塵装置等を介してフード13内の排気ガスを吸引する場合、フード13に接続する配管から離れたエリアでは排気ガスの吸引力が弱く、フード内圧力が大気圧より高くなるとガスや粉塵が漏洩する条件となりやすい。
そこで、制御装置11によって、冷却ガスの流量が排気ガスの流量よりも小さくなるように流量調整弁39とを制御することで、フード内圧力が大気圧より低くすることができる。
When exhaust gas from inside the hood 13 is drawn in via a dust collector or the like, the suction force of the exhaust gas is weak in areas far from the piping connected to the hood 13, and conditions for gas and dust leakage are likely to occur when the pressure inside the hood becomes higher than atmospheric pressure.
Therefore, the control device 11 controls the flow rate of the cooling gas and the flow control valve 39 so that the flow rate of the exhaust gas is less than the flow rate of the exhaust gas, thereby making the pressure inside the hood lower than atmospheric pressure.
以上のように構成された本実施の形態の焼結鉱冷却機の給排気装置3によれば、トラフ台車5とフード13との間の空間全体を安定して負圧に維持することが容易となり、経年劣化等でトラフ台車5の側壁21、23が沈んだり変形したりしてシール機構のシール効果が低下し、トラフ台車5とフード13の間に隙間が発生した場合にも、トラフ台車5側(可動側)とフード13側(固定側)との間のシール部分からガスや粉塵が系外に漏洩することを防止することができる。 As described above, the exhaust and supply system 3 of the sintered ore cooler according to this embodiment makes it easy to maintain a stable negative pressure throughout the entire space between the trough carriage 5 and the hood 13. Even if the side walls 21 and 23 of the trough carriage 5 sink or deform due to aging or other factors, reducing the sealing effect of the sealing mechanism and creating a gap between the trough carriage 5 and the hood 13, it is possible to prevent gas and dust from leaking out of the system from the sealing portion between the trough carriage 5 side (movable side) and the hood 13 side (fixed side).
[変形例1]
経時変化によるトラフ台車5とフード13の間の隙間の発生や拡大は、トラフ台車5に対して無作為に発生する可能性がある。
この場合、図2、図3に示すように、個々のトラフ台車5または複数のトラフ台車5からなるトラフ台車群ごとに、フード13で覆われた空間内の圧力を測定するための圧力計Pと流量調整弁39とを設け、圧力計Pの計測値である圧力値を制御装置11に入力し、フード13で覆われた空間内の圧力が大気圧以上となった箇所(トラフ台車群)について、流量調整弁39を調整して、排気ガスの流量を大きくする。これによって、ピンポイントで漏洩を防止することができ、より経済的となる。
また、各フード13から集められた排気ガス流量の総量が、(排気ガス流量の総量)>(冷却ガス流量)の関係を満たさない場合は、大気圧とフード13内圧との圧力差(大気圧―フード13内圧)が小さいものから排ガス流量調整弁の開度を大きくすることが好ましい。
[Variation 1]
The formation or expansion of gaps between the trough bogie 5 and the hood 13 due to changes over time may occur randomly with respect to the trough bogie 5.
In this case, as shown in Figures 2 and 3, each individual trough trough 5 or a group of trough troughs 5 is provided with a pressure gauge P and a flow control valve 39 for measuring the pressure in the space covered by the hood 13. The pressure value measured by the pressure gauge P is input to the control device 11, and the flow control valve 39 is adjusted to increase the flow rate of exhaust gas in the locations (trough trough groups) where the pressure in the space covered by the hood 13 exceeds atmospheric pressure. This makes it possible to prevent leakage at specific points and is more economical.
Furthermore, if the total amount of exhaust gas flow collected from each hood 13 does not satisfy the relationship (total amount of exhaust gas flow) > (cooling gas flow), it is preferable to increase the opening of the exhaust gas flow control valve starting with the one with the smallest pressure difference between atmospheric pressure and the internal pressure of the hood 13 (atmospheric pressure - internal pressure of the hood 13).
[変形例2]
冷却ガスの流量に比べて排気ガスの流量が過多になると、フード13で覆われた空間内と外部との間の圧力差が大きくなり、シール部分の変形や外部空気の吸い込み、機器変形の可能性がある。また、シール部分から外部空気の吸い込みが大きくなると、排熱回収温度が低下し、ボイラーでの熱交換に支障をきたす。
そこで、図4に示すように、フード13で覆われた空間内に空気を取り込むガス流入管43をフード13に設けることにより、排気ガス流量が一時的に過多となった際にガス流入管43から外気空気を積極的に吸い込み、フード13内外の圧力差を低減させ、フード13内を常に大気圧に近い状態に維持することができる。
[Modified example 2]
If the exhaust gas flow rate is excessive compared to the cooling gas flow rate, the pressure difference between the space covered by the hood 13 and the outside will increase, potentially leading to deformation of the seal, intake of outside air, and deformation of the equipment. Furthermore, if there is a large intake of outside air from the seal, the exhaust heat recovery temperature will decrease, hindering heat exchange in the boiler.
Therefore, as shown in Figure 4, by providing a gas inlet pipe 43 in the hood 13 that takes in air into the space covered by the hood 13, when the exhaust gas flow rate temporarily becomes excessive, outside air can be actively drawn in through the gas inlet pipe 43, reducing the pressure difference between the inside and outside of the hood 13 and maintaining the inside of the hood 13 at a constant pressure close to atmospheric pressure.
ガス流入管43を設ける場合、ガス流入管43における一定以上の長さをフード13内に収められるようにすることで、流入した外部空気がフード13内に収められたガス流入管43内を流れる過程で加熱され、排気ガスの温度低下を抑制することができる。
ガス流入管43の内径、フード13内の部分の長さ及び肉厚のそれぞれが所定の範囲内の寸法であることが望ましく、例えば、内径:0.1~0.5m、フード13内の部分の長さ:0.5m以上、肉厚5mm以上といった範囲内の寸法に設定することが望ましい。内径が小さいすぎると管流入時の圧力損失が増大し、大きすぎると瞬間的に排気ガス温度の低下を招く恐れがある。また、フード13内の部分の長さが短いと流入した外部空気が十分に加熱されない。また、一定程度以上の肉厚を有することで、ガス流入管43を流れる空気の流量が小さい通常運転の間に熱を溜めておく熱容量が確保でき、ガス流入管43からの外部空気の流入量が増大した際のフード13で覆われた空間内の温度低下を抑制する効果が大きくなる。尚、流入管43のフード13内の部分の長さや肉厚の上限は、流入管43の内径に応じて重量等を勘案して妥当な範囲とする。
また、ガス流入管43の吸い込み側先端にフードで覆われた空間から外部に向かう方向のガスの流れを防ぐ逆止弁45やサイクロン(図示なし)を設置する等して、フード13内圧力が局所的に変動した時にも系外へのガスや粉塵の漏洩が防止されるようにしてもよい。
When a gas inlet pipe 43 is provided, by ensuring that a certain length or more of the gas inlet pipe 43 is contained within the hood 13, the incoming outside air is heated as it flows through the gas inlet pipe 43 contained within the hood 13, thereby suppressing the temperature drop of the exhaust gas.
It is desirable that the inner diameter of the gas inlet pipe 43, the length of the portion inside the hood 13, and the wall thickness are all within a predetermined range. For example, it is desirable to set the dimensions to be within the range of inner diameter: 0.1 to 0.5 m, length of the portion inside the hood 13: 0.5 m or more, and wall thickness: 5 mm or more. If the inner diameter is too small, the pressure loss when the pipe flows in will increase, and if it is too large, it may cause a momentary drop in exhaust gas temperature. Also, if the length of the portion inside the hood 13 is too short, the incoming outside air will not be sufficiently heated. Furthermore, having a wall thickness of a certain degree or more ensures that there is enough heat capacity to store heat during normal operation when the airflow rate through the gas inlet pipe 43 is low, and greatly reduces the effect of suppressing the temperature drop in the space covered by the hood 13 when the amount of outside air flowing in from the gas inlet pipe 43 increases. The upper limits of the length and wall thickness of the portion of the inlet pipe 43 inside the hood 13 should be set to a reasonable range considering the weight and other factors according to the inner diameter of the inlet pipe 43.
Furthermore, a check valve 45 or a cyclone (not shown) may be installed at the suction end of the gas inlet pipe 43 to prevent gas from flowing outwards from the space covered by the hood, thereby preventing leakage of gas and dust to the outside of the system even when the pressure inside the hood 13 fluctuates locally.
[変形例3]
トラフ台車5の下部のシール部分は、冷却ガスの漏風を完全に防止することができない。特に機器の経時劣化とともに冷却ガスの漏風が顕著となる。
そこで、冷却ガスの漏洩量を加味して、(排気ガス流量)≧(冷却ガス流量)-(漏風量)となるように制御することにより、排気ガス流量の最小値を小さくできる。これによって、排気ガス流量を低減することができ、排気ブロワ等の電力費の低減に繋がり、より経済的となる。
[Modification 3]
The seal at the bottom of the trough trough 5 cannot completely prevent cooling gas leakage. In particular, cooling gas leakage becomes more pronounced as the equipment deteriorates over time.
Therefore, by taking into account the amount of cooling gas leakage and controlling the system so that (exhaust gas flow rate) ≥ (cooling gas flow rate) - (leakage rate), the minimum value of the exhaust gas flow rate can be reduced. This reduces the exhaust gas flow rate, leading to a reduction in electricity costs for exhaust blowers and other equipment, making it more economical.
漏風量は、既知のデータから冷却ガス流量や圧力等を変数とする演算式から算出してもよく、また、図5に示すように、シール部等の漏洩箇所に風速計47を設けて風速を測定し、測定値を制御装置11に入力して、風速を漏風量に換算してもよい。
いずれにしても、制御装置11によって漏風量に基づいて、(排気ガスの流量)≧(冷却ガスの流量)-(漏風量)の関係を満たすように排気ガス流量調整弁39を制御するよう構成する。
The amount of air leakage may be calculated from known data using a formula that takes the cooling gas flow rate and pressure as variables. Alternatively, as shown in Figure 5, an anemometer 47 may be installed at the leakage point, such as the seal, to measure the wind speed, and the measured value may be input to the control device 11 to convert the wind speed into the amount of air leakage.
In any case, the control device 11 is configured to control the exhaust gas flow rate control valve 39 based on the amount of air leakage so that the relationship (flow rate of exhaust gas) ≥ (flow rate of cooling gas) - (amount of air leakage) is satisfied.
以上、本発明を実施形態及び変形例を用いて説明してきたが、本発明はこれらの実施形態や変形例の構成には限られない。本発明の範囲は添付の特許請求の範囲の記載に基づいて定まるものであり、その範囲内において実施形態や変形例に示した構成要素の一部の省略や変形、またそれらの改良を施した構成の全てが本発明に含まれる。 Although the present invention has been described above using embodiments and modifications, the present invention is not limited to the configurations of these embodiments and modifications. The scope of the present invention is determined based on the description in the appended claims, and within that scope, all configurations that omit, modify, or improve upon some of the components shown in the embodiments and modifications are included in the present invention.
例えば、上記の実施形態においては、流量調整弁39を排気管41のみに設けているが、流量調整弁は圧送管に設けてもよく、また、圧送管と排気管の両方に設けてもよい。 For example, in the above embodiment, the flow control valve 39 is provided only in the exhaust pipe 41, but the flow control valve may also be provided in the pressure pipe, or in both the pressure pipe and the exhaust pipe.
また、上記の実施形態においては、制御装置11は排気ガス吸引装置9(流量調整弁39)のみを制御するよう構成されているが、本発明においては、制御装置は、冷却ガスの流量が排気ガスの流量よりも小さくなるように、冷却ガス圧送装置を制御するよう構成されていても良く、また冷却ガス圧送装置及び排気ガス吸引装置の両方を制御するよう構成されていてもよい。 Furthermore, in the above embodiment, the control device 11 is configured to control only the exhaust gas suction device 9 (flow rate control valve 39). However, in the present invention, the control device may be configured to control the cooling gas pumping device so that the flow rate of the cooling gas is less than the flow rate of the exhaust gas, or it may be configured to control both the cooling gas pumping device and the exhaust gas suction device.
また、上記の実施形態においては、圧送管に冷却ガス流量計を設け、排気管に排気ガス流量計を設け、これらの計測値に基づいて流量調整弁を制御することで、高精度な制御を実現する好ましい形態を示したが、本発明においては、制御装置は、冷却ガスの流量が排気ガスの流量よりも小さくなるように、供給ブロワ及び排出ブロワのうちの少なくともいずれか一方を制御するよう構成されていてもよい。 Furthermore, while the above embodiment demonstrated a preferred configuration for achieving high-precision control by providing a cooling gas flow meter in the pressure pipe and an exhaust gas flow meter in the exhaust pipe, and controlling the flow control valve based on these measured values, the present invention may also be configured to control at least one of the supply blower and the discharge blower so that the flow rate of the cooling gas is less than the flow rate of the exhaust gas.
1 焼結鉱冷却機
3 給排気装置
5 トラフ台車
7 冷却ガス圧送装置
8 供給ブロワ
9 排気ガス吸引装置
10 排出ブロワ
11 制御装置
13 フード
15 焼結鉱
17 車輪
19 トラフ
21 内側側壁
23 外側側壁
25 風箱
27 通気板
28 シール機構
29 圧送管
31 固定側環状エアダクト
33 水封ボックス
35 可動側環状エアダクト
37 連結エアダクト
39 流量調整弁
41 排気管
43 ガス流入管
45 逆止弁
47 風速計
F1、F2 流量計
P 圧力計
1. Sintered ore cooler 3. Supply and exhaust system 5. Trough trolley 7. Cooling gas pressurizing system 8. Supply blower 9. Exhaust gas suction system 10. Discharge blower 11. Control device 13. Hood 15. Sintered ore 17. Wheels 19. Trough 21. Inner side wall 23. Outer side wall 25. Wind box 27. Ventilation plate 28. Seal mechanism 29. Pressurizing pipe 31. Fixed annular air duct 33. Water seal box 35. Movable annular air duct 37. Connecting air duct 39. Flow control valve 41. Exhaust pipe 43. Gas inlet pipe 45. Check valve 47. Anemometer F1, F2 Flow meter P. Pressure gauge
Claims (5)
前記冷却ガスを前記複数のトラフ台車の下方に供給するための冷却ガス圧送装置と、
前記フードで覆われた空間から排気ガスを吸引して外部に排出するための排気ガス吸引装置と、
前記冷却ガスの流量が前記排気ガスの流量よりも小さくなり、フード内圧力が大気圧よりも低くなるように、前記冷却ガス圧送装置及び前記排気ガス吸引装置のうちの少なくともいずれか一方を制御するよう構成された制御装置と、
を備え、
前記冷却ガス圧送装置は、前記冷却ガスの流量を計測する冷却ガス流量計が設けられた圧送管を有し、
前記排気ガス吸引装置は、前記排気ガスの流量を計測する排気ガス流量計が設けられた排気管を有し、
前記圧送管と前記排気管のうち少なくとも前記排気管に流量調整弁が設けられており、
前記複数のトラフ台車のうちの少なくとも1つからなるトラフ台車群ごとに、前記フードで覆われた空間内の圧力を測定するための圧力計と、前記流量調整弁とが設けられ、
前記制御装置は、前記冷却ガス流量計の計測値及び前記排気ガス流量計の計測値に基づいて、前記流量調整弁を制御するよう構成されており、且つ前記圧力計から得られた圧力値に基づいて、前記フードで覆われた空間内の圧力が大気圧以上となった前記トラフ台車群について、前記排気ガスの流量を大きくするように前記流量調整弁を制御するよう構成されていることを特徴とする焼結鉱冷却機の給排気装置。 A supply and exhaust system for a sintered ore cooler, which stacks sintered ore sintered in a sintering machine on a plurality of trough troughs, each of which is covered by a hood at least on top, and continuously cools the sintered ore by passing a cooling gas through the layers of sintered ore while moving the plurality of trough troughs,
A cooling gas pumping device for supplying the cooling gas to the lower part of the plurality of trough trolleys,
An exhaust gas suction device for drawing exhaust gas from the space covered by the aforementioned hood and discharging it to the outside,
A control device configured to control at least one of the cooling gas pumping device and the exhaust gas suction device such that the flow rate of the cooling gas becomes less than the flow rate of the exhaust gas and the pressure inside the hood becomes lower than atmospheric pressure,
Equipped with,
The cooling gas pumping device has a pumping pipe equipped with a cooling gas flow meter for measuring the flow rate of the cooling gas,
The exhaust gas suction device has an exhaust pipe equipped with an exhaust gas flow meter for measuring the flow rate of the exhaust gas,
A flow control valve is provided in at least the exhaust pipe of the pressure pipe and the exhaust pipe.
Each trough trough group, consisting of at least one of the aforementioned plurality of trough troughs, is provided with a pressure gauge for measuring the pressure in the space covered by the hood and the flow control valve.
The control device is configured to control the flow rate adjustment valve based on the measured values of the cooling gas flow meter and the exhaust gas flow meter, and is configured to control the flow rate adjustment valve to increase the flow rate of the exhaust gas for the trough trough group when the pressure in the space covered by the hood exceeds atmospheric pressure, based on the pressure value obtained from the pressure gauge .
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| JP2022023395A JP7832012B2 (en) | 2022-02-18 | 2022-02-18 | Intake and exhaust system for sintered ore cooler |
| PCT/JP2023/004676 WO2023157779A1 (en) | 2022-02-18 | 2023-02-13 | Air supply/exhaust device for sintered ore cooling machine |
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| JP2022023395A JP7832012B2 (en) | 2022-02-18 | 2022-02-18 | Intake and exhaust system for sintered ore cooler |
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| WO2023157779A1 (en) | 2023-08-24 |
| JP2023120488A (en) | 2023-08-30 |
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