JPS59199018A - Deodorizing method - Google Patents

Deodorizing method

Info

Publication number
JPS59199018A
JPS59199018A JP58073034A JP7303483A JPS59199018A JP S59199018 A JPS59199018 A JP S59199018A JP 58073034 A JP58073034 A JP 58073034A JP 7303483 A JP7303483 A JP 7303483A JP S59199018 A JPS59199018 A JP S59199018A
Authority
JP
Japan
Prior art keywords
gas
glycerin
deodorizing
na2so3
effect
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
JP58073034A
Other languages
Japanese (ja)
Inventor
Kenzo Abe
阿部 健蔵
Junji Hagiwara
萩原 純二
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.)
Fuso KK
Original Assignee
Fuso KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Fuso KK filed Critical Fuso KK
Priority to JP58073034A priority Critical patent/JPS59199018A/en
Publication of JPS59199018A publication Critical patent/JPS59199018A/en
Pending legal-status Critical Current

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  • Treating Waste Gases (AREA)

Abstract

PURPOSE:To reduce the decomposition of Na2SO3 even in a hot gas and to enhance the odorizing effect by using an aq. soln. of Na2SO3, added with glycerine, as an absorbing liquid. CONSTITUTION:An odorous gas contg. aldehydes, is introduced into an absorption tower 1. An absorbing liquid consisting of an aq. soln. of Na2SO3 added with glycerine is sprinkled over a packing material layer 2 from a circulation storage tank 5 while controlling the flow rate with a flowmeter 8, and the gas is deodorized by contact with the liquid.

Description

【発明の詳細な説明】 この発明は、薬液洗浄脱臭方法に関する。[Detailed description of the invention] The present invention relates to a chemical cleaning and deodorizing method.

さらに詳しくは、アルデヒド類を含む臭気ガスの脱臭方
法に関するものである。
More specifically, the present invention relates to a method for deodorizing odor gases containing aldehydes.

アルデヒド@を含む臭気ガスは、し尿や汚泥の湿式酸化
、活性汚泥の乾燥や焼却、グラスチックの加熱酸jd1
 シェルモールド鋳造といった有機物を熱処理する工程
の排気に出現するものでちって、悪臭公害の原因とされ
ることが多い。除去手段としての脱臭にtlよ、過酸化
水素や天運塩素酸ソーダの水溶液、あるいは、オゾンを
用いて酸化により無臭化する方法が実施されている。と
ころが、これらのS化剤は、ガス中のアルデヒドの濃度
に応じて、高濃!変で使用しなければならず余剰分の排
出が、二次公害を起す欠点がある。また、酸化条件によ
ってはアルデヒドが有機酸に変化して異種の悪臭を生ず
ることがある。さらに工程の性格上ガス温度が高いこと
から、酸化剤によってl/i熱分解されて、脱臭効果が
ほとんど得られなくなる事例も指摘されている。
Odor gases containing aldehydes are generated by wet oxidation of human waste and sludge, drying and incineration of activated sludge, heating acid of glass
It is a substance that appears in the exhaust gas from processes such as shell mold casting, which heat-treats organic materials, and is often considered to be the cause of odor pollution. For deodorization as a means of removal, a method of deodorizing by oxidation using hydrogen peroxide, an aqueous solution of sodium chlorate, or ozone has been implemented. However, these S-forming agents are highly concentrated depending on the concentration of aldehyde in the gas! It has the disadvantage that it must be used at different times, and the excess discharge causes secondary pollution. Furthermore, depending on the oxidation conditions, aldehydes may change to organic acids, producing a different kind of bad odor. Furthermore, since the gas temperature is high due to the nature of the process, it has been pointed out that there are cases where the gas is thermally decomposed by l/i by the oxidizing agent, resulting in almost no deodorizing effect.

本発明者らは、これらの間頌点が燕<、アルデヒド類に
対する無臭化効果を卒げ、しかも、温度の高いガスにも
適用0T能な脱臭方法を追求して鋭意研究の結果、悪硫
酸ソーダを吸収液とするにあたり、これに適量のグリセ
リン、を添加することによって所期の目的を達成し1尋
ることを認め本発明を完成した。
The present inventors have pursued a deodorizing method that has no odor-reducing effect on aldehydes and is also applicable to high-temperature gases, and as a result of intensive research, we have found that By adding an appropriate amount of glycerin to soda as an absorbing liquid, the inventors achieved the desired objective and completed the present invention.

すなわち、本発明は、グリセリンを添加した唾硫嘔ソー
ダを吸収液とする薬液洗浄脱臭方法である。
That is, the present invention is a chemical cleaning and deodorizing method using salivary soda added with glycerin as an absorbing liquid.

アルデヒド類を主成分とする臭気ガスを対象とする洗浄
脱臭用薬液に亜硫酸ソーダを用いる方法は既に提唱され
ている。しかし、亜硫酸ソーダ液は空気との気液接触に
より色数にγ農咥が減少することが印ら几ている(F水
道協会誌vo120.No 225.1983/215
4〜59頁参照)。したがって、この方法を直後脱臭装
(置に適用しようとす几は多喰の亜硫酸ソーダが脱処反
応ぐこ関与することなく消耗されて不経済である(lず
かりでなく、高濃度のアルデヒド類に対しては脱臭効果
が不光分となる。
A method has already been proposed in which sodium sulfite is used in a chemical solution for cleaning and deodorizing odor gases whose main components are aldehydes. However, it has been shown that the color number of sodium sulfite solution decreases due to gas-liquid contact with air (F Water Works Association Magazine vol. 120. No. 225. 1983/215
(See pages 4-59). Therefore, if this method is applied immediately to a deodorizing device, a large amount of sodium sulfite will be consumed without taking part in the deodorization reaction, making it uneconomical. The deodorizing effect is opaque.

唾1流酸ソーダを含む吸収液に一定の#度でグリセリン
を添加することにより、高4度の臭気ガスに灯して無臭
化効果を得ることが町1目となる。実施例1に示すよう
に添加グリセリンの/#1距が1〜4 w / v %
のところで最大効果が挙げられる。
By adding glycerin at a certain degree to an absorbing liquid containing sodium sulfate, it is possible to obtain an odorless effect by lighting it with a high-4 degree odor gas. The /#1 range of added glycerin is 1-4 w/v% as shown in Example 1
The greatest effect can be seen here.

実施例1 洗気ピン(250m7!”d)VC入れた亜硫酸ソーダ
とアセトアルデヒド約100 ppmずつを含む水溶液
に、#1厖(il−変えてグリセリンを添加し、空気(
I L/ min ) t3時iNj吹き込んでガスク
ロマトグラフ法により通気前後のアセトアルデヒド濃岨
を測定し、その分解率とグリセリン濃+f(の関係を求
めると表1のとPりであった。
Example 1 Air washing pin (250m7!"d) To an aqueous solution containing approximately 100 ppm of sodium sulfite and acetaldehyde in VC, add #1 volume (il) of glycerin, and add air (
I L/min ) At t3, iNj was blown into the reactor, and the acetaldehyde concentration before and after aeration was measured by gas chromatography, and the relationship between the decomposition rate and glycerin concentration + f was determined as shown in Table 1.

表1 徂疏・唆ソーグとアルデヒド類との間に71、次式に示
すような付加反応が起るとされている。
Table 1 It is said that an addition reaction as shown in the following formula occurs between 71 and aldehydes.

これは平衡反応なので、亜硫酸ソーダが不足すると逆反
応を生じアルデヒド類が再生する。
This is an equilibrium reaction, so if there is a shortage of sodium sulfite, a reverse reaction occurs and aldehydes are regenerated.

グリセリンは亜硫酸ソーダの酸化を防止する効果があり
、グリセリン#度が高い程防止効果も促進されるが前記
実施例1でのアセトアルデヒドの分解率には極値があっ
てグリセリン横変の一ヒ昇とは必ずしも一致しない。し
たがって、本発明におけるグリセリンの添カロ効果は=
ll’u硫酸ンーグの酸化作用によるものではなく反応
偽作t・よ不明であるが、4肴のグリセリンが逆反応の
進行を妨げる作用をするので。
Glycerin has the effect of preventing the oxidation of sodium sulfite, and the higher the glycerin content, the more the prevention effect is promoted, but the decomposition rate of acetaldehyde in Example 1 has an extreme value, and the lateral change of glycerin increases rapidly. does not necessarily match. Therefore, the effect of adding glycerin in the present invention is =
This is not due to the oxidizing effect of ll'u sulfuric acid, but is due to a reaction falsification.It is unclear, but the glycerin in the four dishes acts to prevent the progress of the reverse reaction.

はないかと考えられる。It is thought that there is no such thing.

一方、岨硫l浚ソーダは熱により分、解し易く、40℃
以ヒのガスに対しては特に鋭敏であるが、実施例3vC
,示tとおり、本=i色明によれば熱ガスに対しても亜
硫酸ソーダの分解金少くし脱臭効果金挙げることが出来
る。
On the other hand, Kasu l dredged soda is easily decomposed and decomposed by heat, and is heated to 40°C.
Although it is particularly sensitive to the following gases, Example 3vC
As shown, according to the present invention, sodium sulfite decomposes decomposition of sodium sulfite and has a deodorizing effect even on hot gases.

実)血 汐Il 2 ジンマーマンプロセスによるし尿の湿式酸化処理排ガス
(常@)を窮J−図に示す俤な脱臭装置にかけた結東の
一例は表2のと卦りであった。1g1図において、排ガ
スリまダクトダ7パ−13より流速1則ボ用オリフィス
14しよび15を経て吸収塔1に誘引した。吸収液け、
1に頃貯留槽5からポンプIで汲みトげて、流嫂計8で
流量を調整しつつ吸収塔内の充填材層2の上部から塔内
へ散布し充填材りでガスと気7夜接触させた。その他同
図藺′こ忰いて、3はデミスタ−14はガス排出口、1
ipH計、12はマノメーター、6はバルブである。
Table 2 shows an example of a wet oxidation treatment of human waste using the Zimmerman process. In Figure 1g1, the exhaust gas was drawn into the absorption tower 1 from the exhaust gas reservoir duct 7 part 13 through orifices 14 and 15 for flow rate 1 law. Absorbent liquid,
Around 1 hour, the pump I pumps the water from the storage tank 5, and while adjusting the flow rate with the flow meter 8, it is dispersed from the top of the packing layer 2 in the absorption tower into the tower, and the filling material is used to collect gas and air for 7 nights. brought into contact. Others, looking at the same figure, 3 is a demister, 14 is a gas outlet, 1
An ipH meter, 12 a manometer, and 6 a valve.

なか、;悦臭装・置のi[転条件+rよ次のと知り、測
定はガスクロマトグラフ法、三点比校式臭袋法によった
Knowing that the i [transformation condition + r] of the Yue odor apparatus and equipment was as follows, the measurements were performed using the gas chromatography method and the three-point ratio odor bag method.

処理ガスt:150,71′/、、ガス空塔、III[
:1.5m/s、iガス比::2!/7F/、光填高さ
: L 8 tn 、吸収液:亜硫酸ナトリウム1.3
w / v %、グリセリン3 w / v%、pH7
実施例3 活性汚泥の乾燥炉排ガス金、水洗塔で冷却後ガス温度5
0℃の状態で実施例2と同様の脱臭装置で処理し、アル
デヒド類の除去効果金がスクロマトグラフ法で測定した
一例it表3Vこ示す。
Processing gas t: 150,71'/, gas column, III [
:1.5m/s, i gas ratio: :2! /7F/, light filling height: L 8 tn, absorption liquid: sodium sulfite 1.3
w/v%, glycerin 3 w/v%, pH 7
Example 3 Activated sludge drying furnace exhaust gas gold, gas temperature after cooling in water washing tower 5
Table 3V shows an example in which the sample was treated at 0° C. using the same deodorizing device as in Example 2, and the aldehyde removal effect was measured by chromatography.

表3 庄)本発明においてホルムアルデヒドのL余去率は必ず
しも高くないが、ホルムア ルデヒドの感知閾値は’l’p p mと關いので脱臭
への影響はほとんどない。
Table 3) In the present invention, the L removal rate of formaldehyde is not necessarily high, but since the formaldehyde detection threshold is close to 'l' p p m, it has little effect on deodorization.

脱臭装置の吸収液の余剰排出分を、水洗塔の冷却水の一
部に混合使用したところ、脱臭効果に変り(はなく、残
存岨硫酸ソーダのほとんどを熱にLり分解出来た。
When the surplus of the absorbent discharged from the deodorizing device was mixed with a portion of the cooling water of the washing tower, the deodorizing effect was improved (although not), and most of the remaining sodium sulfate was thermally decomposed.

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

υ1図:は、本発明方法を夷l進するのに適した脱県裟
1曖の一1クリを示す線路図である。 1・・・吸収塔  2・・・充填材、曽  3・・・デ
ミスタ−5:(吸収液)循環貯留1臂
Fig. υ1: is a railway diagram showing one of the most difficult routes suitable for carrying out the method of the present invention. 1...Absorption tower 2...Filling material, Zeng 3...Demister-5: (Absorption liquid) circulation storage 1 arm

Claims (1)

【特許請求の範囲】 1、グリセリンを添加した亜硫酸ソーダ水溶液を吸収液
とする薬液洗浄脱臭方法。 2、後段階で用いた吸収液の余剰排出部を前段階の吸収
液として再使用する特許請求の範(用1の方法。 3、脱臭に用いた吸収液の余剰排出部を前置冷却装置の
冷却水の一部として再使用する特許請求の範囲1の方法
[Claims] 1. A chemical cleaning and deodorizing method using an aqueous sodium sulfite solution to which glycerin is added as an absorbing liquid. 2. A claim in which the surplus discharge part of the absorption liquid used in the later stage is reused as the absorption liquid in the previous stage (the method of use 1. 3. The surplus discharge part of the absorption liquid used for deodorization is reused as the absorption liquid in the previous stage). 2. The method of claim 1, wherein the method is reused as part of the cooling water.
JP58073034A 1983-04-27 1983-04-27 Deodorizing method Pending JPS59199018A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58073034A JPS59199018A (en) 1983-04-27 1983-04-27 Deodorizing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58073034A JPS59199018A (en) 1983-04-27 1983-04-27 Deodorizing method

Publications (1)

Publication Number Publication Date
JPS59199018A true JPS59199018A (en) 1984-11-12

Family

ID=13506656

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58073034A Pending JPS59199018A (en) 1983-04-27 1983-04-27 Deodorizing method

Country Status (1)

Country Link
JP (1) JPS59199018A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103877851A (en) * 2014-04-14 2014-06-25 青岛银河环保股份有限公司 Sewage treatment plant deodorizing device with pH buffer function

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS515994A (en) * 1974-07-03 1976-01-19 Koito Kogyo Kk KOSENSHIKIKEIKAISOCHI

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS515994A (en) * 1974-07-03 1976-01-19 Koito Kogyo Kk KOSENSHIKIKEIKAISOCHI

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103877851A (en) * 2014-04-14 2014-06-25 青岛银河环保股份有限公司 Sewage treatment plant deodorizing device with pH buffer function

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