JPS61101233A - Combustion treatment apparatus - Google Patents

Combustion treatment apparatus

Info

Publication number
JPS61101233A
JPS61101233A JP59220595A JP22059584A JPS61101233A JP S61101233 A JPS61101233 A JP S61101233A JP 59220595 A JP59220595 A JP 59220595A JP 22059584 A JP22059584 A JP 22059584A JP S61101233 A JPS61101233 A JP S61101233A
Authority
JP
Japan
Prior art keywords
exhaust gas
combustion
gas
furnace
solvent
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
JP59220595A
Other languages
Japanese (ja)
Inventor
Yasumasa Ishibashi
石橋 康正
Hayami Nagano
早実 長野
Shozo Naruse
成瀬 尚蔵
Shinichi Takimoto
滝本 新一
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 Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP59220595A priority Critical patent/JPS61101233A/en
Publication of JPS61101233A publication Critical patent/JPS61101233A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To treat exhaust gas containing an org. solvent at low cost by uniformizing a gas stream, by well mixing the heated exhaust gas containing the org. solvent with combustion gas in a combustion furnace and providing a buffle containing a Cr-compound so as to insert the same in said furnace. CONSTITUTION:The greater part of solvent-containing exhaust gas is heated while passed through a heat exchanger 5 by a blower 4 to be sent to a combustion furnace 6 and contacted and mixed with high temp. combustion gas to be introduced into a reaction furnace 7 where the solvent component is oxidized and removed under a stay time and temp. condition required for the oxidation of the solvent component in the exhaust gas. A buffle 8 comprising Cr- compound-containing refractory, which is provided with openings for uniformizing a gas flow speed, is inserted in the furnace to allow reaction to easily advance. The gas after reaction is exhausted out of the system from an exhaust port 9 while sensible heat thereof is recovered by a heat exchanger 5.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明に、有機溶剤含有排ガスの燃焼処理装置に関する
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a combustion treatment apparatus for exhaust gas containing an organic solvent.

〔従来の技術〕[Conventional technology]

トルエンなどの有機浴剤を含む排ガスは、大気汚染の見
地から、規制(WL以下に迅埋して排出することが義務
づけられている。その処理方法としてば、一般に、活性
炭などに吸着して回収する方法がとられているが、排ガ
ス中のa度が低く、回収のメリットの少ない場合は、有
機浴剤を燃焼酸化して処理する燃焼が採用されている。
From the perspective of air pollution, exhaust gas containing organic bath agents such as toluene is required to be quickly buried and discharged below the WL level. Generally, the treatment method is to collect it by adsorbing it on activated carbon, etc. However, in cases where the exhaust gas has a low degree of a and there is little merit in recovering it, combustion, in which the organic bath agent is oxidized by combustion, is adopted.

燃焼法は、重油、灯油ま九にLPG t−燃焼して生成
する高温のガスと溶剤を含有する排ガスとを混合させて
、浴剤取分全酸化分解させる方法である。この場合、反
応温度が低いと、溶剤成分の酸化に不十分で、規制値金
クリヤーできない。しかしながら、反応温度を高くする
と、燃料の消費量が多くなり好ましくない。低い反応温
度で酸化をすすめる方法の一つに、触媒全使用する方法
があるが、この方法では、触媒の被毒と価格に問題が8
9、必ずしも経済的でない。
The combustion method is a method in which high-temperature gas produced by t-burning LPG in heavy oil or kerosene is mixed with exhaust gas containing a solvent, and a portion of the bath agent is completely oxidized and decomposed. In this case, if the reaction temperature is low, the oxidation of the solvent component will be insufficient and the regulation gold cannot be cleared. However, increasing the reaction temperature increases fuel consumption, which is undesirable. One method of promoting oxidation at a low reaction temperature is to use the entire catalyst, but this method has problems with catalyst poisoning and cost.
9. Not necessarily economical.

すなわち、燃焼法に、浴剤成分を最低着火温度以上で燃
焼分解させるため、高温度を必要とする。溶剤成分一度
が希薄な場合には、高温度を維持するのに、多くの助燃
料を必要する。助燃料消費量全最小限にする几めに、浴
剤成分を含む排ガスの予熱上い力)に効率工くするか、
燃焼ガスと浴剤成分の混合音いかに工くするかなどの検
討が必要である。とくに、省エネルギーの点から、触媒
を用いて低温度で燃焼させることも広く実用化されてい
るが、この方法は、触媒の被虐・性能低下の点から浴剤
のは類が限られ、かつ排ガス中の重金属ダスト、ミスト
lど全十分に除去しておかなければならない。
That is, the combustion method requires high temperatures in order to burn and decompose the bath agent components above the minimum ignition temperature. When the solvent components are dilute, more co-fuel is required to maintain high temperatures. In order to minimize the amount of auxiliary fuel consumed, the efficiency of preheating the exhaust gas containing bath agent components should be improved.
It is necessary to consider how to improve the mixing sound of combustion gas and bath agent components. In particular, from the point of view of energy conservation, combustion at low temperatures using catalysts has been widely put into practical use, but this method is limited in the types of bath additives that can be used due to the damage and performance deterioration of the catalyst, and the exhaust gas All heavy metal dust and mist inside must be thoroughly removed.

〔発明が解決しょうとする問題点〕[Problem that the invention seeks to solve]

本発明者等は、上記従来の方法の問題?解決する九め、
特に燃焼法による処理装置に注目し、性能の工い低コス
トの燃焼炉を開発し、本発明に到達した。
The present inventors solved the problem with the above conventional method? Nine points to solve,
In particular, we focused on processing equipment using the combustion method, developed a combustion furnace with improved performance and low cost, and arrived at the present invention.

〔問題点を解決するための手段〕[Means for solving problems]

本発明は、有機浴剤を含有する排ガスを昇温させる熱交
換器と、昇温された排ガスを高温の燃焼ガスと接触、混
合させる燃焼炉と、排ガス中の有機溶剤成分全酸化除去
する反応炉エリなる燃焼処理装置において、クロム比合
物全含有し、かつ反応炉内のガス流速が均一になる開口
部を設けたパンフル材tIi厄炉内に設けたことt特徴
とするf、屍処理装置短関する。
The present invention relates to a heat exchanger that raises the temperature of exhaust gas containing an organic bath agent, a combustion furnace that brings the heated exhaust gas into contact with high-temperature combustion gas and mixes it, and a reaction system that completely oxidizes and removes organic solvent components in the exhaust gas. In the combustion treatment equipment called Furnace Eri, a panfur material containing all the chromium compound and provided with an opening to make the gas flow rate uniform in the reactor. Regarding the equipment.

すなわち、本発明でに、燃焼ガスと号剤底分を含む排ガ
スとを炉内で工く混合させるとともに、エフ低い温度で
溶剤取分の酸fヒ分′S全達成できる工うな燃焼炉内挿
入バッフル全役V′ffcことtr#徴とする。
That is, in the present invention, the combustion gas and the exhaust gas containing the bottom part of the No. 1 solvent are mixed in the furnace, and at the same time, the entire acid fraction of the solvent can be achieved at a low temperature. It is assumed that the insertion baffle has a full role V'ffc, also known as tr#.

〔作 用〕[For production]

以下に、本発明装置で図面に基づき説明する。 The apparatus of the present invention will be explained below based on the drawings.

g1図に、本発明てよる燃焼処理装置の・既格図である
。燃料は、燃料タンク1から燃料ポンプ2を通して、バ
ーナ3で燃焼される。一方、浴剤を含む排ガス(以下、
排ガスと略す)ば、ブロワ−4に工9、大部分が熱交換
器(又aボイラlど)5全通して昇温されて、燃焼炉6
に送られる。なお、一部の排ガスは、−次空気としても
使用される。昇温された排ガスに、禮焼炉6で高温の燃
焼ガスと接触、混合され、反応炉7に導びかれる。こ\
で、排ガス中の浴剤成分の酸化に必要な滞留時間と温度
条件のもとで、浴剤成分を規制値以下に酸化除去する。
Fig. g1 is a typical diagram of the combustion processing apparatus according to the present invention. Fuel passes from a fuel tank 1 through a fuel pump 2 and is burned in a burner 3. On the other hand, exhaust gas containing bath additives (hereinafter referred to as
The exhaust gas (abbreviated as "exhaust gas") is passed through the blower 4 (9), the majority of which passes through the heat exchanger (also boiler (1), etc.) 5 and is heated up, and is then heated to the combustion furnace 6.
sent to. Note that some exhaust gas is also used as secondary air. The heated exhaust gas is brought into contact with and mixed with high-temperature combustion gas in a burnishing furnace 6, and is led to a reaction furnace 7. child\
Under the residence time and temperature conditions required for oxidizing the bath agent components in the exhaust gas, the bath agent components are oxidized and removed to below the regulation value.

反応後のガスは、顕熱全熱交換器(又はボイラ)5で回
収された後、排出口9から系外に放出される。
The gas after the reaction is recovered by the sensible total heat exchanger (or boiler) 5 and then discharged from the system through the outlet 9.

本発明装置では、反応全斉易にすすめるためのクロム化
合物の耐火物よりりなるバッフル8が1〜2ヶ反応炉内
7に挿入されている。バッフル断面の一例を第2図に示
す。実際のバッフルの開口部は、処理ガスとの接触面積
ならびに整流作用全考慮して決定される。
In the apparatus of the present invention, one or two baffles 8 made of a chromium compound refractory are inserted into the reactor 7 in order to facilitate the simultaneous reaction. An example of a baffle cross section is shown in FIG. The actual opening of the baffle is determined by taking into account the contact area with the processing gas and the rectification effect.

〔発明の効果〕〔Effect of the invention〕

(1)燃料の燃焼ガスと接触した排ガス(被処理ガス)
ハ、温度分布が不均一である之め、従来の方式でに高効
率の酸化が期待できなかった。ところが、本発明によっ
て適当な開口を有するクロム耐火物のバッフル全通過さ
せることに工っで、燃焼ガスと排ガスを混合させ、均一
な温度分布として、酸化の促進金計ることができる。
(1) Exhaust gas that has come into contact with fuel combustion gas (gas to be treated)
C. Highly efficient oxidation could not be expected with conventional methods because the temperature distribution was non-uniform. However, according to the present invention, by passing the entire chrome refractory baffle with appropriate openings, the combustion gas and the exhaust gas can be mixed and have a uniform temperature distribution, thereby promoting oxidation.

(2)  適当な開口を有したクロム耐火物全通過する
過程で、同耐火物のクロム酸化物の表面と接触し、その
触媒作用で、有機浴剤の酸化全促進することができる。
(2) In the process of passing through a chromium refractory having an appropriate opening, it comes into contact with the chromium oxide surface of the refractory, and its catalytic action can promote the total oxidation of the organic bath agent.

以下に、本発明装置におけるクロム耐火物エフなるバッ
フルの設置効果を実施例にて示す。
Below, the effect of installing a baffle made of chrome refractory F in the apparatus of the present invention will be shown in Examples.

なお、下記実施例では、溶剤成分として、比較的処理の
難かしいトルエンを用いた。
In the following examples, toluene, which is relatively difficult to process, was used as a solvent component.

比較例1 (バッフルのない場合ン 適当な反応温度と滞留時間のとき、トルエンの酸化率は
60%であつ几。
Comparative Example 1 (Without baffle) At appropriate reaction temperature and residence time, the oxidation rate of toluene was 60%.

比較例2 (硅石耐人物で製作したバッフルを1ケ炉内に挿入し几
場合) 上記比較例1と同一の反応時間、滞留時間のとき、トル
エンの酸化率は68%であった。
Comparative Example 2 (When one baffle made of quartz stone was inserted into the furnace) When the reaction time and residence time were the same as in Comparative Example 1, the oxidation rate of toluene was 68%.

実施例1 (クロム耐火物で製作したバッフルを1ケ炉内に挿入し
f?−場合) 比較例1と同一の反応時間、滞留時間のとき、トルエン
の酸化率は80%であった。
Example 1 (When one baffle made of chromium refractory was inserted into the furnace) When the reaction time and residence time were the same as in Comparative Example 1, the oxidation rate of toluene was 80%.

実施例2 (クロム耐火物で製作し几バッフル′t−2ケF内に挿
入し友場合) 比較例1と同一の反応時間、滞留時間のとき、100%
で6つ九〇 実施例5 (実施例1工9i1!化クロム含有率の高いクロム耐火
物で製作したバッフルを1ケ炉内に挿入した場合ン 実施例1と同じ条件でのトルエンの駿化除去率は、90
%で6つ次。
Example 2 (Made of chrome refractory and inserted into a baffle't-2F) When the reaction time and residence time are the same as in Comparative Example 1, 100%
Example 5 (Example 1) 9i1! When one baffle made of a chromium refractory with a high chromium chloride content is inserted into the furnace.Toluene conversion under the same conditions as Example 1 The removal rate is 90
6th in %.

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

第1図は、本発明の燃焼処理装置の概略図である。第2
図は、本発明装置に係るバッフルの断面の1例を示す。 復代理人  内 1)  明 復代理人  萩 原 亮 − 第2図 丁・続補正占 昭和60年 2月7日
FIG. 1 is a schematic diagram of the combustion processing apparatus of the present invention. Second
The figure shows an example of a cross section of a baffle according to the device of the present invention. Sub-agent 1) Meifu agent Ryo Hagiwara - 2nd drawing, continuation amendment February 7, 1985

Claims (1)

【特許請求の範囲】[Claims] 有機溶剤を含有する排ガスを昇温させる熱交換器と、昇
温された排ガスを高温の燃焼ガスと接触、混合させる燃
焼炉と、排ガス中の有機溶剤成分を酸化除去する反応炉
よりりなる燃焼処理装置において、クロム化合物を含有
し、かつ反応炉内のガス流速が均一になる開口部を設け
たバッフル材を反応炉内に設けたことを特徴とする燃焼
処理装置。
Combustion consisting of a heat exchanger that raises the temperature of exhaust gas containing organic solvents, a combustion furnace that contacts and mixes the heated exhaust gas with high-temperature combustion gas, and a reactor that oxidizes and removes organic solvent components in the exhaust gas. A combustion processing apparatus characterized in that a baffle material containing a chromium compound and provided with an opening for uniforming the gas flow rate in the reactor is provided in the reactor.
JP59220595A 1984-10-22 1984-10-22 Combustion treatment apparatus Pending JPS61101233A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59220595A JPS61101233A (en) 1984-10-22 1984-10-22 Combustion treatment apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59220595A JPS61101233A (en) 1984-10-22 1984-10-22 Combustion treatment apparatus

Publications (1)

Publication Number Publication Date
JPS61101233A true JPS61101233A (en) 1986-05-20

Family

ID=16753436

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59220595A Pending JPS61101233A (en) 1984-10-22 1984-10-22 Combustion treatment apparatus

Country Status (1)

Country Link
JP (1) JPS61101233A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010032593A1 (en) * 2008-09-17 2010-03-25 三菱重工業株式会社 Reheat boiler
CN102588941A (en) * 2012-02-23 2012-07-18 无锡华光锅炉股份有限公司 Baffle device for organizing smoke flowing in horizontal exhaust-heat boiler

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010032593A1 (en) * 2008-09-17 2010-03-25 三菱重工業株式会社 Reheat boiler
JP2010071513A (en) * 2008-09-17 2010-04-02 Mitsubishi Heavy Ind Ltd Reheat boiler
KR101280130B1 (en) * 2008-09-17 2013-06-28 미츠비시 쥬고교 가부시키가이샤 Reheat boiler
CN102588941A (en) * 2012-02-23 2012-07-18 无锡华光锅炉股份有限公司 Baffle device for organizing smoke flowing in horizontal exhaust-heat boiler

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