JP2003074826A - Thermal storage combustion device - Google Patents

Thermal storage combustion device

Info

Publication number
JP2003074826A
JP2003074826A JP2001257415A JP2001257415A JP2003074826A JP 2003074826 A JP2003074826 A JP 2003074826A JP 2001257415 A JP2001257415 A JP 2001257415A JP 2001257415 A JP2001257415 A JP 2001257415A JP 2003074826 A JP2003074826 A JP 2003074826A
Authority
JP
Japan
Prior art keywords
heat storage
gas
valve
combustion furnace
combustion
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
Application number
JP2001257415A
Other languages
Japanese (ja)
Inventor
Toshifumi Mukai
利文 向井
Shigeru Tominaga
成 冨永
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.)
Mitsubishi Power Ltd
Original Assignee
Babcock Hitachi 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 Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP2001257415A priority Critical patent/JP2003074826A/en
Publication of JP2003074826A publication Critical patent/JP2003074826A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To protect a rotary distribution valve from seizure during an emergency stop, in a rotating distribution type regenerative combustion device to purify volatile organic compound (VOC)-containing gas. SOLUTION: The thermal combustion device is provided with the rotary distributing valve 7 to distribute gas by switching a kind of gas at a distribution port 4a, each heat storage chamber 14 coupled to the distribution port 4a through a coupling duct 13, and a combustion furnace 15 connected to each thermal storage chamber 14. VOC- containing gas 10 being one of gases id fed in the forward directions of the coupling duct, a thermal storage chamber, and the combustion furnace from the rotary distribution valve and treated gas 8 at the combustion furnace is fed as different gas in a reverse forward direction. In a so formed heat storage combustion device, an atmospheric air induction port 11 is formed in the thermal heat storage chamber 14 and a radiating port 12 is formed in the combustion furnace 15. The atmospheric air induction port 11 and the radiation port 12 are opened and the atmosphere enters during an emergency stop that heaters for VOC-containing gas, a rotary distribution valve, and the combustion furnace are stopped, the thermal storage chamber and the combustion furnace are cooled, and the rise in the temperature of the coupling duct 13 and the rotary distribution valve 7 due to thermal conduction is blocked to protect the devices from seizure.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、揮発性有機化合物
(Volatile Organic Compound:略記VOC)を含むVO
C含有ガスを燃焼して浄化処理し、その処理済みガスか
ら得た蓄熱をVOC含有ガスの予熱に再利用する蓄熱燃
焼装置に係り、特に該装置の緊急停止時に該装置を熱か
ら保護するのに好適な蓄熱燃焼装置に関する。
TECHNICAL FIELD The present invention relates to a volatile organic compound.
VO including (Volatile Organic Compound: VOC for short)
The present invention relates to a heat storage and combustion device that burns a C-containing gas for purification treatment and reuses heat storage obtained from the treated gas for preheating of a VOC-containing gas, and particularly protects the device from heat during an emergency stop of the device. The present invention relates to a heat storage and combustion device suitable for.

【0002】[0002]

【従来の技術】自動車の塗装工場、金属洗浄、印刷工場
などからは、トルエン、キシレン、スチレン等の揮発性
有機化合物(VOC)を含んだ排ガスが発生する。このよ
うなVOC含有ガスは、せいぜい数ppmから数%程度の
VOC濃度であるが、環境への影響がかなり大きいこと
が明らかになってきた。VOC含有ガスは、例えば、
(1)NOxと反応して光化学スモックが発生し、森林が枯
れ死にしたり人体への悪影響を及ぼす、(2)発ガン性な
ど人体に健康障害を起こさせる、(3)光化学オキシダン
トの主成分であるオゾンの対流圏内での増加により地球
温暖化が生じる。このため、前記業界ではVOC含有排
ガスを浄化処理した上で、大気中に排出している。
2. Description of the Related Art Exhaust gas containing volatile organic compounds (VOC) such as toluene, xylene and styrene is emitted from automobile painting factories, metal washing and printing factories. It has been revealed that such a VOC-containing gas has a VOC concentration of several ppm to several% at most, but has a considerably great effect on the environment. The VOC-containing gas is, for example,
(1) Photochemical smock is generated by reacting with NOx, which causes forests to die and have an adverse effect on the human body. (2) Causes health problems such as carcinogenicity to the human body. (3) Main component of photochemical oxidant Global warming is caused by an increase in ozone, which is the troposphere. Therefore, in the above-mentioned industry, the VOC-containing exhaust gas is purified and then discharged into the atmosphere.

【0003】VOCの処理方法としては、直接燃焼式、
触媒燃焼式、蓄熱燃焼方式、触媒燃焼/蓄熱方式、濃縮
方式、生物処理方式があるが、ランニングコスト、保守
保全を考えると蓄熱燃焼方式(触媒燃焼も含む)が有力
視されている。蓄熱燃焼方式には、処理前のVOC含有
ガスを供給する流路と処理済みの浄化ガスを戻す流路を
同じくし、そのガス流れを切り替える方法として、複数
個の弁を組み合わせる複数弁方式と回転分配弁方式があ
り、一般的にコンパクト化、圧力変動の低減の点で回転
分配弁方式が複数弁方式より優れているとされている。
As a VOC treatment method, a direct combustion type,
There are a catalytic combustion type, a thermal storage combustion type, a catalytic combustion / thermal storage type, a concentration type, and a biological treatment type, but the thermal storage combustion type (including catalytic combustion) is considered to be promising in view of running cost and maintenance. In the heat storage combustion method, the flow path for supplying the VOC-containing gas before processing and the flow path for returning the processed purified gas are the same, and as a method for switching the gas flow, a multiple valve method in which a plurality of valves are combined and a rotation method are used. There is a distribution valve system, and it is generally said that the rotary distribution valve system is superior to the multiple valve system in terms of downsizing and reduction in pressure fluctuation.

【0004】[0004]

【発明が解決しようとする課題】回転分配弁方式の蓄熱
燃焼装置は、概して回転分配弁、蓄熱室および燃焼炉を
順次に配置して構成されている。この蓄熱燃焼装置の心
臓部は回転分配弁であり、95%以上の燃焼率や温度効
率を狙うためには、回転分配弁の回転部分とその回転部
分を支持する固定部分との間のシール性を確保するため
に両部分の摺動部がかなり高精度なシール構造となる。
特に、蓄熱燃焼装置の停止時や緊急停止の場合には、こ
の摺動部が熱で損傷しないように十分な保護が必要とな
る。
A rotary distribution valve type heat storage combustion apparatus is generally constructed by sequentially arranging a rotary distribution valve, a heat storage chamber and a combustion furnace. The heart of this heat storage combustion device is a rotary distribution valve, and in order to achieve a combustion rate of 95% or higher and temperature efficiency, the sealing property between the rotating portion of the rotary distribution valve and the fixed portion supporting the rotating portion is required. In order to secure the above, the sliding parts of both parts have a highly accurate sealing structure.
In particular, when the heat storage combustion device is stopped or in the case of an emergency stop, sufficient protection is required to prevent the sliding portion from being damaged by heat.

【0005】例えば、定常運転時において、蓄熱室に設
置された蓄熱体の温度分布は、炉内温度と回転分配弁か
らの供給ガス温度とを直線的につないだ形となる。この
状態で燃焼炉のヒータ、回転分配弁にVOC含有ガスを
供給するブロワー、回転分配弁の駆動モータへの電力供
給を停止した場合に、蓄熱体中の温度勾配が次第に緩和
され、低温側であった回転分配弁も温度上昇する。この
ため回転分配弁と蓄熱室間を連結するダクトないしはホ
ースや回転分配弁のシール部材に有機系の材質を使用し
た場合に焼損したり、最悪の場合には発火原因にもなる
という問題がある。
For example, during steady operation, the temperature distribution of the heat storage body installed in the heat storage chamber has a shape in which the temperature inside the furnace and the temperature of the gas supplied from the rotary distribution valve are connected linearly. In this state, when the electric power supply to the heater of the combustion furnace, the blower that supplies the VOC-containing gas to the rotary distribution valve, and the drive motor of the rotary distribution valve is stopped, the temperature gradient in the heat storage body is gradually alleviated and the low temperature side The temperature of the existing rotary distribution valve also rises. For this reason, there is a problem that if a duct or hose connecting the rotary distribution valve and the heat storage chamber or a seal member of the rotary distribution valve is made of an organic material, it is burnt out or, in the worst case, causes ignition. .

【0006】本発明の目的は、VOCガスを浄化処理す
る回転分配弁方式の蓄熱燃焼装置において、該装置の緊
急停止の際に分配弁等の機材の温度上昇を抑える保護機
構を具備する蓄熱燃焼装置を提供することにある。
An object of the present invention is to provide a rotary storage valve type heat storage combustion apparatus for purifying VOC gas, which is equipped with a protection mechanism for suppressing a temperature rise of equipment such as a distribution valve in the case of an emergency stop of the apparatus. To provide a device.

【0007】[0007]

【課題を解決するための手段】上記目的を達成するため
に、本発明の蓄熱燃焼装置は、複数の分配口へのガスの
種類を切り替えながら分配する回転分配弁と、回転分配
弁の複数の分配口とそれぞれ連結ダクトを介して接続し
内部に蓄熱体を設置する複数の蓄熱室と、該複数の蓄熱
室と接続し内部にヒータを設置する燃焼炉とを備え、か
つ回転分配弁の回転部分と該回転部分を支持する固定部
分間にシール材を設け、そしてガスの一種類でブロワー
から供給されるVOC含有ガスを回転分配弁から連結ダ
クト、蓄熱室、燃焼炉の順方向に送給し、ガスの別の種
類で燃焼炉で揮発性有機化合物含有ガスが燃焼して生じ
た処理済みガスを逆順方向に送出するように構成した蓄
熱燃焼装置において、複数の蓄熱室それぞれの底部に開
閉弁付き大気誘引口を、そして燃焼炉頂部に開閉弁付き
放熱口を設け、装置運転中にブロワー、回転分配弁およ
びヒータへの給電を遮断したときに各開閉弁を開くよう
にしたことを特徴とする。
In order to achieve the above object, a heat storage combustion apparatus of the present invention includes a rotary distribution valve for distributing while distributing gas types to a plurality of distribution ports, and a plurality of rotary distribution valves. A plurality of heat storage chambers each of which is connected to a distribution port through a connecting duct and in which a heat storage body is installed, and a combustion furnace which is connected to the plurality of heat storage chambers and in which a heater is installed, and which rotates a rotary distribution valve. A sealing material is provided between a portion and a fixed portion that supports the rotating portion, and VOC-containing gas supplied from a blower with one kind of gas is fed from the rotary distribution valve in the forward direction of the connecting duct, the heat storage chamber, and the combustion furnace. However, in a heat storage combustion device configured to send out the processed gas generated by burning the volatile organic compound-containing gas in the combustion furnace with another type of gas in the reverse forward direction, opening and closing at the bottom of each heat storage chamber Atmosphere attraction with valve The and-off valve with thermal vents provided in the combustion furnace top, characterized in that to open the respective opening and closing valves when interrupted during device operation blower, rotary distributor valve and the power supply to the heater.

【0008】そして上記蓄熱燃焼装置には、蓄熱室内で
燃焼炉側に蓄熱体に隣接して触媒を設置することが好ま
しい。
In the heat storage combustion apparatus, it is preferable to install a catalyst on the combustion furnace side in the heat storage chamber adjacent to the heat storage body.

【0009】本発明の蓄熱燃焼装置の定常運転において
は、ブロワーから供給されるVOC含有ガスは、回転分
配弁の回転につれて回転分配弁のVOC含有ガス用ポー
トと順次導通する連結ダクトを介して蓄熱室に送られそ
こで蓄熱体の蓄熱により加熱され、燃焼炉でヒーターに
より加熱されて燃焼し、浄化されて処理済みガスとな
る。処理済みガスは、燃焼炉から、回転分配弁の回転に
つれて回転弁の処理済みガス用ポートに順次導通する蓄
熱室および連結ダクト、それから回転分配弁の処理済み
ガス用ポートを通じて、回転分配弁から装置外部に流出
する。パージ空気は、装置停止時や起動時などに回転分
配弁のパージ空気ポートを通じて流す。
In the steady operation of the heat storage and combustion apparatus of the present invention, the VOC-containing gas supplied from the blower stores heat through the connecting duct which is successively connected to the VOC-containing gas port of the rotary distribution valve as the rotary distribution valve rotates. It is sent to the chamber and heated there by the heat storage of the heat storage body, and is heated by the heater in the combustion furnace and burned to be purified into a treated gas. The treated gas is transferred from the combustion furnace to the treated gas port of the rotary valve through the heat storage chamber and the connecting duct, which are sequentially connected to the processed gas port of the rotary valve, and then through the treated gas port of the rotary distribution valve to the rotary distribution valve. It leaks to the outside. Purge air flows through the purge air port of the rotary distribution valve when the device is stopped or started.

【0010】開閉弁付き大気誘引口および開閉弁付き放
熱口は蓄熱燃焼装置を緊急停止する時に保護機構として
機能する。すなわち緊急停止のためブロワー、回転分配
弁およびヒータへの給電を停止したとき、あるいは予期
しない停電が発生したときなどに各開閉弁を「開」にす
ることにより、大気が自然対流で大気誘引口から蓄熱室
に流入し、燃焼炉を経て放熱口から流出し、この大気の
流れで蓄熱室内および燃焼炉内の高温ガスを追い出して
蓄熱室および燃焼炉を冷却する。この冷却により蓄熱室
から連結ダクトないし回転分配弁へ熱が伝導するのが阻
止されるため、連結ダクトや回転分配弁のシール材を熱
による損傷から保護する。したがって耐熱温度の低い有
機系材料を用いた連結ダクト、シール材を採用すること
が可能となる。
The atmosphere inlet port with the on-off valve and the heat radiation port with the on-off valve function as a protection mechanism when the heat storage combustion device is stopped in an emergency. That is, when power supply to the blower, rotary distribution valve and heater is stopped due to an emergency stop, or when an unexpected power failure occurs, each open / close valve is "opened" so that the atmosphere is a natural convection and the atmosphere attracts the atmosphere. Flows into the heat storage chamber from the heat dissipation chamber, flows out from the heat dissipation port through the combustion furnace, and the high temperature gas in the heat storage chamber and the combustion furnace is expelled by the flow of the atmosphere to cool the heat storage chamber and the combustion furnace. This cooling prevents heat from being transferred from the heat storage chamber to the connection duct or the rotary distribution valve, and thus protects the sealing material of the connection duct and the rotary distribution valve from damage due to heat. Therefore, it becomes possible to adopt a connecting duct and a sealing material using an organic material having a low heat resistant temperature.

【0011】[0011]

【発明の実施の形態】以下、本発明の実施の形態となる
蓄熱燃焼装置について説明する。この蓄熱燃焼装置は、
概略、図1に示すように、3種類のガス、すなわち揮発
性有機化合物(Volatile Organic Compound:略記VO
C)を含むガス10(VOC含有ガスという)、それぞ
れ後述する処理済みガス8およびパージ空気を複数の分
配口4aに切り替えながら分配する回転分配弁7と、分
配弁7から連結ダクトとしてのフレキシブルダクト13
を通じて供給されるVOC含有ガス10を予熱する複数
の蓄熱室14と、蓄熱室14から送給されたVOC含有
ガス10をヒータ1により加熱して浄化処理する燃焼炉
15と、各蓄熱室14底部から外気を取り入れる開閉弁
付き大気誘引口11と、燃焼炉15頂部から燃焼炉15
内のガスを放出する開閉弁付き放熱口12とから構成さ
れており、さらに燃焼炉15で浄化された処理済みガス
8を蓄熱室14からフレキブルホース13、分配弁7へ
とVOC含有ガス10とは逆順方向に通過させて排出す
るように、またパージ空気9をVOC含有ガス10と同
じく順方向に流すように構成されている。そして本発明
の蓄熱燃焼装置は、上記大気誘引口11及び放熱口12
を保護機構として備える点に特徴がある。
BEST MODE FOR CARRYING OUT THE INVENTION A heat storage and combustion device according to an embodiment of the present invention will be described below. This heat storage combustion device
Schematically, as shown in FIG. 1, three kinds of gases, namely, volatile organic compounds (VO) are abbreviated.
A gas 10 containing C) (referred to as VOC-containing gas), a processed gas 8 and a purge air, which will be described later, are distributed while switching to a plurality of distribution ports 4a, and a flexible duct as a connecting duct from the distribution valve 7. Thirteen
A plurality of heat storage chambers 14 for preheating the VOC-containing gas 10 supplied through the combustion chamber 15, a heating furnace 15 for heating the VOC-containing gas 10 fed from the heat storage chamber 14 by the heater 1 to purify the VOC-containing gas 10, and a bottom portion of each heat storage chamber 14. Atmosphere inlet 11 with an on-off valve that takes in outside air from the top, and combustion furnace 15 from the top to combustion furnace 15
And a heat radiation port 12 with an on-off valve for discharging the gas inside, and further, the treated gas 8 purified in the combustion furnace 15 from the heat storage chamber 14 to the flexible hose 13 and the distribution valve 7 to the VOC-containing gas 10 In contrast to the above, it is configured so as to pass through in the reverse forward direction and be discharged, and the purge air 9 flows in the forward direction like the VOC-containing gas 10. The heat storage and combustion device of the present invention is provided with the above-mentioned atmosphere induction port 11 and heat dissipation port 12
Is characterized in that is provided as a protection mechanism.

【0012】構成機器をさらに詳しく説明する。分配弁
7は、4重管でなり、隣り合う管と管の間に形成された
3つの環状流路を有するガスヘッダー6と、ガスヘッダ
ー6の各環状流路に対してそれぞれポート(合計3ポー
ト)を有する円板状の回転弁5と、回転弁5の回転につ
れて回転弁5の各ポートを介してガスヘッダー6の各環
状流路と順次に導通する8つの分配口8aを有する固定
弁4と、を順に積むように組み合わせて構成されてい
る。分配弁7の4重管の中心空間には回転弁5に接続す
る回転軸(図示なし)が配置され、その回転軸がモータ
(図示なし)により駆動される。また回転弁5と固定弁
4の間にガスリークを防止するシール材としてパッキン
(図示なし)を設けている。
The components will be described in more detail. The distribution valve 7 is a quadruple pipe, and has a gas header 6 having three annular flow passages formed between adjacent pipes, and a port (total 3 in total) for each annular flow passage of the gas header 6. A fixed valve having a disk-shaped rotary valve 5 having a port) and eight distribution ports 8a sequentially connected to the annular flow paths of the gas header 6 via the ports of the rotary valve 5 as the rotary valve 5 rotates. 4 and so as to be stacked in order. A rotary shaft (not shown) connected to the rotary valve 5 is arranged in the central space of the quadruple pipe of the distribution valve 7, and the rotary shaft is driven by a motor (not shown). Further, packing (not shown) is provided between the rotary valve 5 and the fixed valve 4 as a sealing material for preventing gas leakage.

【0013】ガスヘッダー6の3つの環状流路のうち、
外側の流路6aは処理済みガス8を、中央の流路6cは
VOC含有ガス10を、内側の流路6bはパージ空気9
を流す流路となっている。
Of the three annular flow paths of the gas header 6,
The outer channel 6a contains the treated gas 8, the central channel 6c contains the VOC-containing gas 10, and the inner channel 6b contains the purge air 9.
It is a flow path for flowing.

【0014】回転弁5の3つのポートは、処理済みガス
8用ポート5a、VOC含有ガス10用ポート5c、パ
ージ空気9用ポート5bである。ここでは、処理済みガ
ス8用ポート5a及びVOC含有ガス10用ポート5c
はそれぞれ回転弁5の1/4回転分相当の長さに形成さ
れ、パージ空気9用ポート5bは1/8回転分相当の長
さに形成され、そして各ポートは互いに1/8回転分相
当だけ離れている。回転弁5の回転につれて、固定弁4
の個々の分配口4aには、VOC含有ガス10が上方向
に、処理済みガス8が下方向に、順に通過し、この手順
が繰り返される。ただし、パージ空気9は、燃焼を停止
したときなど、装置の状況に応じて供給される。
The three ports of the rotary valve 5 are a port 5a for the treated gas 8, a port 5c for the VOC-containing gas 10 and a port 5b for the purge air 9. Here, the port 5a for the treated gas 8 and the port 5c for the VOC-containing gas 10 are used.
Are each formed to have a length corresponding to 1/4 rotation of the rotary valve 5, the purge air 9 port 5b is formed to have a length corresponding to 1/8 rotation, and each port is equivalent to 1/8 rotation. Just away. As the rotary valve 5 rotates, the fixed valve 4
The VOC-containing gas 10 passes upward and the treated gas 8 passes downward through the individual distribution ports 4a, and this procedure is repeated. However, the purge air 9 is supplied according to the condition of the apparatus such as when the combustion is stopped.

【0015】蓄熱室14は並列配置された8室からな
り、各室の下部は固定弁4の分配口8aにフレキシブル
ダクト13によって接続されている。ここではフレキシ
ブルダクト13は耐熱温度80℃のφ80mm×300mm
長のものを用いている。8本のフレキシブルダクト13
はガスを分配または集合させるいわゆるマニホールド部
である。一つの蓄熱室14は横断面150mm角、600
mm高さで、その内部にコーディエライト(キン青石:マ
グネシウムアルミノシリケート)質のハニカム(セル密度
210cell/in2)からなる蓄熱体3とその蓄熱体3の基
材の上部に貴金属を担持させてなる触媒2を内蔵してい
る。また8室の蓄熱室14の上に設置された燃焼炉は3
00mm高さとした。
The heat storage chamber 14 consists of eight chambers arranged in parallel, and the lower part of each chamber is connected to the distribution port 8a of the fixed valve 4 by a flexible duct 13. Here, the flexible duct 13 has a heat resistant temperature of 80 ° C. φ80 mm × 300 mm
I use the long one. 8 flexible ducts 13
Is a so-called manifold portion for distributing or collecting gas. One heat storage chamber 14 has a cross section of 150 mm square, 600
With a height of mm, a noble metal is supported on the heat storage body 3 composed of a cordierite (kinseite: magnesium aluminosilicate) honeycomb (cell density 210 cell / in 2 ) and the base material of the heat storage body 3 at a height of mm. It has a built-in catalyst 2. In addition, the combustion furnace installed above the eight heat storage chambers 14 is 3
The height was set to 00 mm.

【0016】上記のように構成された蓄熱燃焼装置の定
常時の動作について説明する。VOC含有ガス10はブ
ロワー(図示なし)により分配弁7に供給される。分配
弁7のガスヘッダー6に形成された環状流路6cに流入
したVOC含有ガス10は、回転弁5の回転につれてポ
ート5cにより開通する固定弁4の分配口4aからフレ
キシブルダクト13を経て蓄熱室14に流入し、そこを
通過する間に蓄熱体3の保有熱により徐々に加熱され、
触媒2によりVOC分解反応が促進され、それから燃焼
炉15に流入してそこでヒータ1による加熱、燃焼によ
って浄化されて処理済みガス8となる。この処理済みガ
ス8は、燃焼炉15から蓄熱室14、フレキシブルダク
ト13を順に通り、回転弁5の回転につれてポート5a
により開通する固定弁4の分配口4、ポート5a、ガス
ヘッダー6の環状流路6aを順次通過して、蓄熱燃焼装
置外に流出する。処理済みガスは、蓄熱室14を通過す
る間に蓄熱体3に放熱して徐々に温度が低下し、そして
蓄熱体3は次にそこを通過するVOC含有ガス10する
ための熱を貯える。個々の分配口14をみると、回転弁
5の1回転中、VOC含有ガス10の流入、処理済みガ
ス8の流出が順に周期的に起きる。、パージ空気9は、
装置の情況に応じて適宜供給される。このようにして本
蓄熱燃焼装置はVOC含有ガス10を連続的に浄化処理
する。なおヒータ1は蓄熱燃焼装置をコールドの状態で
運転開始する際に燃焼炉を予熱する予熱ヒータとしても
用いられる。
The steady-state operation of the heat storage combustion apparatus configured as described above will be described. The VOC-containing gas 10 is supplied to the distribution valve 7 by a blower (not shown). The VOC-containing gas 10 that has flowed into the annular flow path 6c formed in the gas header 6 of the distribution valve 7 is opened by the port 5c as the rotary valve 5 rotates, and flows from the distribution port 4a of the fixed valve 4 through the flexible duct 13 into the heat storage chamber. 14 and is gradually heated by the stored heat of the heat storage body 3 while passing therethrough,
The VOC decomposition reaction is promoted by the catalyst 2, and then flows into the combustion furnace 15 where it is purified by heating and combustion by the heater 1 and becomes the treated gas 8. The processed gas 8 passes from the combustion furnace 15 through the heat storage chamber 14 and the flexible duct 13 in order, and as the rotary valve 5 rotates, the port 5 a.
Through the distribution valve 4 of the fixed valve 4, the port 5a, and the annular flow path 6a of the gas header 6 which are sequentially opened, and flow out of the heat storage combustion device. The treated gas radiates heat to the heat storage body 3 while passing through the heat storage chamber 14 and the temperature thereof gradually decreases, and the heat storage body 3 stores heat for the VOC-containing gas 10 that passes therethrough next. Looking at the individual distribution ports 14, during one revolution of the rotary valve 5, the inflow of the VOC-containing gas 10 and the outflow of the treated gas 8 occur sequentially in sequence. , Purge air 9
It is appropriately supplied depending on the situation of the device. In this way, the heat storage combustion apparatus continuously purifies the VOC-containing gas 10. The heater 1 is also used as a preheat heater for preheating the combustion furnace when the heat storage combustion device is started in a cold state.

【0017】さて、本発明を特徴づける大気誘引口11
及び放熱口12について説明する。図1に示すように、
大気誘引口11は電磁弁16付き配管からなり、蓄熱室
14それぞれの底部に設け、そして放熱口12は同じく
電磁弁16付き配管からなり、燃焼炉15の頂部に設け
ている。各蓄熱室14に設けた大気誘引口11は大気入
口側を1本にまとめているが、必ずしも1本化する必要
がなくばらばらでもよい。電磁弁16は、通電時閉、非
通電時開のものを用いた。
Now, the atmosphere inlet 11 characterizing the present invention
The heat dissipation port 12 will be described. As shown in Figure 1,
The atmosphere intake port 11 is composed of a pipe with an electromagnetic valve 16 and is provided at the bottom of each heat storage chamber 14, and the heat dissipation port 12 is also composed of a pipe with an electromagnetic valve 16 and is provided at the top of the combustion furnace 15. The atmosphere inlet 11 provided in each heat storage chamber 14 has one atmosphere inlet side, but it does not necessarily have to be one and may be separated. The solenoid valve 16 used was closed when energized and opened when not energized.

【0018】これら大気誘引口11及び放熱口12は、
運転中の蓄熱燃焼装置を緊急停止あるいは不時停電した
時に作動させる。即ち、緊急停止のため、VOC含有ガ
ス10を分配弁7に送給するブロワー、分配弁4を駆動
するモータ及び燃焼15のヒータ1への給電を遮断した
時に、大気誘引口11及び放熱口12の各電磁弁16を
開いて、大気を自然対流により各蓄熱室14に流入さ
せ、放熱口12から流出させる。このとき大気の流れ
は、各蓄熱室14に充満する処理済みガスあるいはVO
C含有ガス、炉内の高温ガスを追い出して、各蓄熱室及
び燃焼炉を冷却する。この結果、各蓄熱室14から下方
のフレキシブルダクト13、分配弁7への熱伝導を阻止
することになる。
The atmosphere introducing port 11 and the heat radiating port 12 are
Activate the thermal storage combustion device during operation in the event of an emergency stop or unscheduled power failure. That is, when power supply to the blower that feeds the VOC-containing gas 10 to the distribution valve 7, the motor that drives the distribution valve 4, and the heater 15 for the combustion 15 is cut off for an emergency stop, the atmosphere induction port 11 and the heat radiation port 12 The respective electromagnetic valves 16 are opened to allow atmospheric air to flow into each heat storage chamber 14 by natural convection and to flow out from the heat radiation port 12. At this time, the flow of the atmosphere is the processed gas or VO that fills each heat storage chamber 14.
The C-containing gas and the high temperature gas in the furnace are expelled to cool each heat storage chamber and the combustion furnace. As a result, heat conduction from each heat storage chamber 14 to the lower flexible duct 13 and the distribution valve 7 is blocked.

【0019】次に図2により、本発明の蓄熱燃焼装置の
緊急停止時における装置各部の温度変化を従来の装置と
比較して説明する。緊急停止時、燃焼炉15の炉内温度
は、実線Aで示すように、定常運転時の高温(例えば8
50℃)から徐々に低下し、そして蓄熱体3下端(分配弁
側)の温度は、実線Bで示すように、定常運転時の低温
(大気温度より数十℃高い)より若干上昇するものの、あ
る時間経過後に定常状態になる。かくして蓄熱体3下端
の温度は、蓄熱体3下に接続するフレキシブルダクト1
3や分配弁7の耐熱温度(1点鎖線C)以下に保持され
る。一方、従来装置では、本発明にかかる大気誘引口及
び放熱口がなく、燃焼炉内のガスと各蓄熱室内のガスが
対流で混合するため、炉内温度が、点線aで示すよう
に、急に低下し、それと共に蓄熱体下端温度が、点線b
で示すように、急に上昇して、両温度が接近する。従っ
て、温度上昇した蓄熱体から下方のフレキシブルダクト
や分配弁に熱伝導が生じ、フレキシブルダクトや分配弁
のパッキンがそれらの耐熱温度以上になり、焼損が避け
られない。
Next, referring to FIG. 2, the temperature change of each part of the heat storage combustion apparatus of the present invention during an emergency stop will be described in comparison with a conventional apparatus. At the time of an emergency stop, the temperature inside the combustion furnace 15 is high (for example, 8
50 ° C.), and the temperature of the lower end of the heat storage body 3 (distribution valve side) is, as shown by the solid line B, low temperature during steady operation.
Although it rises a little above (several tens of degrees higher than the atmospheric temperature), it reaches a steady state after a certain period of time. Thus, the temperature of the lower end of the heat storage body 3 is the flexible duct 1 connected below the heat storage body 3.
3 and the distribution valve 7 are kept at the heat-resistant temperature (one-dot chain line C) or lower. On the other hand, in the conventional apparatus, since the gas in the combustion furnace and the gas in each heat storage chamber are mixed by convection without the atmospheric air inlet and the heat radiating port according to the present invention, the temperature in the furnace is steep as shown by the dotted line a. The temperature at the lower end of the heat storage body is reduced to the dotted line b.
As indicated by, the temperature rises sharply and both temperatures approach each other. Therefore, heat conduction occurs from the heat storage body whose temperature has risen to the flexible duct and the distribution valve below, and the packing of the flexible duct and the distribution valve becomes higher than their heat resistant temperatures, and burning is inevitable.

【0020】大気誘引口11及び放熱口12からなる保
護機構は、緊急停止時ばかりでなく、通常運転停止時に
も有効である。これまで蓄熱燃焼装置の通常の停止の
際、燃焼炉のヒータを止めてからある時間、蓄熱燃焼装
置を空運転し蓄熱体を冷却してからでないと、ブロアー
や分配弁を停止することができない。特に、蓄熱室にお
ける熱交換器の温度効率は95%以上高くて放熱しにく
いため、蓄熱室の冷却にかなりの時間の空運転を必要と
し、これは運転操作上好ましくない。そこで本発明にか
かる保護機構(機能上は冷却機構)を利用して大気開放
すれば、冷却期間を設けなくとも蓄熱燃焼装置を即座に
停止することが可能となる。
The protection mechanism consisting of the air intake port 11 and the heat radiation port 12 is effective not only during an emergency stop but also during a normal operation stop. Until now, when the heat storage combustion device was normally shut down, the blower or distribution valve cannot be stopped until the heat storage combustion device is idle and the heat storage body is cooled for a certain time after the heater of the combustion furnace is stopped. . In particular, since the temperature efficiency of the heat exchanger in the heat storage chamber is higher than 95% and it is difficult to radiate heat, idle operation for a considerable time is required for cooling the heat storage chamber, which is not preferable in operation. Therefore, if the protective mechanism (functionally, a cooling mechanism) according to the present invention is used to open the atmosphere, the heat storage combustion device can be immediately stopped without providing a cooling period.

【0021】次に大気誘引口11及び放熱口12からな
る保護機構の効果を確かめた確認実験の結果を説明す
る。蓄熱燃焼装置の各構成要素のサイズは、前述のとお
りで、フレキシブルダクト13は耐熱温度80℃のφ8
0mm×300mm長であり、蓄熱室14は断面150mm
角、600mm高さでコーディエライトの蓄熱体3と貴金
属の触媒2を内蔵し、そして燃焼炉は300mm高さであ
る。この蓄熱燃焼装置に模擬VOCガスとしてトルエン
100ppmを含む空気を5m3/min、パージガスとして空
気を0.6m3/min供給し、炉内温度を850℃一定に維
持しながら定常運転した。VOC処理装置の性能は浄化
率95%以上、熱回収率95%以上、圧力損失2〜2.
5kPaであった。この状態でヒータとブロアーと分配弁
7の給電を遮断した。それと同時に、各蓄熱室14底部
に取り付けた大気誘引口11と燃焼炉15頂部に取り付
けられた放熱口12を開いた。これにより蓄熱室14の
下から空気が取り込まれ、燃焼炉15の上から高温ガス
が排出される。その結果、蓄熱体3の下の温度はほぼ
「大気温度+20℃」以下に維持されることが分かっ
た。そのため、蓄熱室14と分配弁7をつなぐフレキシ
ブルダクト13と分配弁7の温度は低温に維持されたま
まであり、問題ないことが分かった。この効果は触媒を
使わない蓄熱燃焼方式でも同様であり、炉内温度が85
0℃の状態で給電が遮断されても蓄熱体の下の温度は
「大気温度+40℃」以下に維持されることが分かっ
た。
Next, the result of the confirmation experiment for confirming the effect of the protection mechanism composed of the atmosphere inlet 11 and the heat dissipation port 12 will be described. The size of each component of the heat storage combustion device is as described above, and the flexible duct 13 has a heat resistant temperature of 80 ° C. φ8.
The length is 0 mm x 300 mm, and the heat storage chamber 14 has a cross section of 150 mm.
The corners are 600 mm high and contain cordierite heat storage 3 and precious metal catalyst 2, and the combustion furnace is 300 mm high. Air containing 100 ppm of toluene as a simulated VOC gas was supplied to this heat storage and combustion apparatus at 5 m 3 / min and air as a purge gas was supplied at 0.6 m 3 / min, and steady operation was performed while maintaining the furnace temperature at 850 ° C. constant. The performance of VOC treatment equipment is a purification rate of 95% or more, a heat recovery rate of 95% or more, and a pressure loss of 2 to 2.
It was 5 kPa. In this state, power supply to the heater, blower and distribution valve 7 was cut off. At the same time, the air intake port 11 attached to the bottom of each heat storage chamber 14 and the heat radiation port 12 attached to the top of the combustion furnace 15 were opened. As a result, air is taken in from below the heat storage chamber 14, and high-temperature gas is discharged from above the combustion furnace 15. As a result, it was found that the temperature below the heat storage body 3 was maintained at approximately "atmospheric temperature + 20 ° C" or lower. Therefore, it was found that the temperature of the flexible duct 13 that connects the heat storage chamber 14 and the distribution valve 7 and the temperature of the distribution valve 7 were kept low, and there was no problem. This effect is the same with the heat storage combustion method that does not use a catalyst.
It was found that the temperature below the heat storage body was maintained at "atmospheric temperature + 40 ° C" or less even when the power supply was cut off at 0 ° C.

【0022】比較のために、上記確認実験で用いた装置
から大気誘引口11及び放熱口12の保護機構を取り除
いた蓄熱燃焼装置を用いて、上述の確認実験と同様に定
常運転した。その後、ヒータとブロアーと分配弁の給電
を遮断した。その結果、蓄熱室14の底部が180℃ま
で上昇し、有機系材料からなるフレキシブルダクト13
が焼損した。
For comparison, a steady-state operation was carried out in the same manner as in the above-mentioned confirmation experiment, using a heat storage combustion device obtained by removing the protective mechanism for the atmosphere induction port 11 and the heat radiation port 12 from the device used in the confirmation experiment. After that, the power supply to the heater, blower and distribution valve was cut off. As a result, the bottom of the heat storage chamber 14 rises to 180 ° C., and the flexible duct 13 made of an organic material is used.
Was burned.

【0023】そこで有機系材料のフレキシブルダクトの
代わりにステンレス製フレキシブルダクトを分配回転弁
7と各蓄熱室14に接続して、同様の実験をしたとこ
ろ、今度は分配弁7側の温度が120℃近くまで温度上
昇し、回転分配弁の回転を支持するベアリングのグリー
スが分解するような臭気が発生した。
Then, instead of the flexible duct made of an organic material, a flexible duct made of stainless steel was connected to the distribution rotary valve 7 and each heat storage chamber 14, and a similar experiment was conducted. This time, the temperature on the distribution valve 7 side was 120 ° C. The temperature rose to near, and an odor was generated that decomposed the grease in the bearing that supports the rotation of the rotary distribution valve.

【0024】触媒を使わずに蓄熱燃焼させた場合は、さ
らにこの現象は深刻なものとなる。蓄熱体下の温度は3
00℃まで上昇することがあり、フレキシブルダクトや
シール材に有機系の材料は使用できないことが分かっ
た。
This phenomenon becomes more serious when heat storage combustion is performed without using a catalyst. The temperature under the heat storage body is 3
The temperature could rise to 00 ° C., and it was found that organic materials cannot be used for flexible ducts and sealing materials.

【0025】以上述べたように、この蓄熱燃焼装置にお
いて、各蓄熱室底部の大気誘引口及び燃焼炉頂部に放熱
口を、両機器の冷却機構として備えることにより、装置
を緊急停止した場合でも蓄熱室と分配弁間をつなぐフレ
キシブルダクトの耐熱保護や、分配弁のシール材の耐熱
保護が可能となり、安全面に関しても万全である。特に
機器の冷却に空気の自然対流を利用するため、この冷却
のために補助電源や外部のエネルギーが必要としないと
ころが大きな特徴である。また装置の通常停止の場合に
おいても、本冷却機構を使えば、これまで必要とした装
置の冷却運転なしで停止することが可能であり、操作性
が向上するだけでなく省エネルギーにもなる。
As described above, in this heat storage and combustion device, by providing the atmosphere induction port at the bottom of each heat storage chamber and the heat radiation port at the top of the combustion furnace as a cooling mechanism for both devices, the heat storage is performed even when the device is emergency stopped. The flexible duct that connects the chamber and the distribution valve can be protected against heat, and the sealing material of the distribution valve can be protected against heat. In particular, since natural convection of air is used for cooling the equipment, a major feature is that no auxiliary power source or external energy is required for this cooling. Further, even when the apparatus is normally stopped, the present cooling mechanism can be used to stop the apparatus without the required cooling operation, which not only improves operability but also saves energy.

【0026】[0026]

【発明の効果】本発明によれば、VOCガスを浄化処理
する回転分配弁方式の蓄熱燃焼装置において、蓄熱室か
ら燃焼炉を通じて大気を流して熱を大気中に放出する保
護機構を設けたので、装置を緊急停止しても、蓄熱室に
順次接続するフレキシブルダクトや回転分配弁を低温に
維持でき、有機系材料からなるフレキシブルダクトや回
転分配弁のシール材でも熱による損傷から保護すること
ができる。
According to the present invention, a rotary distribution valve type heat storage combustion apparatus for purifying VOC gas is provided with a protection mechanism for flowing the atmosphere from the heat storage chamber through the combustion furnace to release heat to the atmosphere. Even if the device is stopped suddenly, the flexible duct and rotary distribution valve that are sequentially connected to the heat storage chamber can be maintained at a low temperature, and the flexible duct made of organic material and the seal material of the rotary distribution valve can be protected from damage due to heat. it can.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の実施形態となる蓄熱燃焼装置の構成図
である。
FIG. 1 is a configuration diagram of a heat storage combustion device according to an embodiment of the present invention.

【図2】緊急停止時における本発明の蓄熱燃焼装置の各
部温度変化を従来技術と比較した図である。
FIG. 2 is a diagram comparing a temperature change of each part of the heat storage combustion apparatus of the present invention at the time of an emergency stop with a conventional technique.

【符号の説明】[Explanation of symbols]

1 ヒータ 2 触媒 3 蓄熱体 4 固定弁 4a 分配口 5 回転弁 6 ガスヘッダー 7 分配弁 8 処理済みガス 9 パージ空気 10 VOCガス 11 大気誘引口 12 放熱口 13 フレキシブルダクト 14 蓄熱室 15 燃焼炉 16 電磁弁 1 heater 2 catalyst 3 heat storage 4 fixed valve 4a Distribution port 5 rotary valve 6 gas header 7 distribution valve 8 treated gas 9 Purge air 10 VOC gas 11 Atmosphere attraction 12 Heat dissipation port 13 Flexible duct 14 heat storage room 15 Combustion furnace 16 solenoid valve

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 3K062 AA24 AB01 AC19 DB23 3K078 AA04 BA17 BA21 DA26 DA32 EA10    ─────────────────────────────────────────────────── ─── Continued front page    F term (reference) 3K062 AA24 AB01 AC19 DB23                 3K078 AA04 BA17 BA21 DA26 DA32                       EA10

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 複数の分配口へのガスの種類を切り替え
ながら分配する回転分配弁と、前記回転分配弁の前記複
数の分配口とそれぞれ連結ダクトを介して接続し内部に
蓄熱体を設置する複数の蓄熱室と、該複数の蓄熱室と接
続し内部にヒータを設置する燃焼炉とを備え、かつ前記
回転分配弁の回転部分と該回転部分を支持する固定部分
間にシール材を設け、そして前記ガスの一種類でブロワ
ーから供給される揮発性有機化合物含有ガスを前記回転
分配弁から前記連結ダクト、前記蓄熱室、前記燃焼炉の
順方向に送給し、前記ガスの別の種類で前記燃焼炉で前
記揮発性有機化合物含有ガスが燃焼して生じた処理済み
ガスを前記順方向とは逆の逆順方向に送出するように構
成した蓄熱燃焼装置において、 前記複数の蓄熱室それぞれの底部に開閉弁付き大気誘引
口を、そして前記燃焼炉頂部に開閉弁付き放熱口を設
け、装置運転中に前記ブロワー、前記回転分配弁および
前記ヒータへの給電を遮断したときに前記各開閉弁を開
くようにしたことを特徴とする蓄熱燃焼装置。
1. A rotary distribution valve that distributes gas to a plurality of distribution ports while switching the gas type, and the plurality of distribution ports of the rotary distribution valve are connected to each other via connecting ducts, and a heat storage body is installed inside. A plurality of heat storage chambers, a combustion furnace connected to the plurality of heat storage chambers and having a heater installed therein, and a seal member provided between a rotating portion of the rotary distribution valve and a fixed portion supporting the rotating portion, Then, a volatile organic compound-containing gas supplied from a blower with one type of the gas is fed from the rotary distribution valve in the forward direction of the connection duct, the heat storage chamber, and the combustion furnace, and with another type of the gas. In a heat storage combustion apparatus configured to deliver a treated gas generated by burning the volatile organic compound-containing gas in the combustion furnace in a reverse forward direction opposite to the forward direction, a bottom portion of each of the plurality of heat storage chambers On-off valve An air intake port, and a heat dissipation port with an on-off valve at the top of the combustion furnace, so that each of the on-off valves is opened when power supply to the blower, the rotary distribution valve, and the heater is cut off during operation of the apparatus. A heat storage and combustion device characterized in that
【請求項2】 前記蓄熱室内で前記燃焼炉側に前記蓄熱
体に隣接して触媒を設置したことを特徴とする請求項1
記載の蓄熱燃焼装置。
2. A catalyst is installed adjacent to the heat storage body on the combustion furnace side in the heat storage chamber.
The heat storage combustion device described.
JP2001257415A 2001-08-28 2001-08-28 Thermal storage combustion device Pending JP2003074826A (en)

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005265234A (en) * 2004-03-17 2005-09-29 Babcock Hitachi Kk Ammonia containing exhaust gas treating device and method
CN103574625A (en) * 2013-10-11 2014-02-12 李庆彪 Catalytic combustion furnace
KR20170005667A (en) * 2015-07-06 2017-01-16 김은연 Regenerator combustion and oxidization apparatus capable of preventing leakage of gas
CN109745822A (en) * 2019-03-11 2019-05-14 杨松 A kind of VOCs waste-gas adsorbant desorption pyrolysis oven
CN109745823A (en) * 2019-03-11 2019-05-14 杨松 A kind of VOCs waste-gas adsorbant desorption pyrolytic process
CN117704396A (en) * 2023-12-25 2024-03-15 天华化工机械及自动化研究设计院有限公司 Bottom visualization device for incineration waste gas treatment equipment in coking industry

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005265234A (en) * 2004-03-17 2005-09-29 Babcock Hitachi Kk Ammonia containing exhaust gas treating device and method
CN103574625A (en) * 2013-10-11 2014-02-12 李庆彪 Catalytic combustion furnace
CN103574625B (en) * 2013-10-11 2017-01-25 李庆彪 Catalytic combustion furnace
KR20170005667A (en) * 2015-07-06 2017-01-16 김은연 Regenerator combustion and oxidization apparatus capable of preventing leakage of gas
KR101721762B1 (en) 2015-07-06 2017-03-30 김은연 Regenerator combustion and oxidization apparatus capable of preventing leakage of gas
CN109745822A (en) * 2019-03-11 2019-05-14 杨松 A kind of VOCs waste-gas adsorbant desorption pyrolysis oven
CN109745823A (en) * 2019-03-11 2019-05-14 杨松 A kind of VOCs waste-gas adsorbant desorption pyrolytic process
CN117704396A (en) * 2023-12-25 2024-03-15 天华化工机械及自动化研究设计院有限公司 Bottom visualization device for incineration waste gas treatment equipment in coking industry

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