JP2008185267A - Heat storage type deodorizer - Google Patents

Heat storage type deodorizer Download PDF

Info

Publication number
JP2008185267A
JP2008185267A JP2007019123A JP2007019123A JP2008185267A JP 2008185267 A JP2008185267 A JP 2008185267A JP 2007019123 A JP2007019123 A JP 2007019123A JP 2007019123 A JP2007019123 A JP 2007019123A JP 2008185267 A JP2008185267 A JP 2008185267A
Authority
JP
Japan
Prior art keywords
heat storage
gas
combustible
heat
treated
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
JP2007019123A
Other languages
Japanese (ja)
Inventor
Yuichi Nakajima
優一 中島
Tadao Matsumoto
忠雄 松本
Yoshinori Kaneda
芳典 金田
Isamu Aoki
勇 青木
Akira Noda
晃 野田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shinko Pantec Co Ltd
Original Assignee
Kobelco Eco Solutions Co Ltd
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 Kobelco Eco Solutions Co Ltd filed Critical Kobelco Eco Solutions Co Ltd
Priority to JP2007019123A priority Critical patent/JP2008185267A/en
Publication of JP2008185267A publication Critical patent/JP2008185267A/en
Pending legal-status Critical Current

Links

Images

Landscapes

  • Incineration Of Waste (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a heat storage type deodorizer capable of lowering costs by carrying out heat treatment by heating gas to be treated in a heat treatment area to a predetermined temperature without using a heating means such as a burner. <P>SOLUTION: The heat storage type deodorizer 1 is provided with a plurality of heat storage areas 3 housing heat storage material 31, and the heat treatment area 2 carrying out heat treatment of the gas to be treated supplied via at least one of the plurality of heat storage areas 3. A mixing means 5 is provided for mixing an inflammable combustion agent into the gas to be treated. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は、主として、工場等から排出される被処理ガスを脱臭するための蓄熱式脱臭装置に関し、特に、揮発性有機化合物(以下、「VOC」という)等の有機物を含んだ被処理ガスの脱臭に好適な蓄熱式脱臭装置に関する。   The present invention mainly relates to a heat storage type deodorization apparatus for deodorizing a gas to be processed discharged from a factory or the like, and in particular, a gas to be processed containing an organic substance such as a volatile organic compound (hereinafter referred to as “VOC”). The present invention relates to a heat storage deodorizing apparatus suitable for deodorization.

従来、工場等から排出されVOCを含んだ被処理ガスの脱臭装置として、例えば、被処理ガスを熱処理するための加熱処理領域と、該加熱処理領域へ導入する被処理ガスを予熱するための複数の蓄熱領域とを備えてなり、該蓄熱領域には、被処理ガスを予熱するための蓄熱材として例えばハニカム状の蓄熱材が収容されたものが知られている。   2. Description of the Related Art Conventionally, as a deodorizing apparatus for a gas to be processed discharged from a factory or the like and containing VOC, for example, a heat treatment region for heat treating the gas to be treated and a plurality of gas for preheating the gas to be treated introduced into the heat treatment region There is known a heat storage region in which, for example, a honeycomb-shaped heat storage material is accommodated as a heat storage material for preheating the gas to be processed.

かかる蓄熱式脱臭装置は、被処理ガスを何れか一つの蓄熱領域を通過させて加熱処理領域へと導入し、該加熱処理領域にて熱処理した後、他の蓄熱領域を出口として排出するように運転されるものであり、加熱処理領域内には、該加熱処理領域内の被処理ガスを所定の温度に昇温するための加熱手段として、例えばバーナーが設けられている(下記特許文献1参照)。   Such a heat storage type deodorizing apparatus is configured to introduce a gas to be treated through any one heat storage region into the heat treatment region, heat-treat in the heat treatment region, and then discharge the other heat storage region as an outlet. In the heat treatment region, for example, a burner is provided as a heating means for raising the gas to be treated in the heat treatment region to a predetermined temperature (see Patent Document 1 below). ).

かかる加熱手段は、燃焼ガスに空気を混合したものを燃焼させることで加熱処理領域内の被処理ガスを所定の温度に昇温するものである。
特開2000−171021号公報
Such a heating means raises the temperature of the gas to be treated in the heat treatment region to a predetermined temperature by burning a mixture of air and combustion gas.
JP 2000-171021 A

しかしながら、上記従来の蓄熱式脱臭装置にあっては、加熱処理領域内の被処理ガスを所定の温度に昇温するためには、加熱手段としてのバーナーの特性上、多量の空気を燃焼ガスに混合して空気の比率を高くした状態で燃焼しなければならず、そのために例えば空気供給用ブロワを用いなければならない。そうすると、例えば蓄熱式脱臭装置自体の設備費や稼動費などにおいてコストを低く抑えることが困難となる。   However, in the conventional heat storage deodorizing apparatus, in order to raise the temperature of the gas to be treated in the heat treatment region to a predetermined temperature, a large amount of air is used as the combustion gas due to the characteristics of the burner as the heating means. It must be mixed and burned at a high air ratio, and for this purpose, for example, an air supply blower must be used. If it does so, it will become difficult to hold down cost, for example in the installation expense of the thermal storage type deodorizing device itself, an operating cost, etc.

そこで、本発明は、上記従来の問題に鑑みてなされ、バーナー等の加熱手段を用いることなく加熱処理領域内の被処理ガスを所定の温度に昇温して熱処理することができるようにすることで、コストを低くすることができる蓄熱式脱臭装置を提供することを課題とする。   Accordingly, the present invention has been made in view of the above-described conventional problems, and enables heat treatment by raising the gas to be processed in the heat treatment region to a predetermined temperature without using a heating means such as a burner. Thus, it is an object to provide a heat storage type deodorizing apparatus capable of reducing the cost.

本発明は、上記課題を解決すべくなされたものであり、本発明に係る蓄熱式脱臭装置は、蓄熱材が収容された複数の蓄熱領域と、該複数の蓄熱領域の少なくとも1つを介して供給される被処理ガスを熱処理する加熱処理領域とを備える蓄熱式脱臭装置であって、前記被処理ガスに可燃性燃焼剤を混合する混合手段を備えることを特徴とする。   The present invention has been made to solve the above problems, and a heat storage deodorization apparatus according to the present invention includes a plurality of heat storage regions in which a heat storage material is accommodated and at least one of the plurality of heat storage regions. A regenerative deodorization apparatus comprising a heat treatment region for heat-treating a supplied gas to be treated, comprising a mixing means for mixing a combustible combustion agent with the gas to be treated.

該構成の蓄熱式脱臭装置にあっては、混合手段によって被処理ガスに可燃性燃焼剤を混合するので、被処理ガスと可燃性燃焼剤とが予め混合されて加熱処理領域に供給される。そうすると、加熱処理領域において可燃性燃焼剤が燃焼し、加熱処理領域内の被処理ガスを所定の温度に昇温して熱処理することができる。   In the heat storage type deodorizing apparatus having such a configuration, the combustible combustible is mixed with the gas to be processed by the mixing means, and therefore the gas to be processed and the combustible combustible are mixed in advance and supplied to the heat treatment region. Then, the combustible combustion agent burns in the heat treatment region, and the gas to be treated in the heat treatment region can be heated to a predetermined temperature and heat treated.

また、本発明に係る蓄熱式脱臭装置は、蓄熱材が収容された複数の蓄熱領域と、該複数の蓄熱領域の少なくとも1つに被処理ガスを供給する供給側ダクトと、前記複数の蓄熱領域と連通され前記被処理ガスを熱処理する加熱処理領域とを備える蓄熱式脱臭装置であって、前記供給側ダクト内に液体状の可燃性燃焼剤を噴霧して前記被処理ガスに混合する混合手段を備えることを特徴とする。   The heat storage deodorization apparatus according to the present invention includes a plurality of heat storage regions in which a heat storage material is accommodated, a supply-side duct that supplies a gas to be treated to at least one of the plurality of heat storage regions, and the plurality of heat storage regions. A heat storage deodorizing device that is in communication with a heat treatment region for heat-treating the gas to be treated, and is a mixing unit that sprays a liquid combustible combustible into the supply-side duct and mixes it with the gas to be treated. It is characterized by providing.

該構成の蓄熱式脱臭装置にあっては、供給側ダクト内に液体状の可燃性燃焼剤を噴霧することで被処理ガスに可燃性燃焼剤を混合する混合手段を備えているので、被処理ガスと可燃性燃焼剤とが予め混合されて供給側ダクトから蓄熱領域を介して加熱処理領域に供給される。そうすると、加熱処理領域において可燃性燃焼剤が燃焼し、加熱処理領域内の被処理ガスを所定の温度に昇温して熱処理することができる。   In the heat storage type deodorizing apparatus having the above configuration, since it includes a mixing means for mixing the combustible combustible agent with the gas to be processed by spraying the liquid combustible combustible agent in the supply side duct, The gas and the combustible combustion agent are mixed in advance and supplied from the supply side duct to the heat treatment region through the heat storage region. Then, the combustible combustion agent burns in the heat treatment region, and the gas to be treated in the heat treatment region can be heated to a predetermined temperature and heat treated.

また、本発明に係る蓄熱式脱臭装置は、蓄熱材が収容された複数の蓄熱領域と、該複数の蓄熱領域の少なくとも1つに被処理ガスを供給する供給側ダクトと、前記複数の蓄熱領域と連通され前記被処理ガスを熱処理する加熱処理領域とを備える蓄熱式脱臭装置であって、前記供給側ダクト内に気化させた可燃性燃焼剤を導入して前記被処理ガスに混合する混合手段を備えることを特徴とする。   The heat storage deodorization apparatus according to the present invention includes a plurality of heat storage regions in which a heat storage material is accommodated, a supply-side duct that supplies a gas to be treated to at least one of the plurality of heat storage regions, and the plurality of heat storage regions. A heat storage deodorizing device that is in communication with a heat treatment region that heat-treats the gas to be treated, and is a mixing unit that introduces a combustible combustor that is vaporized into the supply-side duct and mixes it with the gas to be treated It is characterized by providing.

該構成の蓄熱式脱臭装置にあっては、供給側ダクト内に気化させた可燃性燃焼剤を導入して、該可燃性燃焼剤を被処理ガスに混合する混合手段を備えているので、被処理ガスと可燃性燃焼剤とが予め混合されて供給側ダクトから蓄熱領域を介して加熱処理領域に供給される。そうすると、加熱処理領域において可燃性燃焼剤が燃焼し、加熱処理領域内の被処理ガスを所定の温度に昇温して熱処理することができる。   The regenerative deodorization apparatus having the above configuration includes mixing means for introducing the combustible combustible vaporized into the supply side duct and mixing the combustible combustible with the gas to be treated. The processing gas and the combustible combustion agent are mixed in advance and supplied from the supply side duct to the heat treatment region via the heat storage region. Then, the combustible combustion agent burns in the heat treatment region, and the gas to be treated in the heat treatment region can be heated to a predetermined temperature and heat treated.

また、本発明に係る蓄熱式脱臭装置は、蓄熱材が収容された複数の蓄熱領域と、該複数の蓄熱領域の少なくとも1つを介して供給される被処理ガスを熱処理する加熱処理領域とを備える蓄熱式脱臭装置であって、液体状の可燃性燃焼剤が前記加熱処理領域内全体に拡散するように該可燃性燃焼剤を噴霧することによって、前記可燃性燃焼剤と前記被処理ガスとを混合する混合手段を備えることを特徴とする。   Moreover, the heat storage deodorizing apparatus according to the present invention includes a plurality of heat storage regions in which a heat storage material is accommodated, and a heat treatment region for heat-treating a gas to be processed supplied via at least one of the plurality of heat storage regions. A thermal storage type deodorizing device comprising: spraying the combustible combustible so that the liquid combustible combustible is diffused throughout the heat treatment region, whereby the combustible combustible and the gas to be treated are It is characterized by comprising mixing means for mixing.

該構成の蓄熱式脱臭装置にあっては、液体状の可燃性燃焼剤が前記加熱処理領域内全体に拡散するように該可燃性燃焼剤を噴霧することによって、前記可燃性燃焼剤と前記被処理ガスとを混合する混合手段を備えているので、加熱処理領域において被処理ガスと可燃性燃焼剤とが混合されて可燃性燃焼剤が燃焼する。ここで、液体状の可燃性燃焼剤は、前記加熱処理領域内全体に拡散するように噴霧されるので、加熱処理領域の全域に亘って被処理ガスと可燃性燃焼剤とが均一に混合された状態となる。そうすると、加熱処理領域全域にて可燃性燃焼剤が燃焼し、加熱処理領域の温度分布が均一となり、効率良く被処理ガスを所定温度に昇温して熱処理することができる。   In the heat storage type deodorizing apparatus having the above configuration, the combustible combustible and the object to be burned are sprayed by spraying the combustible combustible so that the liquid combustible combustible is diffused throughout the heat treatment region. Since the mixing means for mixing the processing gas is provided, the gas to be processed and the combustible combustion agent are mixed in the heat treatment region, and the combustible combustion agent burns. Here, since the liquid combustible combustion agent is sprayed so as to diffuse throughout the heat treatment region, the gas to be treated and the combustible combustion agent are uniformly mixed throughout the heat treatment region. It becomes a state. As a result, the combustible combustor burns in the entire heat treatment region, the temperature distribution in the heat treatment region becomes uniform, and the gas to be treated can be efficiently heated to a predetermined temperature for heat treatment.

このように、本発明にかかる蓄熱式脱臭装置にあっては、混合手段によって被処理ガスに可燃性燃焼剤を混合するので、被処理ガスと可燃性燃焼剤とが予め混合されて加熱処理領域に供給され、可燃性燃焼剤が燃焼する。従って、従来のようにバーナー等の加熱手段を用いなくても加熱処理領域内の被処理ガスを所定の温度に昇温して熱処理することができ、コストを低くすることができるという効果を奏する。   Thus, in the regenerative deodorization apparatus according to the present invention, the combustible combustible is mixed with the gas to be treated by the mixing means, so the gas to be treated and the combustible combustible are mixed in advance and the heat treatment region. The combustible combustible is combusted. Therefore, the gas to be processed in the heat treatment region can be heated to a predetermined temperature and heat-treated without using a heating means such as a burner as in the prior art, and the cost can be reduced. .

また、本発明に係る蓄熱式脱臭装置にあっては、供給側ダクト内に液体状の可燃性燃焼剤を噴霧することで被処理ガスに可燃性燃焼剤を混合する混合手段を備えているので、被処理ガスと可燃性燃焼剤とが予め混合されて供給側ダクトから蓄熱領域を介して加熱処理領域に供給され、可燃性燃焼剤が燃焼する。従って、従来のようにバーナー等の加熱手段を用いずに加熱処理領域内の被処理ガスを所定の温度に昇温して熱処理することができ、コストを低くすることができるという効果を奏する。   Further, the heat storage deodorization apparatus according to the present invention includes a mixing means for mixing the combustible combustion agent with the gas to be treated by spraying a liquid combustible combustion agent in the supply side duct. The gas to be treated and the combustible combustion agent are mixed in advance and supplied from the supply side duct to the heat treatment region via the heat storage region, and the combustible combustion agent burns. Therefore, the gas to be processed in the heat treatment region can be heated to a predetermined temperature without using a heating means such as a burner as in the prior art, and the cost can be reduced.

また、本発明に係る蓄熱式脱臭装置にあっては、供給側ダクト内に気化させた可燃性燃焼剤を導入して、該可燃性燃焼剤を被処理ガスに混合する混合手段を備えているので、被処理ガスと可燃性燃焼剤とが予め混合されて供給側ダクトから蓄熱領域を介して加熱処理領域に供給され、可燃性燃焼剤が燃焼する。従って、従来のようにバーナー等の加熱手段を用いずに加熱処理領域内の被処理ガスを所定の温度に昇温して熱処理することができ、コストを低くすることができるという効果を奏する。   The heat storage deodorizing apparatus according to the present invention further includes a mixing means for introducing the combustible combustible vaporized into the supply side duct and mixing the combustible combustible with the gas to be treated. Therefore, the gas to be treated and the combustible combustion agent are mixed in advance and supplied from the supply duct through the heat storage region to the heat treatment region, and the combustible combustion agent burns. Therefore, the gas to be processed in the heat treatment region can be heated to a predetermined temperature without using a heating means such as a burner as in the prior art, and the cost can be reduced.

また、本発明に係る蓄熱式脱臭装置にあっては、液体状の可燃性燃焼剤が前記加熱処理領域内全体に拡散するように、該可燃性燃焼剤を噴霧することによって前記可燃性燃焼剤と前記被処理ガスとを混合することができる混合手段を備えているので、加熱処理領域の全域に亘って被処理ガスと可燃性燃焼剤とが均一に混合されて可燃性燃焼剤が燃焼する。従って、加熱処理領域の温度分布が均一となり、従来のようにバーナー等の加熱手段を用いなくても効率良く被処理ガスを所定温度に昇温して熱処理することができ、コストを低くすることができるという効果を奏する。   Further, in the heat storage type deodorizing apparatus according to the present invention, the combustible combustor is sprayed by spraying the combustible combustible so that the liquid combustible combustible is diffused throughout the heat treatment region. And the above-mentioned gas to be treated are provided, so that the gas to be treated and the combustible combustor are uniformly mixed over the entire heat treatment region, and the combustible combustor is burned. . Accordingly, the temperature distribution in the heat treatment region becomes uniform, and the gas to be treated can be efficiently heated to a predetermined temperature and heat treated without using a heating means such as a burner as in the prior art, thereby reducing the cost. There is an effect that can be.

以下、本発明に係る蓄熱式脱臭装置に関し、図面を参照しつつ詳細に説明する。
図1は、本発明の第一実施形態の蓄熱式脱臭装置1において、被処理ガスの流れの一態様を示したフロー図である。
Hereinafter, the heat storage deodorizing apparatus according to the present invention will be described in detail with reference to the drawings.
FIG. 1 is a flow diagram showing an aspect of the flow of the gas to be treated in the heat storage deodorization apparatus 1 of the first embodiment of the present invention.

該蓄熱式脱臭装置1は、蓄熱材31が収容された複数の蓄熱領域3と、該複数の蓄熱領域3の少なくとも1つに被処理ガスを供給する供給側ダクト4と、前記複数の蓄熱領域3と連通され、供給側ダクト4から蓄熱領域3を介して供給される前記被処理ガスを熱処理する加熱処理領域2と、前記被処理ガスに可燃性燃焼剤を混合する混合手段5とを備えてなり、本第一実施形態においては、3つの蓄熱領域3を備える所謂三塔式蓄熱式脱臭装置として構成されている。   The heat storage deodorizer 1 includes a plurality of heat storage regions 3 in which a heat storage material 31 is accommodated, a supply-side duct 4 that supplies a gas to be treated to at least one of the plurality of heat storage regions 3, and the plurality of heat storage regions. 3, a heat treatment region 2 that heat-treats the gas to be treated supplied from the supply side duct 4 through the heat storage region 3, and a mixing unit 5 that mixes a combustible combustion agent with the gas to be treated. Thus, the first embodiment is configured as a so-called three-column heat storage deodorizing device including three heat storage regions 3.

この蓄熱式脱臭装置1は、供給側ダクト4から蓄熱領域3内を通って加熱処理領域2内に供給された被処理ガスを加熱して該被処理ガス中に含まれるVOC等の有機物を酸化分解することで被処理ガスを脱臭することができるようになっている。   The heat storage deodorizer 1 oxidizes organic substances such as VOC contained in the gas to be processed by heating the gas to be processed supplied from the supply duct 4 through the heat storage region 3 and into the heat treatment region 2. By decomposing, the gas to be treated can be deodorized.

加熱処理領域2は、耐熱性の筐体21の内部領域である。該筐体21には、その天部211に例えばバーナー等の加熱手段6が設けられており、該加熱手段6にてその内部を昇温させることができるようになっている。尚、本第一実施形態においては、加熱手段6は、ガス経路61から導入される燃焼ガスを燃焼させることで加熱処理領域2内部を昇温することができるように構成されている。   The heat treatment area 2 is an internal area of the heat resistant casing 21. The casing 21 is provided with a heating means 6 such as a burner at the top 211, and the inside of the casing 21 can be heated by the heating means 6. In the first embodiment, the heating means 6 is configured to raise the temperature inside the heat treatment region 2 by burning the combustion gas introduced from the gas path 61.

蓄熱領域3は、被処理ガスが供給側ダクト4からその内部を通って加熱処理領域2へと導入される供給状態と、加熱処理領域2にて熱処理された被処理ガスがその内部を通って排出される排出状態とを変更可能に構成されている。   The heat storage region 3 has a supply state in which the gas to be treated is introduced from the supply side duct 4 through the inside thereof to the heat treatment region 2, and the gas to be treated which is heat-treated in the heat treatment region 2 passes through the inside. It is configured such that the discharged state can be changed.

蓄熱領域3に収容されている蓄熱材31は、蓄熱領域3が供給状態のときには、その内部を通過する被処理ガスを予熱し、蓄熱領域3が排出状態のときには、その内部を通過する高温の被処理ガスから熱を吸収するように構成されている。尚、蓄熱材31としては、例えば、複数のガス流路を区画形成して被処理ガスとの伝熱効率を向上すべく、ハニカム状に形成された金属製或いはセラミック製のものを使用することができる。   The heat storage material 31 accommodated in the heat storage region 3 preheats the gas to be processed that passes through the interior when the heat storage region 3 is in the supply state, and the high temperature material that passes through the interior when the heat storage region 3 is in the discharge state. It is configured to absorb heat from the gas to be processed. In addition, as the heat storage material 31, for example, a metal or ceramic material formed in a honeycomb shape may be used in order to partition a plurality of gas flow paths and improve heat transfer efficiency with the gas to be processed. it can.

供給側ダクト4は、図示しないガスタンク内の被処理ガスを各蓄熱領域3に供給しうるように配されており、配管41と該配管41の途中に介装された複数の開閉バルブ42とを備えてなり、本第一実施形態においては、各蓄熱領域3へと被処理ガスを供給するための流れを形成する供給ファンFが介装されている。尚、供給ファンFは前記複数の開閉バルブ42よりも上流側に配備されている。また、前記開閉バルブ42を操作することによって、蓄熱領域3が供給状態となったり、又は、その状態が解除されたりする。   The supply side duct 4 is arranged so that the gas to be treated in a gas tank (not shown) can be supplied to each heat storage region 3. The supply side duct 4 includes a pipe 41 and a plurality of opening / closing valves 42 interposed in the middle of the pipe 41. In the first embodiment, a supply fan F that forms a flow for supplying the gas to be processed to each heat storage region 3 is interposed. The supply fan F is disposed upstream of the plurality of opening / closing valves 42. Further, by operating the on-off valve 42, the heat storage region 3 is in a supply state or the state is released.

前記混合手段5は、供給側ダクト4から供給状態の蓄熱領域3を通過して加熱処理領域2へと供給される被処理ガスに可燃性燃焼剤を混合することができるように構成されている。具体的には、本第一実施形態における混合手段5は、供給側ダクト4内に液体状の可燃性燃焼剤を噴霧して被処理ガスに混合することができるように構成されている。本第一実施形態においては、混合手段5は、前記供給ファンFよりも上流側にて供給側ダクト4内に可燃性燃焼剤を噴霧することができるように配置されている。尚、混合手段5は、供給ファンFよりも下流側で且つ前記開閉バルブ42よりも上流側にて供給側ダクト4内に可燃性燃焼剤を噴霧することができるように配置されている場合や、開閉バルブ42よりも下流側にて供給側ダクト4内に可燃性燃焼剤を噴霧することができるように配置されている場合であってもよい。   The said mixing means 5 is comprised so that a combustible combustion agent can be mixed with the to-be-processed gas supplied to the heat processing area | region 2 through the heat storage area | region 3 of the supply state from the supply side duct 4. FIG. . Specifically, the mixing means 5 in the first embodiment is configured such that a liquid combustible combustion agent can be sprayed into the supply side duct 4 and mixed with the gas to be processed. In the first embodiment, the mixing means 5 is arranged so that the combustible combustion agent can be sprayed into the supply side duct 4 on the upstream side of the supply fan F. The mixing means 5 may be disposed so that the combustible combustion agent can be sprayed into the supply side duct 4 on the downstream side of the supply fan F and on the upstream side of the opening / closing valve 42. Further, it may be arranged such that the combustible combustion agent can be sprayed into the supply side duct 4 on the downstream side of the opening / closing valve 42.

混合手段5は、液体状の可燃性燃焼剤が貯留される燃焼剤タンク51と、該燃焼剤タンク51と前記供給側ダクト4とを連通し供給側ダクト4内に可燃性燃焼剤を霧状に噴出することができる噴霧経路52とを備え、該噴霧経路52の途中に介装され加熱処理領域2内に可燃性燃焼剤を噴霧するための流れを形成する噴霧ポンプP1が介装されて構成されている。尚、混合手段5は、供給側ダクト4内に可燃性燃焼剤を噴霧しうるものであれば特に限定されるものではなく、例えば、噴霧ポンプP1ではなく噴霧ファンを用いることも可能である。また、可燃性燃焼剤としては、例えば、重油やオイルなどの可燃性の液体を採用することができる。   The mixing means 5 communicates the combustion agent tank 51 in which the liquid combustible combustion agent is stored, the combustion agent tank 51 and the supply side duct 4, and the combustible combustion agent is atomized in the supply side duct 4. And a spray pump P1 that forms a flow for spraying the combustible combustion agent in the heat treatment region 2 and is provided in the middle of the spray path 52. It is configured. The mixing means 5 is not particularly limited as long as it can spray the combustible combustion agent into the supply-side duct 4, and for example, a spray fan can be used instead of the spray pump P1. Moreover, as a combustible combustion agent, combustible liquids, such as heavy oil and oil, are employable, for example.

また、蓄熱式脱臭装置1は、前記加熱処理領域2にて熱処理された被処理ガスを排出状態の蓄熱領域3から系外(例えば、大気中)に排出しうるように配された排出側ダクト7と、供給側ダクト4及び排出側ダクト7双方との被処理ガスの行き来が遮断された状態の蓄熱領域3内に溜まっている被処理ガスを供給側ダクト4又はガスタンクに返送するように配されたパージ用返送ダクト8とを備えている。尚、排出側ダクト7とパージ用返送ダクト8とは、それぞれ配管71,81と該配管71,81の途中に介装された複数の開閉バルブ72,82とを備えて構成されている。また、前記パージ用返送ダクト8は、少なくとも前記供給ファンFよりも上流側の供給側ダクト4或いはガスタンクに被処理ガスを返送しうるように構成されている。また、排出側ダクト7の開閉バルブ72を操作することによって、蓄熱領域3を排出状態としたり、又は、その状態を解除したりすることができる。   In addition, the heat storage deodorization apparatus 1 has a discharge side duct arranged so that the gas to be treated heat-treated in the heat treatment region 2 can be discharged from the heat storage region 3 in the discharged state to the outside of the system (for example, in the atmosphere). 7 and the treated gas accumulated in the heat storage region 3 in a state where the flow of the treated gas between the supply side duct 4 and the discharge side duct 7 is interrupted is returned to the supply side duct 4 or the gas tank. The purge return duct 8 is provided. The discharge side duct 7 and the purge return duct 8 are respectively provided with pipes 71, 81 and a plurality of on-off valves 72, 82 interposed in the middle of the pipes 71, 81. The purge return duct 8 is configured to return the gas to be processed to at least the supply side duct 4 or the gas tank upstream of the supply fan F. Further, by operating the open / close valve 72 of the discharge side duct 7, the heat storage region 3 can be discharged or released.

本第一実施形態の蓄熱式脱臭装置1に於いて、通常運転によって被処理ガスの脱臭をするには、まず、第一工程として、供給側ダクト4、排出側ダクト7、及びパージ用返送ダクト8に設けられている各開閉バルブ42,72,82の開閉操作によって、各蓄熱領域3のうち、何れか1以上の蓄熱領域3(以下、第一蓄熱部という場合がある。)を供給状態とし、別の何れか1以上の蓄熱領域3(以下、第二蓄熱部という場合がある。)を排出状態とし、更に別の蓄熱領域3(以下、第3蓄熱部という場合がある。)を、その内部の被処理ガスが供給側ダクト4に返送され且つその後は被処理ガスの流入流出が禁止されるパージ状態とする。次に、第二工程として、第一蓄熱部をパージ状態、第二蓄熱部を供給状態、第三蓄熱部を排出状態とする。次に、第三工程として、第一蓄熱部を排出状態、第二蓄熱部をパージ状態、第三蓄熱部を供給状態とする。   In the heat storage deodorization apparatus 1 of the first embodiment, in order to deodorize the gas to be treated by normal operation, first, as a first step, the supply side duct 4, the discharge side duct 7, and the purge return duct By opening / closing the open / close valves 42, 72, and 82 provided in FIG. 8, any one or more of the heat storage regions 3 (hereinafter sometimes referred to as a first heat storage unit) is supplied. And any other one or more heat storage regions 3 (hereinafter sometimes referred to as second heat storage portions) are set in a discharged state, and another heat storage region 3 (hereinafter may be referred to as third heat storage portions). Then, a purge state is established in which the gas to be processed inside is returned to the supply-side duct 4 and thereafter the inflow and outflow of the gas to be processed are prohibited. Next, as the second step, the first heat storage unit is set to the purge state, the second heat storage unit is set to the supply state, and the third heat storage unit is set to the discharge state. Next, as the third step, the first heat storage unit is set to the discharge state, the second heat storage unit is set to the purge state, and the third heat storage unit is set to the supply state.

各工程において、被処理ガスは、前記混合手段5によって供給側ダクト4内に可燃性燃焼剤が噴霧されて、可燃性燃焼剤と予め混合された状態で供給側ダクト4内を流れて蓄熱領域3内に導入される。そして、混合された被処理ガスと可燃性燃焼剤とは、蓄熱領域3内の予め加熱された蓄熱材31から熱を受けることによって、通常750〜930℃にまで予熱されて該蓄熱領域3を通過して加熱処理領域2内へ供給され、加熱処理領域2内にて可燃性燃焼剤が燃焼して、加熱処理領域2内の被処理ガスを所定の温度に昇温して酸化させて脱臭することができる。従って、従来のようにバーナー等の加熱手段6を用いなくても、加熱処理領域2内の被処理ガスを熱処理して脱臭することができ、コストを低くすることができる。   In each step, the gas to be treated flows through the supply side duct 4 in a state where the combustible combustor is sprayed in the supply side duct 4 by the mixing means 5 and is mixed in advance with the combustible combustion agent, thereby storing heat. 3 is introduced. And the to-be-processed gas and the combustible combustion agent which were mixed are preheated to 750-930 degreeC normally by receiving heat from the preheated heat storage material 31 in the heat storage area | region 3, and this heat storage area | region 3 is made. It passes through and is supplied into the heat treatment region 2, and the combustible combustion agent burns in the heat treatment region 2, and the gas to be treated in the heat treatment region 2 is heated to a predetermined temperature and oxidized to deodorize it. can do. Therefore, even if the heating means 6 such as a burner is not used as in the prior art, the gas to be processed in the heat treatment region 2 can be deodorized by heat treatment, and the cost can be reduced.

しかも、従来のバーナーを用いた場合にあっては、局部的な加熱となって加熱処理領域2内の温度分布が偏る傾向があり、被処理ガスの脱臭が不十分となる虞があるが、被処理ガスと可燃性燃焼剤とが予め混合された状態で加熱処理領域2内に供給される構成とすることで、加熱処理領域2内の温度分布が均一となり確実に脱臭することができる。   Moreover, in the case of using a conventional burner, there is a tendency that the temperature distribution in the heat treatment region 2 becomes biased due to local heating, and the deodorization of the gas to be treated may be insufficient. By adopting a configuration in which the gas to be treated and the combustible combustion agent are supplied into the heat treatment region 2 in a premixed state, the temperature distribution in the heat treatment region 2 becomes uniform and can be deodorized reliably.

このように、脱臭処理された高温の被処理ガスは、排出状態の蓄熱領域3内を通過する際に、その内部の蓄熱材31によって吸熱され、通常20〜120℃にまで冷却されて大気中に排出される。尚、パージ状態の蓄熱領域3では、その内部の被処理ガスがパージ用返送ダクト8を経由して供給側ダクト4に返送され、その後は被処理ガスの流入流出が禁止されることとなる。   Thus, the deodorized high-temperature gas to be treated is absorbed by the heat storage material 31 inside when passing through the discharged heat storage region 3, and is usually cooled to 20 to 120 ° C. in the atmosphere. To be discharged. In the heat storage region 3 in the purge state, the gas to be processed therein is returned to the supply side duct 4 via the purge return duct 8, and thereafter the inflow and outflow of the gas to be processed are prohibited.

また、蓄熱材31を設けることによって、熱処理された被処理ガスの熱を利用して被処理ガスを効率よく予熱することができ、処理コスト等を更に低減することができる。また、供給状態の蓄熱領域3を次工程ではパージ状態とすることから、蓄熱領域3内に残存する被処理ガスが熱処理されずに大気中に排出されるような不具合を低減できる。   Moreover, by providing the heat storage material 31, the gas to be processed can be efficiently preheated using the heat of the gas to be processed that has been heat-treated, and the processing cost and the like can be further reduced. In addition, since the heat storage region 3 in the supply state is set to the purge state in the next step, it is possible to reduce a problem that the gas to be processed remaining in the heat storage region 3 is discharged into the atmosphere without being heat-treated.

尚、蓄熱領域3をベークアウトするには、開閉バルブ42,72,82の開閉操作によって、何れか1以上の蓄熱領域3(例えば、前記第一蓄熱部)を供給状態とし、別の何れか1以上の蓄熱領域3(例えば、前記第二蓄熱部)を排出状態とし、更に別の蓄熱領域3(例えば、前記第三蓄熱部)を空焼状態に設定して加熱処理領域2にて熱処理を行い、且つ、所定期間毎に、供給状態に設定された蓄熱領域3と排出状態に設定された蓄熱領域3とが、その設定状態が交互に交替するように操作する。このような一連の操作により、空焼状態に設定された蓄熱領域3は、比較的長時間に渡って加熱処理領域2から熱を受けることとなり、付着した有機物等が除去される。   In order to bake out the heat storage region 3, any one or more of the heat storage regions 3 (for example, the first heat storage unit) is set in a supply state by opening / closing the opening / closing valves 42, 72, and 82, One or more heat storage regions 3 (for example, the second heat storage unit) are set in an exhausted state, and another heat storage region 3 (for example, the third heat storage unit) is set in an air-burning state to perform heat treatment in the heat treatment region 2. The heat storage region 3 set in the supply state and the heat storage region 3 set in the discharge state are operated so that the set state alternates at predetermined intervals. As a result of such a series of operations, the heat storage region 3 set in the air-burning state receives heat from the heat treatment region 2 for a relatively long time, and attached organic matter and the like are removed.

また、このような一連の操作において、設定状態の切り替えは、特に限定されるものではないが、通常、供給状態の蓄熱領域3の導入側温度が20〜120℃まで低下したタイミングで行う。尚、切り替える際には、供給状態から排出状態とされる蓄熱領域3内の被処理ガスを、パージ用返送ダクト8を経由して、供給側ダクト4に返送する。かかる操作を行うことにより、切り替えのタイミングで蓄熱領域3内にある被処理ガスが未処理のまま大気中に排出されることを防止できる。   In such a series of operations, the switching of the setting state is not particularly limited, but is normally performed at a timing when the introduction side temperature of the heat storage region 3 in the supply state is lowered to 20 to 120 ° C. In addition, when switching, the to-be-processed gas in the heat storage area | region 3 made into a discharge | emission state from a supply state is returned to the supply side duct 4 via the return duct 8 for a purge. By performing such an operation, it is possible to prevent the gas to be processed in the heat storage region 3 from being discharged into the atmosphere without being processed at the switching timing.

図2は、本発明の第二実施形態の蓄熱式脱臭装置1において、被処理ガスの流れの一態様を示したフロー図である。尚、前記第一実施形態に係る蓄熱式脱臭装置1と同様の構成については、同じ符号を付すこととしその説明を省略する。   FIG. 2 is a flow diagram showing an aspect of the flow of the gas to be treated in the heat storage deodorization apparatus 1 of the second embodiment of the present invention. In addition, about the structure similar to the heat storage type deodorizing apparatus 1 which concerns on said 1st embodiment, the same code | symbol shall be attached | subjected and the description is abbreviate | omitted.

該蓄熱式脱臭装置1は、蓄熱材31が収容された複数の蓄熱領域3と、該複数の蓄熱領域3の少なくとも1つに被処理ガスを供給する供給側ダクト4と、前記複数の蓄熱領域3と連通され、供給側ダクト4から蓄熱領域3を介して供給される前記被処理ガスを熱処理する加熱処理領域2と、前記被処理ガスに可燃性燃焼剤を混合する混合手段5とを備えてなる。   The heat storage deodorizer 1 includes a plurality of heat storage regions 3 in which a heat storage material 31 is accommodated, a supply-side duct 4 that supplies a gas to be treated to at least one of the plurality of heat storage regions 3, and the plurality of heat storage regions. 3, a heat treatment region 2 that heat-treats the gas to be treated supplied from the supply side duct 4 through the heat storage region 3, and a mixing unit 5 that mixes a combustible combustion agent with the gas to be treated. It becomes.

前記混合手段5は、供給側ダクト4から供給状態の蓄熱領域3を通過して加熱処理領域2へと供給される被処理ガスに可燃性燃焼剤を混合することができるように構成されている。具体的には、本第二実施形態における混合手段5は、供給側ダクト4内に気化させた可燃性燃焼剤を導入して被処理ガスに混合することができるように構成されている。混合手段5は、前記供給ファンFよりも上流側にて供給側ダクト4内に気化した可燃性燃焼剤を送り込むことができるように配置されている。尚、混合手段5は、供給ファンFよりも下流側で且つ前記開閉バルブ42よりも上流側にて供給側ダクト4内に可燃性燃焼剤を噴霧することができるように配置されている場合や、開閉バルブ42よりも下流側にて供給側ダクト4内に可燃性燃焼剤を噴霧することができるように配置されている場合であってもよい。   The said mixing means 5 is comprised so that a combustible combustion agent can be mixed with the to-be-processed gas supplied to the heat processing area | region 2 through the heat storage area | region 3 of the supply state from the supply side duct 4. FIG. . Specifically, the mixing means 5 in the second embodiment is configured such that a combustible combustible vaporized in the supply side duct 4 can be introduced and mixed with the gas to be processed. The mixing means 5 is arranged so that the combustible combustible vaporized in the supply duct 4 can be fed upstream from the supply fan F. The mixing means 5 may be disposed so that the combustible combustion agent can be sprayed into the supply side duct 4 on the downstream side of the supply fan F and on the upstream side of the opening / closing valve 42. Further, it may be arranged such that the combustible combustion agent can be sprayed into the supply side duct 4 on the downstream side of the opening / closing valve 42.

混合手段5は、供給側ダクト4内に気化された可燃性燃焼剤を送り込むことができるものであれば特に限定されるものではないが、例えば、液体状の可燃性燃焼剤が貯留される燃焼剤タンク51と、該液体状の可燃性燃焼剤を気化させる気化手段53と、燃焼剤タンク51及び前記供給側ダクト4を連通する気化経路54とを備え、該気化経路54の途中に介装され供給側ダクト4内に可燃性燃焼剤を導入する導入ポンプP2を備えてなる。尚、可燃性燃焼剤としては、例えば、重油やオイルなどの可燃性の液体を採用することができる。   The mixing means 5 is not particularly limited as long as the combustible combustible vaporized in the supply-side duct 4 can be fed into the supply-side duct 4, but for example, combustion in which liquid combustible combustible is stored. A vaporizer tank 51, vaporization means 53 for vaporizing the liquid combustible combustion agent, and a vaporization path 54 communicating the combustion agent tank 51 and the supply side duct 4. And an introduction pump P <b> 2 for introducing a combustible combustion agent into the supply-side duct 4. In addition, as a combustible combustion agent, combustible liquids, such as heavy oil and oil, are employable, for example.

前記気化手段53は、図3に示すように、液体状の可燃性燃焼剤を気化させる気化部531と、該気化部531を加熱する加熱部532とを備える。気化部531は、例えば金属製の蒸発板であり、加熱部532の一端部に取り付けられている。加熱部532は、その内部に電熱線532aを備えており、該電熱線532aに通電することによって気化部531を加熱することができるように構成されている。かかる気化手段53は、気化経路54と対向するように、加熱部532の一端部が配管41に嵌め込まれて取付けられている。従って、気化部531は、配管41の内部に配備されると共に気化経路54に対向する配置となる。   As shown in FIG. 3, the vaporizing means 53 includes a vaporizing unit 531 that vaporizes a liquid combustible combustion agent, and a heating unit 532 that heats the vaporizing unit 531. The vaporization unit 531 is, for example, a metal evaporation plate, and is attached to one end of the heating unit 532. The heating unit 532 includes a heating wire 532a therein, and is configured to heat the vaporizing unit 531 by energizing the heating wire 532a. The vaporizing means 53 is attached by fitting one end of the heating unit 532 into the pipe 41 so as to face the vaporizing path 54. Therefore, the vaporization unit 531 is disposed inside the pipe 41 and is disposed to face the vaporization path 54.

このような構成の気化手段53を採用する場合には、可燃性燃焼剤が液滴の状態で配管41内に導入されるように、気化経路54や導入ポンプP2等を調整する。そうすると、気化経路54から配管41内に導入された可燃性燃焼剤の液滴は、気化部531の表面に落下し、気化部531の熱によって蒸発して気体となり、被処理ガスと混合する。尚、図3に示す矢印Xは、被処理ガスが流れる方向を示す。   When the vaporizing means 53 having such a configuration is employed, the vaporization path 54, the introduction pump P2, and the like are adjusted so that the combustible combustion agent is introduced into the pipe 41 in the form of droplets. If it does so, the droplet of the combustible combustion agent introduce | transduced in the piping 41 from the vaporization path | route 54 will fall on the surface of the vaporization part 531, will evaporate with the heat | fever of the vaporization part 531, and will become gas, and will mix with to-be-processed gas. Note that the arrow X shown in FIG. 3 indicates the direction in which the gas to be processed flows.

尚、気化手段53としては、例えば、前記気化経路54の周囲又は内部に配設される電熱線を採用することもできるし、熱媒体を流すための配管を採用することもできる。熱媒体としては、加熱された流体を使用することができ、例えば、前記加熱処理領域2において加熱された被処理ガスを好適に使用することができる。また、気化手段53に前記導入ポンプP2を内蔵したものとすることもできる。   As the vaporization means 53, for example, a heating wire disposed around or inside the vaporization path 54 may be employed, or a pipe for flowing a heat medium may be employed. As the heat medium, a heated fluid can be used. For example, a gas to be processed heated in the heat treatment region 2 can be preferably used. Further, the introduction pump P2 may be built in the vaporizing means 53.

本第二実施形態の蓄熱式脱臭装置1において、通常運転によって被処理ガスの脱臭を行うには、上述の第一工程、第二工程、及び第三工程にて行う。各工程において、被処理ガスは、前記混合手段5により供給側ダクト4内に気化させた可燃性燃焼剤が導入されることによって、可燃性燃焼剤と予め混合された状態で供給側ダクト4内を流れて供給状態の蓄熱領域3内に導入される。そして、混合された被処理ガスと可燃性燃焼剤とは、蓄熱領域3内の予め加熱された蓄熱材31から熱を受けることによって、通常750〜930℃にまで予熱されて該蓄熱領域3を通過して加熱処理領域2内へ供給される。そして、加熱処理領域2内にて可燃性燃焼剤が燃焼して、加熱処理領域2内の被処理ガスを所定の温度に昇温して酸化させて脱臭することができる。従って、従来のようにバーナーを用いなくても、加熱処理領域2内の被処理ガスを熱処理して脱臭することができ、コストを低くすることができる。   In the regenerative deodorization apparatus 1 of the second embodiment, in order to deodorize the gas to be treated by normal operation, the first step, the second step, and the third step are performed. In each process, the gas to be treated is introduced into the supply side duct 4 in a state of being preliminarily mixed with the combustible combustion agent by introducing the combustible combustion agent vaporized into the supply side duct 4 by the mixing means 5. And is introduced into the heat storage region 3 in the supply state. And the to-be-processed gas and the combustible combustion agent which were mixed are preheated to 750-930 degreeC normally by receiving heat from the preheated heat storage material 31 in the heat storage area | region 3, and this heat storage area | region 3 is made. It passes through and is supplied into the heat treatment region 2. Then, the combustible combustion agent burns in the heat treatment region 2, and the gas to be treated in the heat treatment region 2 is heated to a predetermined temperature and oxidized to deodorize it. Therefore, the gas to be treated in the heat treatment region 2 can be deodorized by heat treatment without using a burner as in the prior art, and the cost can be reduced.

しかも、従来のバーナーを用いた場合にあっては、局部的な加熱となって加熱処理領域2内の温度分布が偏る傾向があり、被処理ガスの脱臭が不十分となる虞があるが、被処理ガスと気化された可燃性燃焼剤とが予め混合された状態で加熱処理領域2内に供給される構成とすることで、前記温度分布が均一となり確実に脱臭することができる。   Moreover, in the case of using a conventional burner, there is a tendency that the temperature distribution in the heat treatment region 2 becomes biased due to local heating, and the deodorization of the gas to be treated may be insufficient. By adopting a configuration in which the gas to be treated and the vaporized combustible combustion agent are supplied into the heat treatment region 2 in a state of being mixed in advance, the temperature distribution becomes uniform and the deodorization can be reliably performed.

そして、脱臭処理された高温の被処理ガスは、排出状態の蓄熱領域3内を通過する際に、その内部の蓄熱材31によって吸熱され、通常20〜120℃にまで冷却されて大気中に排出される。尚、パージ状態の蓄熱領域3では、その内部の被処理ガスがパージ用返送ダクト8を経由して供給側ダクト4に返送され、その後は被処理ガスの流入流出が禁止されることとなる。   The deodorized high-temperature gas to be treated is absorbed by the heat storage material 31 inside when passing through the discharged heat storage region 3, and is usually cooled to 20 to 120 ° C and discharged into the atmosphere. Is done. In the heat storage region 3 in the purge state, the gas to be processed therein is returned to the supply side duct 4 via the purge return duct 8, and thereafter the inflow and outflow of the gas to be processed are prohibited.

図4は、本発明の第三実施形態の蓄熱式脱臭装置1において、被処理ガスの流れの一態様を示したフロー図である。尚、前記第一及び第二実施形態に係る蓄熱式脱臭装置1と同様の構成については、同じ符号を付こととしその説明を省略する。   FIG. 4 is a flow diagram showing an aspect of the flow of the gas to be processed in the heat storage deodorizer 1 according to the third embodiment of the present invention. In addition, about the structure similar to the thermal storage deodorizing apparatus 1 which concerns on said 1st and 2nd embodiment, the same code | symbol is attached | subjected and the description is abbreviate | omitted.

該蓄熱式脱臭装置1は、蓄熱材31が収容された複数の蓄熱領域3と、該複数の蓄熱領域3の少なくとも1つに被処理ガスを供給する供給側ダクト4と、前記複数の蓄熱領域3と連通され、供給側ダクト4から蓄熱領域3を介して供給される前記被処理ガスを熱処理する加熱処理領域2と、前記被処理ガスに可燃性燃焼剤を混合する混合手段5とを備えてなる。   The heat storage deodorizer 1 includes a plurality of heat storage regions 3 in which a heat storage material 31 is accommodated, a supply-side duct 4 that supplies a gas to be treated to at least one of the plurality of heat storage regions 3, and the plurality of heat storage regions. 3, a heat treatment region 2 that heat-treats the gas to be treated supplied from the supply side duct 4 through the heat storage region 3, and a mixing unit 5 that mixes a combustible combustion agent with the gas to be treated. It becomes.

前記混合手段5は、液体状の可燃性燃焼剤が前記加熱処理領域2内全体に拡散するように噴霧することによって、前記可燃性燃焼剤と前記被処理ガスとを混合することができるように構成されている。具体的には、本第三実施形態における混合手段5は、液体状の可燃性燃焼剤が貯留される燃焼剤タンク51と、前記加熱処理領域2を形成する筐体21に設けられる複数の噴霧ノズル55と、該複数の噴霧ノズル55のそれぞれに接続され前記燃焼剤タンク51と前記加熱処理領域2とを連通する噴霧経路56と、該噴霧経路56の途中に介装され加熱処理領域2内に可燃性燃焼剤を噴霧するための流れを形成する噴霧ポンプP1とを備えてなる。尚、混合手段5は、液体状の可燃性燃焼剤が前記加熱処理領域2内全体に拡散するように噴霧することによって、前記可燃性燃焼剤と前記被処理ガスとを混合しうるものであれば特に限定されるものではない。また、可燃性燃焼剤としては、例えば、重油やオイルなどの可燃性の液体を採用することができる。   The said mixing means 5 can mix the said combustible combustion agent and the said to-be-processed gas by spraying so that a liquid combustible combustion agent may diffuse in the said heat processing area | region 2 whole. It is configured. Specifically, the mixing means 5 in the third embodiment includes a plurality of sprays provided in a combustion agent tank 51 in which a liquid combustible combustion agent is stored and a casing 21 that forms the heat treatment region 2. A nozzle 55, a spray path 56 connected to each of the plurality of spray nozzles 55 and communicating the combustion agent tank 51 and the heat treatment region 2; And a spray pump P1 that forms a flow for spraying the combustible combustion agent. The mixing means 5 is capable of mixing the combustible combustion agent and the gas to be treated by spraying the liquid combustible combustion agent so as to diffuse throughout the heat treatment region 2. There is no particular limitation. Moreover, as a combustible combustion agent, combustible liquids, such as heavy oil and oil, are employable, for example.

前記噴霧ノズル55は、噴霧経路56を通って流れてきた液体状の可燃性燃焼剤を霧状に噴出することができるように構成されており、前記筐体21の少なくとも周方向(横方向)全周に亘って、所定間隔を空けて複数設けられている。本第三実施形態においては、噴霧ノズル55は、筐体21の側壁部212だけでなく天部211にも設けられており、天部211に設けられる噴霧ノズル55は、前記バーナーよりも側壁部212側に設けられている。   The spray nozzle 55 is configured to be able to eject the liquid combustible combustion agent flowing through the spray path 56 in the form of a mist, and at least the circumferential direction (lateral direction) of the casing 21. A plurality are provided at predetermined intervals along the entire circumference. In the third embodiment, the spray nozzle 55 is provided not only on the side wall portion 212 of the housing 21 but also on the top portion 211, and the spray nozzle 55 provided on the top portion 211 has a side wall portion rather than the burner. It is provided on the 212 side.

また、側壁部212に設けられている噴霧ノズル55は、周方向だけでなく上下方向にも複数配置されており、各噴霧ノズル55の噴出方向は、水平方向或いは水平方向に対し若干上向き又は下向きの方向となっている。   In addition, a plurality of spray nozzles 55 provided in the side wall portion 212 are arranged not only in the circumferential direction but also in the vertical direction, and the spray direction of each spray nozzle 55 is slightly upward or downward with respect to the horizontal direction or the horizontal direction. It has become the direction.

また、天部211に設けられている噴霧ノズル55は、前記筐体21の天部211、即ち、加熱処理領域2の外周側から中心側に向けて噴霧することができるように、その噴出方向が設定されている。つまり、天部211に設けられている噴霧ノズル55から噴霧される可燃性燃焼剤は、加熱処理領域2の外周側から中心側へ向けて内向きに噴出される。   Moreover, the spray nozzle 55 provided in the top part 211 has its spray direction so that it can spray toward the top part 211 of the said housing | casing 21, ie, the outer peripheral side of the heat processing area | region 2, toward a center side. Is set. That is, the combustible combustion agent sprayed from the spray nozzle 55 provided in the top portion 211 is ejected inward from the outer peripheral side to the center side of the heat treatment region 2.

このように、筐体21の少なくとも周方向(横方向)全周に亘って、所定間隔を空けて複数の噴霧ノズル55を設けることによって、加熱処理領域2の中心部へ向けて周囲から可燃性燃焼剤を噴霧することができ、加熱処理領域2内全体に可燃性燃焼剤を拡散することができる。   In this way, by providing a plurality of spray nozzles 55 at predetermined intervals over the entire circumference of at least the circumferential direction (lateral direction) of the casing 21, combustibility from the periphery toward the center of the heat treatment region 2. The combustion agent can be sprayed, and the combustible combustion agent can be diffused throughout the heat treatment region 2.

本第三実施形態の蓄熱式脱臭装置1において、通常運転によって被処理ガスの脱臭を行うには、上述の第一工程、第二工程、及び第三工程にて行う。各工程において、供給側ダクト4内を流れてきた被処理ガスは、蓄熱領域3内の予め加熱された蓄熱材31から熱を受けることによって、通常750〜930℃にまで予熱されて該蓄熱領域3を通過し、加熱処理領域2内へ供給される。そして、混合手段5によって液体状の可燃性燃焼剤が加熱処理領域2内全体に拡散するように噴霧されることによって、加熱処理領域2の全域に亘って被処理ガスと可燃性燃焼剤とが均一に混合された状態となる。そして、加熱処理領域2全域にて可燃性燃焼剤が燃焼し、加熱処理領域2の温度分布が均一となり、効率良く被処理ガスを所定の温度に昇温して酸化させて脱臭することができる。従って、従来のようにバーナー等の加熱手段6を用いなくても、加熱処理領域2内の被処理ガスを熱処理して脱臭することができ、コストを低くすることができる。   In the heat storage deodorization apparatus 1 of the third embodiment, in order to deodorize the gas to be treated by normal operation, the above-described first step, second step, and third step are performed. In each step, the gas to be treated that has flowed through the supply-side duct 4 is preheated to 750 to 930 ° C. by receiving heat from the preheated heat storage material 31 in the heat storage region 3 and is usually stored in the heat storage region. 3 is supplied into the heat treatment region 2. Then, the liquid combustible combustion agent is sprayed by the mixing means 5 so as to diffuse throughout the heat treatment region 2, whereby the gas to be treated and the combustible combustion agent are spread over the entire heat treatment region 2. A uniformly mixed state is obtained. And the combustible combustion agent burns in the entire heat treatment region 2, the temperature distribution in the heat treatment region 2 becomes uniform, and the gas to be treated can be efficiently heated to a predetermined temperature to be oxidized and deodorized. . Therefore, even if the heating means 6 such as a burner is not used as in the prior art, the gas to be processed in the heat treatment region 2 can be deodorized by heat treatment, and the cost can be reduced.

しかも、従来のバーナーを用いた場合にあっては、局部的な加熱となって加熱処理領域2内の温度分布が偏る傾向があり、被処理ガスの脱臭が不十分となる虞があるが、被処理ガスと気化された可燃性燃焼剤とが予め混合された状態で加熱処理領域2内に供給される構成とすることで、前記温度分布が均一となり確実に脱臭することができる。   Moreover, in the case of using a conventional burner, there is a tendency that the temperature distribution in the heat treatment region 2 becomes biased due to local heating, and the deodorization of the gas to be treated may be insufficient. By adopting a configuration in which the gas to be treated and the vaporized combustible combustion agent are supplied into the heat treatment region 2 in a state of being mixed in advance, the temperature distribution becomes uniform and the deodorization can be reliably performed.

そして、脱臭処理された高温の被処理ガスは、排出状態の蓄熱領域3内を通過する際に、その内部の蓄熱材31によって吸熱され、通常20〜120℃にまで冷却されて大気中に排出される。尚、パージ状態の蓄熱領域3では、その内部の被処理ガスがパージ用返送ダクト8を経由して供給側ダクト4に返送され、その後は被処理ガスの流入流出が禁止されることとなる。   The deodorized high-temperature gas to be treated is absorbed by the heat storage material 31 inside when passing through the discharged heat storage region 3, and is usually cooled to 20 to 120 ° C and discharged into the atmosphere. Is done. In the heat storage region 3 in the purge state, the gas to be processed therein is returned to the supply side duct 4 via the purge return duct 8, and thereafter the inflow and outflow of the gas to be processed are prohibited.

尚、本第一乃至第三実施形態の蓄熱式脱臭装置1は、上記の如く構成され、上記の如き効果を奏するものであるが、本発明の蓄熱式脱臭装置1は、上記構成に限定されず、本発明の意図する範囲内に於いて適宜設計変更可能である。   The regenerative deodorization apparatus 1 of the first to third embodiments is configured as described above and has the effects as described above. However, the regenerative deodorization apparatus 1 of the present invention is limited to the above configuration. However, the design can be appropriately changed within the range intended by the present invention.

例えば、前記第一乃至第三実施形態においては、三塔式蓄熱式脱臭装置を例に挙げて説明したが、本発明はこれに限定されるものではなく、二塔式や回転式などの他の形式の蓄熱式脱臭装置とすることも可能である。また、前記第一乃至第三実施形態において説明した構成のうち、一又は二以上の構成を組合せて採用してもよい。   For example, in the first to third embodiments, the three-column heat storage deodorizing apparatus has been described as an example. However, the present invention is not limited to this, and other methods such as a two-column type and a rotary type are also used. It is also possible to use a heat storage deodorizing device of the type Moreover, you may employ | adopt combining 1 or 2 or more structures among the structures demonstrated in said 1st thru | or 3rd embodiment.

また、本第一乃至第三実施形態の蓄熱式脱臭装置1に於いては、パージ用返送ダクトが備えられ、被処理ガスが上流側に返送されるように構成されたが、パージ用返送ダクトが備えられず、供給状態から排出状態に切り替える際に、供給側ダクトを介して例えば外気等を導入することにより、蓄熱領域内の被処理ガスを加熱処理領域内に押し出して熱処理するように構成されていてもよい。かかる蓄熱式脱臭装置1においては、別途パージ用返送ダクトが設けられなくとも、未処理の被処理ガスが大気中に排出される虞が低減されることとなるため、装置の構成が簡略されたものとなる。   Moreover, in the heat storage deodorizing apparatus 1 of the first to third embodiments, the purge return duct is provided and the gas to be treated is returned to the upstream side. When switching from the supply state to the discharge state, for example, by introducing outside air or the like through the supply side duct, the gas to be processed in the heat storage region is pushed into the heat treatment region and heat treated. May be. In such a heat storage type deodorizing apparatus 1, the possibility of untreated gas being discharged into the atmosphere is reduced even if a separate return duct for purging is not provided, so that the configuration of the apparatus is simplified. It will be a thing.

本発明に係る蓄熱式脱臭装置の第一実施形態を示したフロー図。The flowchart which showed 1st embodiment of the thermal storage type deodorizing apparatus which concerns on this invention. 本発明に係る蓄熱式脱臭装置の第二実施形態を示したフロー図。The flowchart which showed 2nd embodiment of the thermal storage type deodorizing apparatus which concerns on this invention. 第二実施形態にかかる気化手段を示す概略図。Schematic which shows the vaporization means concerning 2nd embodiment. 本発明に係る蓄熱式脱臭装置の第三実施形態を示したフロー図。The flowchart which showed 3rd embodiment of the thermal storage type deodorizing apparatus which concerns on this invention.

符号の説明Explanation of symbols

1…蓄熱式脱臭装置、2…加熱処理領域、3…蓄熱領域、4…供給側ダクト、5…混合手段、6…加熱手段、7…排出側ダクト、8…パージ用返送ダクト、21…筐体、31…蓄熱材、41,71,81…配管、42,72,82…開閉バルブ、51…燃焼剤タンク、52,56…噴霧経路、53…気化手段、54…気化経路、55…噴霧ノズル、61…ガス経路、211…天部、212…側壁部、531…気化部、532…加熱部、F…供給ファン、P1…噴霧ポンプ、P2…導入ポンプ   DESCRIPTION OF SYMBOLS 1 ... Thermal storage deodorizing device, 2 ... Heat processing area, 3 ... Heat storage area, 4 ... Supply side duct, 5 ... Mixing means, 6 ... Heating means, 7 ... Discharge side duct, 8 ... Returning duct for purge, 21 ... Housing Body, 31 ... heat storage material, 41, 71, 81 ... piping, 42, 72, 82 ... open / close valve, 51 ... combustion agent tank, 52, 56 ... spray path, 53 ... vaporization means, 54 ... vaporization path, 55 ... spray Nozzle, 61 ... gas path, 211 ... top part, 212 ... side wall part, 531 ... vaporization part, 532 ... heating part, F ... supply fan, P1 ... spray pump, P2 ... introduction pump

Claims (4)

蓄熱材が収容された複数の蓄熱領域と、該複数の蓄熱領域の少なくとも1つを介して供給される被処理ガスを熱処理する加熱処理領域とを備える蓄熱式脱臭装置であって、前記被処理ガスに可燃性燃焼剤を混合する混合手段を備えることを特徴とする蓄熱式脱臭装置。   A heat storage deodorizing apparatus comprising: a plurality of heat storage regions in which a heat storage material is housed; and a heat treatment region for heat-treating a gas to be treated supplied through at least one of the plurality of heat storage regions. A regenerative deodorizing apparatus comprising a mixing means for mixing a combustible combustion agent with gas. 蓄熱材が収容された複数の蓄熱領域と、該複数の蓄熱領域の少なくとも1つに被処理ガスを供給する供給側ダクトと、前記複数の蓄熱領域と連通され前記被処理ガスを熱処理する加熱処理領域とを備える蓄熱式脱臭装置であって、前記供給側ダクト内に液体状の可燃性燃焼剤を噴霧して前記被処理ガスに混合する混合手段を備えることを特徴とする蓄熱式脱臭装置。   A plurality of heat storage regions in which a heat storage material is accommodated, a supply-side duct that supplies a gas to be processed to at least one of the plurality of heat storage regions, and a heat treatment that communicates with the plurality of heat storage regions and heat-treats the gas to be processed A regenerative deodorization apparatus comprising: a heat storage deodorization apparatus including a mixing unit that sprays a liquid combustible combustion agent into the supply duct and mixes it with the gas to be treated. 蓄熱材が収容された複数の蓄熱領域と、該複数の蓄熱領域の少なくとも1つに被処理ガスを供給する供給側ダクトと、前記複数の蓄熱領域と連通され前記被処理ガスを熱処理する加熱処理領域とを備える蓄熱式脱臭装置であって、前記供給側ダクト内に気化させた可燃性燃焼剤を導入して前記被処理ガスに混合する混合手段を備えることを特徴とする蓄熱式脱臭装置。   A plurality of heat storage regions in which a heat storage material is accommodated, a supply-side duct that supplies a gas to be processed to at least one of the plurality of heat storage regions, and a heat treatment that communicates with the plurality of heat storage regions and heat-treats the gas to be processed A regenerative deodorization apparatus comprising: a heat storage deodorization apparatus including a mixing unit that introduces a combustible combustible vaporized into the supply-side duct and mixes it with the gas to be treated. 蓄熱材が収容された複数の蓄熱領域と、該複数の蓄熱領域の少なくとも1つを介して供給される被処理ガスを熱処理する加熱処理領域とを備える蓄熱式脱臭装置であって、液体状の可燃性燃焼剤が前記加熱処理領域内全体に拡散するように該可燃性燃焼剤を噴霧することによって、前記可燃性燃焼剤と前記被処理ガスとを混合する混合手段を備えることを特徴とする蓄熱式脱臭装置。   A heat storage deodorizing apparatus comprising a plurality of heat storage regions in which a heat storage material is accommodated and a heat treatment region for heat-treating a gas to be treated supplied via at least one of the plurality of heat storage regions, It comprises mixing means for mixing the combustible combustible and the gas to be treated by spraying the combustible combustible so that the combustible combustible is diffused throughout the heat treatment region. Thermal storage deodorizer.
JP2007019123A 2007-01-30 2007-01-30 Heat storage type deodorizer Pending JP2008185267A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2007019123A JP2008185267A (en) 2007-01-30 2007-01-30 Heat storage type deodorizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2007019123A JP2008185267A (en) 2007-01-30 2007-01-30 Heat storage type deodorizer

Publications (1)

Publication Number Publication Date
JP2008185267A true JP2008185267A (en) 2008-08-14

Family

ID=39728435

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2007019123A Pending JP2008185267A (en) 2007-01-30 2007-01-30 Heat storage type deodorizer

Country Status (1)

Country Link
JP (1) JP2008185267A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011102664A (en) * 2009-11-10 2011-05-26 Chugai Ro Co Ltd Heat storage type combustion deodorizer
CN103301725A (en) * 2012-03-16 2013-09-18 达斯环境专家有限责任公司 Method and apparatus for treating harmful gases

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001355822A (en) * 2000-06-13 2001-12-26 Ishikawajima Harima Heavy Ind Co Ltd Heat storage combustion type gas treating furnace
JP2002089821A (en) * 2000-09-20 2002-03-27 Tokyo Gas Co Ltd Heat storage gas processing apparatus and its operation method
JP2005144235A (en) * 2003-11-11 2005-06-09 Japan Steel Works Ltd:The Premixing type catalytically deodorization method and apparatus

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001355822A (en) * 2000-06-13 2001-12-26 Ishikawajima Harima Heavy Ind Co Ltd Heat storage combustion type gas treating furnace
JP2002089821A (en) * 2000-09-20 2002-03-27 Tokyo Gas Co Ltd Heat storage gas processing apparatus and its operation method
JP2005144235A (en) * 2003-11-11 2005-06-09 Japan Steel Works Ltd:The Premixing type catalytically deodorization method and apparatus

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011102664A (en) * 2009-11-10 2011-05-26 Chugai Ro Co Ltd Heat storage type combustion deodorizer
CN103301725A (en) * 2012-03-16 2013-09-18 达斯环境专家有限责任公司 Method and apparatus for treating harmful gases
DE102012102251A1 (en) * 2012-03-16 2013-09-19 Das Environmental Expert Gmbh Method for treating noxious gases discharged during semiconductor material production, involves partially converting noxious gas to process gas by using reactant, so that heat energy of gases is used partially for reactant evaporation
DE102012102251B4 (en) * 2012-03-16 2013-11-07 Das Environmental Expert Gmbh Process and device for the treatment of noxious gases

Similar Documents

Publication Publication Date Title
KR102238253B1 (en) High Efficiency Energy Saving NOx and VOC Removal System
JP4704432B2 (en) Toxic gas cleaning equipment from production process
ES2260452T3 (en) METHOD AND DEVICE FOR LITTLE NON-CATALYTIC CONTAMINANT COMBUSTION OF A LIQUID FUEL.
TWI492782B (en) Method of treating an exhaust gas stream
JP5492482B2 (en) Direct combustion deodorization furnace
JPH01200115A (en) Combustion apparatus having auxiliary combustion apparatus for liquid
TWI542830B (en) Burning device
JP2008185267A (en) Heat storage type deodorizer
US7270539B1 (en) Method and apparatus for destruction of vapors and waste streams using flash oxidation
KR100788909B1 (en) Voc incineration apparatus designed by module type with large turn down ratio and without backfire occurrence
KR101645171B1 (en) NON-DEGRADABLE HAZARDOUS GAS PURIFICATION SYSTEM GENERATED IN THE SEMICONDUCTOR AND VOCs EMISSION PROCESS
KR102634533B1 (en) VOCs REMOVAL SYSTEM
US20040197251A1 (en) Vaporization having fast start up
US8145044B1 (en) Air ammonia heater and vaporization chamber system
US20020044886A1 (en) Vaporization system having blower positioned in reduced temperature zone
JPH1172221A (en) Incinerator
EP0906545B1 (en) Surface-combustion liquid-fuel burner and method of combustion
JP2007263420A (en) Heat storage type combustion deodorizing device and combustion deodorizing method
WO1997049952A9 (en) Surface-combustion liquid-fuel burner and method of operating it
JP2008045818A (en) Heat storage type burning deodorizing apparatus
KR100879800B1 (en) Hybrid gas scrubber
JP6411314B2 (en) Combustion treatment apparatus and combustion treatment method for liquid VOC
JP2003139316A (en) Heat storage type volatile organic compound treatment device and treatment method
JP2014124624A (en) Method for treating low concentration pcb and contaminated soil
JPS587330B2 (en) Exhaust gas deodorization method and deodorization device

Legal Events

Date Code Title Description
RD04 Notification of resignation of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7424

Effective date: 20080626

A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20090826

A977 Report on retrieval

Effective date: 20111222

Free format text: JAPANESE INTERMEDIATE CODE: A971007

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20120106

A02 Decision of refusal

Effective date: 20120511

Free format text: JAPANESE INTERMEDIATE CODE: A02