JP2009056354A - Dust shakedown control method of high-temperature dust collector and dust shakedown control unit - Google Patents

Dust shakedown control method of high-temperature dust collector and dust shakedown control unit Download PDF

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JP2009056354A
JP2009056354A JP2007223944A JP2007223944A JP2009056354A JP 2009056354 A JP2009056354 A JP 2009056354A JP 2007223944 A JP2007223944 A JP 2007223944A JP 2007223944 A JP2007223944 A JP 2007223944A JP 2009056354 A JP2009056354 A JP 2009056354A
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JP5288750B2 (en
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Hiroyuki Hikita
浩之 引田
Ryoji Samejima
良二 鮫島
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Takuma Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To effectively prevent the clogging of a ceramic filter while suppressing the temperature drop of a combustion gas. <P>SOLUTION: The temperature of the combustion gas at the inlet of a high-temperature dust collector 3 is detected by a temperature detector 16 and, when the detected temperature of the combustion gas becomes a preset predetermined temperature or above, a predetermined amount of compressed air is blown in the ceramic filter of the high-temperature dust collector 3 from a compressed air supply device 5 to shake down the dust adhered to the surface of the ceramic filter. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は、廃棄物の燃焼等により発生する高温燃焼ガス中のダストを筒状のセラミックフィルタにより除去する高温集塵装置のダスト払い落し制御方法および制御装置に関するものである。   The present invention relates to a dust removal control method and a control device for a high-temperature dust collector that removes dust in a high-temperature combustion gas generated by combustion of waste by a cylindrical ceramic filter.

廃棄物焼却炉や焼却灰の溶融炉等にて発生する高温の燃焼ガスを集塵する集塵装置として、耐熱性を有する筒状のセラミックフィルタを用いた高温集塵装置が用いられている(特許文献1参照)。セラミックフィルタは、その特性から高温雰囲気においても使用可能であるため、ボイラよりも上流側に設置することができる。こうして、燃焼ガス中のダストをボイラ上流で除去することにより、ボイラへのダストの付着を抑制し、過熱管の腐食を防止し、ボイラ蒸気の温度を高くすることができ、これによって熱回収効率を向上させることができる。   As a dust collector that collects high-temperature combustion gas generated in a waste incinerator or incineration ash melting furnace, a high-temperature dust collector using a heat-resistant cylindrical ceramic filter is used ( Patent Document 1). Since the ceramic filter can be used even in a high-temperature atmosphere due to its characteristics, the ceramic filter can be installed upstream of the boiler. In this way, by removing dust in the combustion gas upstream of the boiler, dust adhesion to the boiler can be suppressed, corrosion of the superheated tube can be prevented, and the boiler steam temperature can be increased, thereby improving the heat recovery efficiency. Can be improved.

ところで、この種の高温集塵装置においては、筒状のセラミックフィルタの外側からダストを含む高温燃焼ガスが供給され、セラミックフィルタの細孔を有するセラミック層にてダストが除去され、精製された燃焼ガスがセラミックフィルタの内側空間を通って排出される。このようなダスト除去機構となっているので、燃焼ガスを連続的に流通させると、セラミックフィルタの外表面にダストが付着、堆積し、細孔が目詰まりを起こすため、定期的にセラミックフィルタの内側空間に圧縮空気を供給する(逆洗浄する)ことで、ダストを払い落すようにされている(特許文献2参照)。   By the way, in this type of high-temperature dust collector, high-temperature combustion gas containing dust is supplied from the outside of the cylindrical ceramic filter, and dust is removed and purified by a ceramic layer having pores of the ceramic filter. Gas is exhausted through the inner space of the ceramic filter. Since it is such a dust removal mechanism, if the combustion gas is circulated continuously, dust adheres and accumulates on the outer surface of the ceramic filter and clogs the pores. By supplying compressed air to the inner space (reverse cleaning), dust is removed (see Patent Document 2).

図4には、従来のダスト払い落し制御装置のシステム構成図が示されている。図示のように、焼却炉50の燃焼ガス通路51には、ボイラ52の上流側にセラミックフィルタを備えた高温集塵装置53が設置されている。この高温集塵装置53には圧縮空気供給装置54が接続され、制御装置55からの指令信号によりその圧縮空気供給装置54からセラミックフィルタの内側空間に圧縮空気が供給される。また、高温集塵装置53の入口側と出口側との差圧を演算する差圧検出装置56が設けられ、この差圧検出装置56からの信号に基づき、前記制御装置55はその差圧が所定値以上になったときに、セラミックフィルタに目詰まりが発生したと判断され、圧縮空気供給装置54に指令信号が送信されてフィルタ逆洗のための圧縮空気が供給される。   FIG. 4 shows a system configuration diagram of a conventional dust removal control device. As shown in the figure, a high-temperature dust collector 53 having a ceramic filter is installed in the combustion gas passage 51 of the incinerator 50 on the upstream side of the boiler 52. A compressed air supply device 54 is connected to the high temperature dust collector 53, and compressed air is supplied from the compressed air supply device 54 to the inner space of the ceramic filter by a command signal from the control device 55. Further, a differential pressure detecting device 56 for calculating the differential pressure between the inlet side and the outlet side of the high temperature dust collecting device 53 is provided. Based on a signal from the differential pressure detecting device 56, the control device 55 detects the differential pressure. When the predetermined value is exceeded, it is determined that the ceramic filter is clogged, and a command signal is transmitted to the compressed air supply device 54 to supply compressed air for backwashing the filter.

しかしながら、前記従来のダスト払い落し制御装置では、高温集塵装置53の入口側と出口側との差圧が上昇した際に、言い換えればフィルタに目詰まりが発生した際に圧縮空気を供給するように構成されているため、フィルタに詰まったダストを効果的に除去できない場合があり、圧縮空気量を多くしたり、圧縮空気圧を大きくしたり、あるいは供給頻度を多くしたりする必要があった。そして、このようにダスト払い落しのための空気量、払い落し回数等を多くすると、燃焼ガス温度が低下し、高温集塵装置53の下流側に配されるボイラ52での熱回収効率が低下してしまうという問題点がある。   However, the conventional dust removal control device supplies compressed air when the differential pressure between the inlet side and the outlet side of the high-temperature dust collector 53 increases, in other words, when the filter is clogged. Therefore, there is a case where dust clogged in the filter cannot be effectively removed, and it is necessary to increase the amount of compressed air, increase the compressed air pressure, or increase the supply frequency. When the amount of air for dust removal, the number of times of dust removal, etc. are increased in this way, the combustion gas temperature decreases, and the heat recovery efficiency in the boiler 52 disposed downstream of the high temperature dust collector 53 decreases. There is a problem that it will.

特開2001−108216号公報JP 2001-108216 A 特開2001−179024号公報JP 2001-179024 A

本発明は、前述のような問題点に鑑みてなされたもので、燃焼ガス温度の低下を抑制しつつ、セラミックフィルタの目詰まりを効果的に防止することのできる高温集塵装置のダスト払い落し制御方法および制御装置を提供することを目的とするものである。   The present invention has been made in view of the above-described problems, and dust removal of a high-temperature dust collector that can effectively prevent clogging of a ceramic filter while suppressing a decrease in combustion gas temperature. It is an object of the present invention to provide a control method and a control device.

本発明者らは、焼却炉出口のセラミックフィルタの目詰まりは、燃焼ガス中のダストやヒュームに含有されるNa、K、Caなどの成分が作用して生じることを見出した。Na、K、Caといったアルカリ金属やアルカリ土類金属の塩化物等は低融点のため、燃焼ガス温度が高いほど融解する。そして、この融解した塩化物等はセラミックフィルタの細孔に侵入、固着し、細孔の目詰まりを引き起こす。このようなことから、本発明者らは、セラミックフィルタの目詰まりは高温集塵装置の入口温度に依存するとの知見を得、本発明を完成させるに至った。   The present inventors have found that clogging of the ceramic filter at the outlet of the incinerator is caused by the action of components such as Na, K, and Ca contained in dust and fume in the combustion gas. Alkali metals such as Na, K, and Ca, and chlorides of alkaline earth metals have a low melting point, and therefore melt as the combustion gas temperature increases. The molten chloride or the like enters and adheres to the pores of the ceramic filter, causing clogging of the pores. For these reasons, the present inventors have obtained the knowledge that clogging of the ceramic filter depends on the inlet temperature of the high temperature dust collector, and have completed the present invention.

要するに、前記目的を達成するために、第1発明による高温集塵装置のダスト払い落し制御方法は、
筒状のセラミックフィルタにより高温燃焼ガス中のダストを除去する高温集塵装置において、
前記高温集塵装置の入口における燃焼ガス温度を検出し、この検出される燃焼ガス温度が予め設定される所定温度以上になったときに、前記セラミックフィルタの内部に所定量および所定圧の圧縮空気を吹き込んでセラミックフィルタの表面に付着したダストを払い落すことを特徴とするものである。
In short, in order to achieve the above object, the dust removal control method of the high-temperature dust collector according to the first invention is:
In a high-temperature dust collector that removes dust in high-temperature combustion gas with a cylindrical ceramic filter,
When the combustion gas temperature at the inlet of the high-temperature dust collector is detected and the detected combustion gas temperature is equal to or higher than a predetermined temperature, the compressed air having a predetermined amount and a predetermined pressure is placed inside the ceramic filter. The dust adhering to the surface of the ceramic filter is blown off.

また、第2発明による高温集塵装置のダスト払い落し制御装置は、
筒状のセラミックフィルタにより高温燃焼ガス中のダストを除去する高温集塵装置において、
(a)前記セラミックフィルタの内部に圧縮空気を吹き込む圧縮空気供給手段と、
(b)前記高温集塵装置の入口における燃焼ガス温度を検出する温度検出手段と、
(c)前記高温集塵装置の入口における燃焼ガス温度と、前記圧縮空気供給手段より供給する圧縮空気量、圧縮空気圧および圧縮空気供給回数との関係を示すデータを記憶する記憶手段と、
(d)前記温度検出手段により検出される燃焼ガス温度が予め設定される所定温度以上になったときに、その燃焼ガス温度に対応する圧縮空気量、圧縮空気圧および圧縮空気供給回数のデータを前記記憶手段より読み出して指令値を演算し、この指令値に基づいて前記圧縮空気供給手段を制御する制御手段とを備えることを特徴とするものである。
The dust removal control device for the high-temperature dust collector according to the second invention is
In a high-temperature dust collector that removes dust in high-temperature combustion gas with a cylindrical ceramic filter,
(A) compressed air supply means for blowing compressed air into the ceramic filter;
(B) temperature detection means for detecting the combustion gas temperature at the inlet of the high-temperature dust collector;
(C) storage means for storing data indicating the relationship between the combustion gas temperature at the inlet of the high-temperature dust collector and the amount of compressed air supplied from the compressed air supply means, the compressed air pressure, and the number of times of compressed air supply;
(D) When the combustion gas temperature detected by the temperature detection means is equal to or higher than a predetermined temperature set in advance, the compressed air amount, compressed air pressure and compressed air supply frequency data corresponding to the combustion gas temperature are And a control means for calculating a command value by reading from the storage means and controlling the compressed air supply means based on the command value.

前記第1発明および第2発明によれば、高温集塵装置の入口における燃焼ガス温度に応じてセラミックフィルタの表面に付着したダストを払い落すための圧縮空気量、圧縮空気圧および圧縮空気供給回数が制御されるので、圧縮空気量、圧縮空気圧および圧縮空気供給回数が適切に制御され、セラミックフィルタの目詰まりを効果的に抑制し、かつ圧縮空気供給による燃焼ガス温度の低下を抑制することができ、これによって熱回収率の低下を従来のものに比べてより抑制することができる。また、圧縮空気供給手段を効率的に運転することができるので、動力および電気使用量も低減させることができる。   According to the first and second inventions, the amount of compressed air, the compressed air pressure, and the number of times compressed air is supplied to remove dust adhering to the surface of the ceramic filter in accordance with the combustion gas temperature at the inlet of the high temperature dust collector. Therefore, the amount of compressed air, compressed air pressure, and the number of times of compressed air supply are appropriately controlled to effectively suppress clogging of the ceramic filter and to suppress a decrease in combustion gas temperature due to compressed air supply. As a result, the reduction in the heat recovery rate can be further suppressed as compared with the conventional one. Moreover, since the compressed air supply means can be operated efficiently, power and electricity consumption can also be reduced.

次に、本発明による高温集塵装置のダスト払い落し制御方法および制御装置の具体的な実施の形態について、図面を参照しつつ説明する。   Next, specific embodiments of a dust removal control method and a control device for a high-temperature dust collector according to the present invention will be described with reference to the drawings.

図1には、本発明の一実施形態に係る高温集塵装置のダスト払い落し制御装置のシステム構成図が示され、図2には、本実施形態の高温集塵装置の部分断面図が示されている。   FIG. 1 shows a system configuration diagram of a dust removal control device for a high-temperature dust collector according to an embodiment of the present invention, and FIG. 2 shows a partial cross-sectional view of the high-temperature dust collector of this embodiment. Has been.

図1に示されるように、本実施形態において、焼却炉1の燃焼ガス通路2には、セラミックフィルタを備えた高温集塵装置3が設置され、この高温集塵装置3の下流側にボイラ4が設置されている。そして、高温集塵装置3には圧縮空気供給装置(本発明の「圧縮空気供給手段」に対応)5が接続されて、必要時にその圧縮空気供給装置5から高温集塵装置3内のセラミックフィルタに逆洗空気が供給される。   As shown in FIG. 1, in this embodiment, a high-temperature dust collector 3 having a ceramic filter is installed in the combustion gas passage 2 of the incinerator 1, and a boiler 4 is disposed downstream of the high-temperature dust collector 3. Is installed. A compressed air supply device (corresponding to “compressed air supply means” of the present invention) 5 is connected to the high temperature dust collector 3, and the ceramic filter in the high temperature dust collector 3 is supplied from the compressed air supply device 5 when necessary. Is supplied with backwash air.

前記高温集塵装置3は、図2に示されるように(全体図を省略する。)、円筒状の胴部を有する外筒6と、この外筒6の内側で同心円状に設けられる内筒7とを有するケーシングを備え、このケーシング内に外筒6と内筒7とに囲まれる内部空間8が画成され、この内部空間8の上方に燃焼ガス(排ガス)を導入するガス導入口が設けられるとともに、内部空間8の下方にダストを溜めて排出するためのホッパが設けられて構成されている。また、内筒7の内部空間9の上方には清浄ガスを導出するガス導出口が設けられている。   As shown in FIG. 2 (the whole figure is omitted), the high-temperature dust collector 3 includes an outer cylinder 6 having a cylindrical body, and an inner cylinder provided concentrically inside the outer cylinder 6. 7, an inner space 8 surrounded by the outer cylinder 6 and the inner cylinder 7 is defined in the casing, and a gas inlet for introducing combustion gas (exhaust gas) is provided above the inner space 8. In addition to being provided, a hopper for collecting and discharging dust is provided below the internal space 8. In addition, a gas outlet for deriving clean gas is provided above the inner space 9 of the inner cylinder 7.

前記外筒6と内筒7との間には、複数個(図2では1個のみを図示)の筒状のセラミックフィルタ10が懸架されている。これらセラミックフィルタ10は、内筒7の中心軸線を中心として放射状に、かつ上下に多段に配されている。   A plurality of (only one is shown in FIG. 2) cylindrical ceramic filters 10 are suspended between the outer cylinder 6 and the inner cylinder 7. These ceramic filters 10 are arranged radially in the upper and lower stages with the central axis of the inner cylinder 7 as the center.

各セラミックフィルタ10は、一端部が、外筒6に穿設された貫通孔11に嵌合されて固定されるとともに、他端部が、内筒7に穿設されたガス通過口12のやや大径にされた外側端部に嵌合固定されて支持されている。なお、ガス通過口12の径はセラミックフィルタ10の内径とほぼ同径にされている。   Each ceramic filter 10 has one end fitted into and fixed to a through hole 11 drilled in the outer cylinder 6, and the other end is somewhat of the gas passage port 12 drilled in the inner cylinder 7. The outer end portion having a large diameter is fitted and fixed and supported. The diameter of the gas passage port 12 is substantially the same as the inner diameter of the ceramic filter 10.

前記セラミックフィルタ10の一端部には逆洗空気吹込み口13が設けられ、この逆洗空気吹込み口13に、パルス管14から分岐された逆洗空気吹込み管15の先端部が挿入されている。   A backwash air blowing port 13 is provided at one end of the ceramic filter 10, and a tip of a backwash air blowing tube 15 branched from the pulse tube 14 is inserted into the backwash air blowing port 13. ing.

こうして、セラミックフィルタ10の逆洗に際しては、パルス管14に圧縮空気が供給されることで、逆洗空気吹込み管15から逆洗空気吹込み口13を経てセラミックフィルタ10内部に圧縮空気(逆洗空気)が噴出され、セラミックフィルタ10の外表面に付着したダストの払い落しが行われる。なお、逆洗空気は、直進してガス通過口12に流れ、その際に流量が絞られて急激な圧力低下を起こさず、セラミックフィルタ10の内部で所要の圧力に保たれる。   In this way, when the ceramic filter 10 is backwashed, compressed air is supplied to the pulse tube 14, so that compressed air (reverse backflow) enters the ceramic filter 10 from the backwash air blowing tube 15 through the backwash air inlet 13. Washing air) is ejected, and dust attached to the outer surface of the ceramic filter 10 is removed. Note that the backwash air travels straight and flows to the gas passage port 12, and at that time, the flow rate is reduced, and a rapid pressure drop does not occur, and the required pressure is maintained inside the ceramic filter 10.

図1のシステム構成図に戻って、高温集塵装置3の入口側の燃焼ガス通路2には、その燃焼ガス通路2を通過する燃焼ガスの温度を検出する温度検出器(本発明の「温度検出手段」に対応)16が設置され、この温度検出器16にて検出された温度検出信号が制御装置17に送信される。制御装置17は、入力信号等に基づき所要の演算を行って指令信号を出力する演算部(本発明の「制御手段」に対応)17aと、この演算に必要なデータおよび所要のプログラム等を記憶するメモリ(本発明の「記憶手段」に対応)17bとを備えている。この制御装置17の演算部17aでは、後述する所要の演算を行い、その演算結果に基づき圧縮空気供給装置5に指令信号が送信され、この圧縮空気供給装置5が運転される。   Returning to the system configuration diagram of FIG. 1, the combustion gas passage 2 on the inlet side of the high-temperature dust collector 3 has a temperature detector that detects the temperature of the combustion gas passing through the combustion gas passage 2 (“temperature” of the present invention). (Corresponding to “detection means”) 16 is installed, and a temperature detection signal detected by the temperature detector 16 is transmitted to the control device 17. The control device 17 stores a calculation unit (corresponding to the “control unit” of the present invention) 17a that performs a required calculation based on an input signal or the like and outputs a command signal, data necessary for the calculation, a required program, and the like. And a memory (corresponding to the “storage means” of the present invention) 17b. The calculation unit 17a of the control device 17 performs a required calculation described later, a command signal is transmitted to the compressed air supply device 5 based on the calculation result, and the compressed air supply device 5 is operated.

ところで、本発明者らの研究によれば、焼却炉出口のセラミックフィルタの目詰まりは、燃焼ガス中のダストやヒュームに含有されるNa、K、Caなどの塩化物等が融解してセラミックフィルタの細孔に侵入、固着することにより生じることがわかった。これらNa、K、Caといったアルカリ金属やアルカリ土類金属の塩化物等は低融点のため、燃焼ガス温度が高いほど融解することから、セラミックフィルタの目詰まりは高温集塵装置の入口温度に依存するものと考えられる。そこで、燃焼ガス温度とダストやヒュームの融点との関係から、ダストによるセラミックフィルタ10の目詰まりを防止するためのデータ(もしくは関係式)を制御装置17のメモリ17b内に予め設定、記憶しておくことで、圧縮空気供給装置5を効果的に運転することが可能になる。   By the way, according to the study by the present inventors, clogging of the ceramic filter at the incinerator outlet is caused by melting of chlorides such as Na, K and Ca contained in dust and fume in the combustion gas. It was found that it was caused by intruding into and adhering to the pores. Since alkali metal and alkaline earth metal chlorides such as Na, K, and Ca have a low melting point, they melt as the combustion gas temperature increases, so clogging of the ceramic filter depends on the inlet temperature of the high-temperature dust collector. It is thought to do. Therefore, data (or a relational expression) for preventing clogging of the ceramic filter 10 due to dust is preset and stored in the memory 17b of the control device 17 based on the relationship between the combustion gas temperature and the melting point of dust and fume. By setting it, it becomes possible to drive the compressed air supply device 5 effectively.

本実施形態では、圧縮空気の供給制御のためのデータ(もしくは演算式)として、図3に示されるように、燃焼ガス温度(℃)に対応するセラミックフィルタ1本当たりの圧縮空気量(L/本)、圧縮空気圧(MPa)および供給回数(回/h)のデータをメモリ17bに記憶させておき、温度検出器16にて検出される燃焼ガス温度に基づき、このメモリ17bのデータを参照して演算部17aにて必要な圧縮空気量、圧縮空気圧および供給回数を演算し、圧縮空気供給装置5に指令信号を送信する。   In the present embodiment, as data (or an arithmetic expression) for compressed air supply control, as shown in FIG. 3, the amount of compressed air (L / L) per ceramic filter corresponding to the combustion gas temperature (° C.). The data of the compressed air pressure (MPa) and the number of times of supply (times / h) are stored in the memory 17b, and the data in the memory 17b is referred to based on the combustion gas temperature detected by the temperature detector 16. Then, the calculation unit 17 a calculates the necessary compressed air amount, compressed air pressure, and the number of times of supply, and transmits a command signal to the compressed air supply device 5.

ここで、図3に示されるデータ(もしくは演算式)は、焼却炉1に投入されるごみ質(発熱量、水分など)等に応じて変わるため、メモリ17bにはそれらごみ質等に対応する複数のデータが記憶されている。   Here, since the data (or arithmetic expression) shown in FIG. 3 changes according to the waste quality (calorific value, moisture, etc.) put into the incinerator 1, the memory 17b corresponds to the waste quality. A plurality of data is stored.

本実施形態の高温集塵装置のダスト払い落し制御装置は以上のように構成されているので、筒状のセラミックフィルタ10内に供給される圧縮空気の空気量、空気圧および供給回数を適切に制御することができ、これによってセラミックフィルタ10の目詰まりを効果的に抑制するとともに、圧縮空気供給による燃焼ガス温度の低下を抑制することができる。したがって、熱回収率の低下を抑制することができるだけでなく、圧縮空気供給装置5を効率的に運転することができるので、動力および電気使用量も低減することができるという優れた効果を有している。   Since the dust removal control device of the high-temperature dust collector of the present embodiment is configured as described above, the air amount, air pressure, and number of times of supply of compressed air supplied into the cylindrical ceramic filter 10 are appropriately controlled. Accordingly, clogging of the ceramic filter 10 can be effectively suppressed, and a decrease in the combustion gas temperature due to the supply of compressed air can be suppressed. Therefore, not only can the decrease in the heat recovery rate be suppressed, but also the compressed air supply device 5 can be operated efficiently, so that the power and the amount of electricity used can be reduced. ing.

本発明の一実施形態に係る高温集塵装置のダスト払い落し制御装置のシステム構成図The system block diagram of the dust removal control apparatus of the high temperature dust collector which concerns on one Embodiment of this invention. 本実施形態の高温集塵装置の部分断面図Partial sectional view of the high temperature dust collector of this embodiment 燃焼ガス温度と圧縮空気量、圧縮空気圧および供給回数との関係を示すグラフGraph showing the relationship between combustion gas temperature, compressed air volume, compressed air pressure, and number of supply 従来のダスト払い落し制御装置のシステム構成図System configuration diagram of a conventional dust removal control device

符号の説明Explanation of symbols

1 焼却炉
2 燃焼ガス通路
3 高温集塵装置
4 ボイラ
5 圧縮空気供給装置
6 外筒
7 内筒
10 セラミックフィルタ
13 逆洗空気吹込み口
14 パルス管
15 逆洗空気吹込み管
16 温度検出器
17 制御装置
17a 演算部
17b メモリ
DESCRIPTION OF SYMBOLS 1 Incinerator 2 Combustion gas passage 3 High temperature dust collector 4 Boiler 5 Compressed air supply device 6 Outer cylinder 7 Inner cylinder 10 Ceramic filter 13 Backwash air blowing port 14 Pulse tube 15 Backwash air blowing tube 16 Temperature detector 17 Control device 17a arithmetic unit 17b memory

Claims (2)

筒状のセラミックフィルタにより高温燃焼ガス中のダストを除去する高温集塵装置において、
前記高温集塵装置の入口における燃焼ガス温度を検出し、この検出される燃焼ガス温度が予め設定される所定温度以上になったときに、前記セラミックフィルタの内部に所定量および所定圧の圧縮空気を吹き込んでセラミックフィルタの表面に付着したダストを払い落すことを特徴とする高温集塵装置のダスト払い落し制御方法。
In a high-temperature dust collector that removes dust in high-temperature combustion gas with a cylindrical ceramic filter,
When the combustion gas temperature at the inlet of the high-temperature dust collector is detected and the detected combustion gas temperature is equal to or higher than a predetermined temperature, the compressed air having a predetermined amount and a predetermined pressure is placed inside the ceramic filter. A dust removal control method for a high-temperature dust collector, wherein dust attached to the surface of the ceramic filter is removed by blowing air.
筒状のセラミックフィルタにより高温燃焼ガス中のダストを除去する高温集塵装置において、
(a)前記セラミックフィルタの内部に圧縮空気を吹き込む圧縮空気供給手段と、
(b)前記高温集塵装置の入口における燃焼ガス温度を検出する温度検出手段と、
(c)前記高温集塵装置の入口における燃焼ガス温度と、前記圧縮空気供給手段より供給する圧縮空気量、圧縮空気圧および圧縮空気供給回数との関係を示すデータを記憶する記憶手段と、
(d)前記温度検出手段により検出される燃焼ガス温度が予め設定される所定温度以上になったときに、その燃焼ガス温度に対応する圧縮空気量、圧縮空気圧および圧縮空気供給回数のデータを前記記憶手段より読み出して指令値を演算し、この指令値に基づいて前記圧縮空気供給手段を制御する制御手段とを備えることを特徴とする高温集塵装置のダスト払い落し制御装置。
In a high-temperature dust collector that removes dust in high-temperature combustion gas with a cylindrical ceramic filter,
(A) compressed air supply means for blowing compressed air into the ceramic filter;
(B) temperature detection means for detecting the combustion gas temperature at the inlet of the high-temperature dust collector;
(C) storage means for storing data indicating the relationship between the combustion gas temperature at the inlet of the high-temperature dust collector and the amount of compressed air supplied from the compressed air supply means, the compressed air pressure, and the number of times of compressed air supply;
(D) When the combustion gas temperature detected by the temperature detection means is equal to or higher than a predetermined temperature set in advance, the compressed air amount, compressed air pressure and compressed air supply frequency data corresponding to the combustion gas temperature are A dust removal control device for a high-temperature dust collector, comprising: a control unit that reads out from a storage unit, calculates a command value, and controls the compressed air supply unit based on the command value.
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Publication number Priority date Publication date Assignee Title
JPH0326310A (en) * 1989-06-16 1991-02-04 Metallges Ag Method for avoiding generation of highly condensed aromatic hydrocarbon and dioxins in incineration facility and apparatus for executing this method
JPH05212227A (en) * 1992-02-04 1993-08-24 Ishikawajima Harima Heavy Ind Co Ltd Method for protecting high temperature and high pressure dust removal equipment
JPH0650127A (en) * 1992-07-30 1994-02-22 Isuzu Motors Ltd Particulate removal device
JPH0649718U (en) * 1992-12-10 1994-07-08 いすゞ自動車株式会社 Exhaust gas purification device for engine
JPH06336912A (en) * 1993-05-31 1994-12-06 Isuzu Ceramics Kenkyusho:Kk Tubular ceramics filter
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