JPH06262037A - Method for denitrification of exhaust gas from glass kiln - Google Patents

Method for denitrification of exhaust gas from glass kiln

Info

Publication number
JPH06262037A
JPH06262037A JP5076216A JP7621693A JPH06262037A JP H06262037 A JPH06262037 A JP H06262037A JP 5076216 A JP5076216 A JP 5076216A JP 7621693 A JP7621693 A JP 7621693A JP H06262037 A JPH06262037 A JP H06262037A
Authority
JP
Japan
Prior art keywords
exhaust gas
demister
gas
water
wet
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
JP5076216A
Other languages
Japanese (ja)
Inventor
Yukio Ogura
幸生 小倉
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.)
AGC Inc
Original Assignee
Asahi Glass 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 Asahi Glass Co Ltd filed Critical Asahi Glass Co Ltd
Priority to JP5076216A priority Critical patent/JPH06262037A/en
Publication of JPH06262037A publication Critical patent/JPH06262037A/en
Pending legal-status Critical Current

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  • Treating Waste Gases (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)

Abstract

PURPOSE:To prevent clogging and deterioration of a denitrification catalyst in a nitrogen oxide removing process from occurring and to perform denitrification of exhaust gas for a long time by holding a demister under a wet condition when SOx in the exhaust gas from a glass kiln is desulfurizated under wet condition and the treated gas is passed through the demister and then, reduction of NOx with ammonia is performed. CONSTITUTION:Exhaust gas from a glass kiln for producing sheet glasses etc., is at first introduced in a wet desulfurization apparatus and SOx in the exhaust gas is removed by transferring the exhaust gas from the lower part to the upper part while caustic soda water soln. is sprayed. Then, the exhaust gas is introduced into a demister and is brought into contact with water from a water spraying pipe to make the demister under a wet condition in such a way that waterdrops are dropped down with condensed water of steam in the exhaust gas and dust is removed thereby. Then, the exhaust gas from the demister is heated at about 350 deg.C and it is passed through a honeycomb catalyst after ammonia is incorporated to reduce nitrogen oxide to nitrogen gas.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、ガラス窯の排ガスの脱
硝方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for denitrifying exhaust gas from a glass kiln.

【0002】[0002]

【従来の技術】ガラス窯の燃焼排ガス中のSOx を先ず
湿式脱硫し、次いで湿式脱硫したガスをデミスターを通
過させ、ガス中のダストを除去し、次いでこのガスを脱
硝装置に送り、NH3 を吹込み触媒の存在下でガス中の
NOx をN2 に還元する方法が知られている。
Is first wet desulfurization the SO x in the combustion exhaust gas of the Prior Art Glass furnace, then wet desulphurized gas passed through the demister and to remove dust in the gas and then feeding the gas to the denitration apparatus, NH 3 A method is known in which NO x in gas is reduced to N 2 in the presence of a catalyst for blowing NO.

【0003】[0003]

【発明が解決しようとする課題】しかし、この方法で
は、デミスターにより除去できないダストが脱硝装置に
入り、脱硝触媒の表面に付着しNOx の除去効率が低下
したり、脱硝触媒の通気孔を閉塞するという課題があっ
た。本発明は従来技術の前記課題を解消し、ダストが脱
硝触媒の表面に付着しNOx の除去効率が低下したり、
脱硝触媒の通気孔を閉塞することのないガラス窯の排ガ
スの脱硝方法の提供を目的とする。
However, in this method, dust that cannot be removed by the demister enters the denitration device and adheres to the surface of the denitration catalyst to reduce the NO x removal efficiency, or the vent holes of the denitration catalyst are blocked. There was a problem to do. The present invention solves the above problems of the prior art, and dust adheres to the surface of the denitration catalyst to reduce the NO x removal efficiency,
An object of the present invention is to provide a method for denitrifying exhaust gas from a glass kiln without blocking the vent holes of the denitration catalyst.

【0004】[0004]

【課題を解決するための手段】本発明は、ガラス窯の排
ガス中のSOx を湿式脱硫し、次いで湿式脱硫したガス
をデミスターを通過させ、ガス中のダストを除去し、次
いでNH3 によりガス中のNOx を還元除去するにあた
り、デミスターを湿潤状態に保持することを特徴とする
排ガスの脱硝方法である。
According to the present invention, SO x in the exhaust gas of a glass kiln is wet desulfurized, the wet desulfurized gas is then passed through a demister to remove dust in the gas, and then the gas is removed with NH 3. This is a method for denitration of exhaust gas, which is characterized in that a demister is kept in a wet state in reducing and removing NO x therein.

【0005】本発明においては、ガラス窯の排ガスは先
ず湿式脱硫により排ガス中のSOxが除去される。この
湿式脱硫方法としては排ガスと苛性ソーダ、炭酸ソーダ
等の水溶液とを接触し排ガス中のSOx を水溶液に吸収
し、芒硝として回収するタイプのもの等広範囲に使用で
きる。
[0005] In the present invention, the exhaust gas of the glass furnace is first SO x in the exhaust gas by a wet desulfurization is removed. This wet desulfurization method can be used in a wide range such as a type in which exhaust gas is contacted with an aqueous solution of caustic soda, sodium carbonate or the like to absorb SO x in the exhaust gas into the aqueous solution, and is recovered as Glauber's salt.

【0006】この湿式脱硫の工程において、SOx の他
にダストも除去される。通常、この工程において、排ガ
スは60〜70℃程度に冷却される。この湿式脱硫の工
程を通過した排ガスには、微量のSOx ダスト(アルカ
リ金属とイオウの化合物を主体とするもの)が含有され
る。
In this wet desulfurization process, dust is removed in addition to SO x . Usually, in this process, the exhaust gas is cooled to about 60 to 70 ° C. Exhaust gas that has passed through this wet desulfurization process contains a small amount of SO x dust (containing mainly alkali metal and sulfur compounds).

【0007】次いで、この微量のSOx ダストを含有す
るガスは、デミスターを通過し、微量のSOx ダストが
除去される。このデミスターは、排ガスに含まれる水蒸
気の凝縮した水、外部から別途供給される水等により常
に湿潤状態に保持されている。この湿潤状態は、水滴が
デミスターより滴下する程度で充分である。
[0007] Then, gas containing SO x dust of the small amount passes through the demister, traces of the SO x dust is removed. This demister is always kept in a wet state by water condensed with water vapor contained in the exhaust gas, water supplied separately from the outside or the like. It is sufficient that the wet state is such that water drops are dropped from the demister.

【0008】また、このデミスターの貫通孔は0.5〜
20μmΦの円に相当する面積を有するものが好まし
い。貫通孔が上記範囲の下限より小さい場合は、排ガス
の抵抗が大きくなりすぎ好ましくなく、上限より大きい
場合はSOx ダストの除去率が低下するので好ましくな
い。デミスターの構造としては、ワイヤーメッシュタイ
プのもの等広範囲のものが採用される。
Further, the through hole of this demister is 0.5 to
Those having an area corresponding to a circle of 20 μmΦ are preferable. If the through-holes are smaller than the lower limit of the above range, the resistance of exhaust gas becomes too large, which is not preferable, and if the through-holes are larger than the upper limit, the removal rate of SO x dust decreases, which is not preferable. As the structure of the demister, a wide range of structures such as a wire mesh type are adopted.

【0009】排ガスは、このデミスターを通過する際、
デミスターに付着している水にダスト、SOx が吸着し
又は溶解して排ガスから除去される。さらにミストは、
デミスターの貫通孔で捕捉され、排ガスから除去され
る。
When the exhaust gas passes through this demister,
Dust and SO x are adsorbed or dissolved in the water adhering to the demister and removed from the exhaust gas. Furthermore, the mist is
It is captured in the through holes of the demister and removed from the exhaust gas.

【0010】ダスト、SOx 、ミストを含有する水は水
滴となり、デミスターから滴下し、排ガスの流路から外
部に排出され、所定の処理が行われる。
Water containing dust, SO x , and mist becomes water droplets, which are dropped from the demister and discharged from the exhaust gas flow path to the outside to undergo a predetermined treatment.

【0011】次いで、デミスターを通過した排ガスは3
00〜400℃の温度に加熱され、アンモニアが添加さ
れる。次いで、このアンモニアを含有する排ガスは、ハ
ニカム状触媒を通過し、排ガス中の窒素酸化物が窒素ガ
スに還元される。この触媒としてはTiO2 −V25
−WO3 系のもの等広範囲のものが使用される。
Next, the exhaust gas passing through the demister is 3
Heat to a temperature of 00-400 ° C. and add ammonia. Next, the exhaust gas containing this ammonia passes through the honeycomb catalyst, and the nitrogen oxides in the exhaust gas are reduced to nitrogen gas. As this catalyst, TiO 2 —V 2 O 5
-Wide range of materials such as WO 3 type are used.

【0012】次いで、窒素酸化物の除去された排ガス
は、熱交換器により熱回収され、煙突から外部に排出さ
れる。この熱交換器により回収された熱は、上記デミス
ターを通過した排ガスの加熱に利用することが熱効率の
面で好ましい。
Next, the exhaust gas from which the nitrogen oxides have been removed is subjected to heat recovery by the heat exchanger and discharged from the chimney to the outside. From the viewpoint of thermal efficiency, it is preferable to use the heat recovered by this heat exchanger for heating the exhaust gas that has passed through the demister.

【0013】[0013]

【実施例】板ガラスを生産しているガラス窯の排ガス
を、先ず湿式脱硫装置に導入した。この湿式脱硫装置に
おいては苛性ソーダ水が散布されており、排ガスを装置
下方より上方へ流動させ苛性ソーダ水と接触し、排ガス
中のSOx が除去される。次いで湿式脱硫装置を通過し
た排ガスはEP装置に導入され、排ガス中のダストが除
去された。この排ガスの温度は約60℃であった。
[Examples] Exhaust gas from a glass kiln producing sheet glass was first introduced into a wet desulfurization apparatus. In this wet desulfurization device, caustic soda water is sprinkled, and the exhaust gas is caused to flow upward from the lower part of the device to come into contact with the caustic soda water, and SO x in the exhaust gas is removed. Next, the exhaust gas that passed through the wet desulfurization device was introduced into the EP device, and the dust in the exhaust gas was removed. The temperature of this exhaust gas was about 60 ° C.

【0014】次いで、排ガスをデミスターに導入した。
このデミスターは、下方には貫通孔1μmの、上方には
貫通孔10μmの各ワイヤーメッシュを設け、両者の間
に散水管を設けたものである。このワイヤーメッシュ
は、排ガス中に含有される水蒸気の凝縮及び散水管の散
水により水滴が滴下する程度に湿潤していた。
Then, the exhaust gas was introduced into the demister.
In this demister, each wire mesh having a through hole of 1 μm in the lower part and a through hole of 10 μm in the upper part is provided, and a water spray pipe is provided between the two. The wire mesh was wet to the extent that water droplets dropped due to the condensation of water vapor contained in the exhaust gas and the water spray of the water spray pipe.

【0015】この下方のワイヤーメッシュより下方に入
口を設け排ガスを下方から上方に流し、上方のワイヤー
メッシュより上方に設けた出口より排出した。次いで、
デミスターの出口より排出された排ガスを350℃に加
熱し、アンモニアを添加した。次いでこの排ガスをハニ
カム触媒を通過し、排ガス中の窒素酸化物を窒素ガスに
還元し、外気へ排出した。
An exhaust gas was provided below the lower wire mesh to flow the exhaust gas from the lower side to the upper side, and discharged from an outlet provided above the upper wire mesh. Then
The exhaust gas discharged from the outlet of the demister was heated to 350 ° C., and ammonia was added. Next, the exhaust gas passed through the honeycomb catalyst, the nitrogen oxides in the exhaust gas were reduced to nitrogen gas, and the exhaust gas was discharged to the outside air.

【0016】かかる排ガスの処理において、ばいじん濃
度(ダスト、SOx )を測定した結果、デミスター入口
では約30mg/Nm3 、デミスター出口では約4mg
/Nm3 であった。
In the treatment of the exhaust gas, the dust concentration (dust, SO x ) was measured, and as a result, it was about 30 mg / Nm 3 at the demister inlet and about 4 mg at the demister outlet.
/ Nm 3 .

【0017】比較のため、上方ワイヤーメッシュを湿潤
状態にしないで、同様の排ガス処理を行ったところ、ば
いじん濃度はデミスター入口では約30mg/Nm3
デミスター出口では12〜18mg/Nm3 であった。
このように、本発明は、ばいじんの除去率がきわめて高
いので、その後の窒素酸化物の除去工程で脱硝触媒の閉
塞、劣化が生じにくい。
For comparison, when the same exhaust gas treatment was performed without making the upper wire mesh wet, the dust concentration was about 30 mg / Nm 3 at the demister inlet,
It was 12 to 18 mg / Nm 3 at the demister outlet.
As described above, according to the present invention, since the removal rate of soot and dust is extremely high, the denitration catalyst is unlikely to be blocked or deteriorated in the subsequent nitrogen oxide removal step.

【0018】[0018]

【発明の効果】本発明によれば、湿式脱硫された排ガス
に微量に含有されるダスト、SOx が高度に除去される
ので、その後の窒素酸化物の除去工程で脱硝触媒の閉
塞、劣化を生じ難く、長期間連続してガラス窯の排ガス
の脱硝を行うことができる。
EFFECTS OF THE INVENTION According to the present invention, since a small amount of dust and SO x contained in the wet desulfurized exhaust gas are highly removed, clogging and deterioration of the denitration catalyst are prevented in the subsequent nitrogen oxide removal step. It is difficult to occur, and it is possible to denitrate the exhaust gas of the glass kiln continuously for a long period of time.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 C03B 5/16 ZAB ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification code Internal reference number FI technical display location C03B 5/16 ZAB

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】ガラス窯の排ガス中のSOx を湿式脱硫
し、次いで湿式脱硫したガスをデミスターを通過させ、
ガス中のダストを除去し、次いでNH3 によりガス中の
NOxを還元除去するにあたり、デミスターを湿潤状態
に保持することを特徴とする排ガスの脱硝方法。
1. A the SO x in the exhaust gas of the glass furnace and wet desulfurization, then wet desulfurized gas is passed through the demister,
A method for denitrification of exhaust gas, which comprises maintaining a demister in a wet state when removing dust in the gas and then reducing and removing NO x in the gas with NH 3 .
JP5076216A 1993-03-10 1993-03-10 Method for denitrification of exhaust gas from glass kiln Pending JPH06262037A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5076216A JPH06262037A (en) 1993-03-10 1993-03-10 Method for denitrification of exhaust gas from glass kiln

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5076216A JPH06262037A (en) 1993-03-10 1993-03-10 Method for denitrification of exhaust gas from glass kiln

Publications (1)

Publication Number Publication Date
JPH06262037A true JPH06262037A (en) 1994-09-20

Family

ID=13598988

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5076216A Pending JPH06262037A (en) 1993-03-10 1993-03-10 Method for denitrification of exhaust gas from glass kiln

Country Status (1)

Country Link
JP (1) JPH06262037A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105797651A (en) * 2016-05-25 2016-07-27 北京神雾环境能源科技集团股份有限公司 Gas demister of slurry bed for hydrogenation of acetylene to ethylene
CN105833801A (en) * 2016-05-27 2016-08-10 北京神雾环境能源科技集团股份有限公司 Gas foam remover for acetylene hydrogenation type ethylene preparation trickle bed
CN105833803A (en) * 2016-05-27 2016-08-10 北京神雾环境能源科技集团股份有限公司 Gas foam remover for acetylene hydrogenation type ethylene preparation packing bubbling bed
CN105833806A (en) * 2016-05-27 2016-08-10 北京神雾环境能源科技集团股份有限公司 Gas foam remover for acetylene hydrogenation type ethylene preparation three-phase fluidized bed
KR20180119115A (en) * 2017-04-24 2018-11-01 에이지씨 가부시키가이샤 Exhaust Gas Treatment Method, Exhaust Gas Treatment Apparatus, Apparatus for Manufacturing Glass Article, and Method of Manufacturing Glass Article
CN114682070A (en) * 2020-12-28 2022-07-01 福建龙净脱硫脱硝工程有限公司 Ceramic flue gas treatment system

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105797651A (en) * 2016-05-25 2016-07-27 北京神雾环境能源科技集团股份有限公司 Gas demister of slurry bed for hydrogenation of acetylene to ethylene
CN105833801A (en) * 2016-05-27 2016-08-10 北京神雾环境能源科技集团股份有限公司 Gas foam remover for acetylene hydrogenation type ethylene preparation trickle bed
CN105833803A (en) * 2016-05-27 2016-08-10 北京神雾环境能源科技集团股份有限公司 Gas foam remover for acetylene hydrogenation type ethylene preparation packing bubbling bed
CN105833806A (en) * 2016-05-27 2016-08-10 北京神雾环境能源科技集团股份有限公司 Gas foam remover for acetylene hydrogenation type ethylene preparation three-phase fluidized bed
KR20180119115A (en) * 2017-04-24 2018-11-01 에이지씨 가부시키가이샤 Exhaust Gas Treatment Method, Exhaust Gas Treatment Apparatus, Apparatus for Manufacturing Glass Article, and Method of Manufacturing Glass Article
CN114682070A (en) * 2020-12-28 2022-07-01 福建龙净脱硫脱硝工程有限公司 Ceramic flue gas treatment system

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