JPH0352617A - Method for preventing dew condensation in dry deodorizing device - Google Patents
Method for preventing dew condensation in dry deodorizing deviceInfo
- Publication number
- JPH0352617A JPH0352617A JP1183579A JP18357989A JPH0352617A JP H0352617 A JPH0352617 A JP H0352617A JP 1183579 A JP1183579 A JP 1183579A JP 18357989 A JP18357989 A JP 18357989A JP H0352617 A JPH0352617 A JP H0352617A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- treated
- deodorizing device
- heated
- heater
- 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.)
- Granted
Links
- 230000001877 deodorizing effect Effects 0.000 title claims abstract description 27
- 238000009833 condensation Methods 0.000 title claims abstract description 13
- 230000005494 condensation Effects 0.000 title claims abstract description 13
- 238000000034 method Methods 0.000 title claims description 12
- 239000003463 adsorbent Substances 0.000 abstract description 13
- 238000005260 corrosion Methods 0.000 abstract description 12
- 230000007797 corrosion Effects 0.000 abstract description 12
- 238000010438 heat treatment Methods 0.000 abstract description 7
- 239000000463 material Substances 0.000 abstract description 4
- 238000010790 dilution Methods 0.000 abstract description 2
- 239000012895 dilution Substances 0.000 abstract description 2
- 238000001035 drying Methods 0.000 abstract 1
- 230000002035 prolonged effect Effects 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 41
- 235000019645 odor Nutrition 0.000 description 10
- 238000010586 diagram Methods 0.000 description 6
- 239000003595 mist Substances 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 3
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 229910021536 Zeolite Inorganic materials 0.000 description 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000011810 insulating material Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000010457 zeolite Substances 0.000 description 2
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000010800 human waste Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- -1 mercabutane Chemical compound 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、臭気或分を含有するガス中から臭気成分を吸
着除去する乾式脱臭装置の結露防止法に関するものであ
る.
〔従来の技術〕
従来、し尿や下水等の処理場、製紙工場及び各種化学工
場等から、硫化水素、メルカブタン及びアンモニア等の
臭気成分を含有するガスが発生し、当該ガス中の臭気成
分を脱臭処理するのに、活性炭やゼオライト等の吸着剤
を充填した乾式脱臭装置(以下脱臭装置という.)が用
いられている.上記脱臭装置では、特に冬期等において
、被処理ガス中の水分含量が飽和に近くなるため、水分
が装置内面及び吸着剤表面等で凝縮結露し、吸着剤の吸
着能力低下や寿命の短縮を生起する恐れがある.従って
、従来は第3図に示すように、被処理ガスAをミストセ
パレータ1に導入してミスト等の粒子を除去したのち、
ガス加熱器7で直接加熱し2〜5℃程度昇温して相対湿
度を低下させ、ファン2で脱臭塔3へ導入することによ
り結露を防止するという対策等がとられている.〔発明
が解決しようとする課題〕
従来の被処理ガスを加熱器で直接昇温する結露防止法で
は、加熱器内が高温・多湿の条件下に晒されるため、被
処理ガスに含有する硫化水素等の腐食性ガスにより加熱
器が腐食されやすく、特にヒータエレメントでは、更に
高温であるため、ステンレス材等の経済的な材質のヒー
タエレメントを用いることができず、チタン材等の、耐
食性を考慮した高価な特殊材が用いられているが、それ
でも腐食事故の問題を生じている.本発明は、腐食問題
を起す恐れがなく、且つ被処理ガスを確実に所定温度迄
昇温し結露を防止することができる脱臭装置の結露防止
法を提供しようするものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for preventing condensation in a dry deodorizing device that adsorbs and removes odor components from gas containing certain odors. [Conventional technology] Conventionally, gases containing odorous components such as hydrogen sulfide, mercabutane, and ammonia are generated from human waste and sewage treatment plants, paper mills, and various chemical plants, and it is necessary to deodorize the odorous components in the gases. A dry deodorizing device (hereinafter referred to as a deodorizing device) filled with an adsorbent such as activated carbon or zeolite is used for the treatment. In the above-mentioned deodorizing equipment, especially in winter, the water content in the gas to be treated is close to saturation, so water condenses on the inside of the equipment and on the surface of the adsorbent, resulting in a decrease in the adsorption capacity of the adsorbent and a shortened service life. There is a risk that Therefore, conventionally, as shown in FIG. 3, after introducing the gas A to be treated into the mist separator 1 to remove particles such as mist,
Measures are taken to prevent dew condensation by directly heating the gas with a gas heater 7 to raise the temperature by about 2 to 5 degrees Celsius, lowering the relative humidity, and introducing it into the deodorizing tower 3 with a fan 2. [Problem to be solved by the invention] In the conventional dew condensation prevention method in which the temperature of the gas to be treated is directly raised using a heater, the inside of the heater is exposed to high temperature and high humidity conditions, so hydrogen sulfide contained in the gas to be treated is The heater is easily corroded by corrosive gases such as, and the heater element in particular is at an even higher temperature, so it is not possible to use a heater element made of economical material such as stainless steel, and the corrosion resistance of titanium is considered. Although expensive special materials are used, corrosion accidents still occur. The present invention aims to provide a method for preventing dew condensation in a deodorizing device, which does not cause corrosion problems and can reliably raise the temperature of the gas to be treated to a predetermined temperature to prevent condensation.
上記事情に鑑みてなされた本発明の要旨は、臭気成分を
含有する被処理ガスを乾式法で脱臭処理する方法におい
て、前記被処理ガス中に加熱空気を混入して昇温したの
ち乾式脱臭装置へ導入することを特徴とする脱臭装置の
結露防止法である.(作 用)
腐食の恐れがない空気を空気加熱器で加熱し、得られた
加熱空気を腐食性の臭気成分を含有する被処理ガス中に
混入することにより、腐食原因になる被処理ガスを加熱
器に通すことなく、被処理ガスを昇温し、相対湿度を低
下させている.又相対湿度が低下された被処理ガスを脱
臭装置に導入することにより、吸着剤表面等での結露を
防止して臭気成分を吸着除去している.
(実施例)
以下本発明の方法を図面に基いて詳述する。The gist of the present invention, which was made in view of the above circumstances, is to provide a method for deodorizing a gas to be treated containing odor components by a dry method, in which heated air is mixed into the gas to be treated to raise the temperature, and then a dry deodorizer is used. This is a method for preventing dew condensation in deodorizing equipment, which is characterized by introducing it into a deodorizing device. (Function) By heating air with no risk of corrosion using an air heater and mixing the resulting heated air into the gas to be treated that contains corrosive odor components, the gas to be treated that causes corrosion can be removed. The temperature of the gas to be processed is raised and the relative humidity is lowered without passing it through a heater. In addition, by introducing the gas to be treated with reduced relative humidity into the deodorizing device, dew condensation on the adsorbent surface is prevented and odor components are adsorbed and removed. (Example) The method of the present invention will be explained in detail below based on the drawings.
第1図は本発明の一実施例の系統図、第2図は他の実施
例の系統図、第3図は従来方法の系統図である.尚各図
においては、同一機器には同一符番を用いている。1は
臭気或分を含有する被処理ガスAに同伴されたミストや
粉塵等を除去するためのミストセパレータである。2は
被処理ガスAを脱臭塔3へ導入するファンである.3は
活性炭やゼオライト等の吸着剤を充填し臭気或分を吸着
除去する脱臭装置である脱臭塔で、通常は吸着剤を層状
に充填した固定床式が用いられ、被処理ガスAが吸着剤
層を上向流にて流れるよう下部に被処理ガスAの導入口
、上部に臭気成分が除去された処理ガスBの導出口を具
備している.尚前記脱臭塔3は充填した吸着剤が流動化
する流動床式でも、又吸着剤を連続的に供給排出する移
動床式等でも乾式法であれば本発明の適用対象となる。Fig. 1 is a system diagram of one embodiment of the present invention, Fig. 2 is a system diagram of another embodiment, and Fig. 3 is a system diagram of a conventional method. In each figure, the same numbers are used for the same equipment. Reference numeral 1 denotes a mist separator for removing mist, dust, etc. entrained in the gas to be treated A containing a certain amount of odor. 2 is a fan that introduces the gas A to be treated into the deodorizing tower 3. 3 is a deodorizing tower which is a deodorizing device that is filled with an adsorbent such as activated carbon or zeolite and adsorbs and removes a certain amount of odor.Usually, a fixed bed type filled with adsorbent in layers is used, and the gas to be treated A is absorbed by the adsorbent. The chamber is equipped with an inlet for the gas A to be treated at the bottom and an outlet for the gas B from which odor components have been removed at the top so that the gas to be treated can flow upward through the layer. The present invention is applicable to the deodorizing tower 3 as long as it is a dry method, such as a fluidized bed type in which the packed adsorbent is fluidized, or a moving bed type in which the adsorbent is continuously supplied and discharged.
4は空気Cの加熱器で、ヒータエレメント5を設けた電
熱式の加熱器が温度調節や維持管理等の容易性により好
ましいが、蒸気等の加熱媒体を用いた熱交換式であって
も、又バーナを用いた加熱であってもよい.従来方法に
用いられている被処理ガスAの加熱器7では、主にヒー
タエレメント5を設けた電熱式の加熱器が用いられてい
る。6は加熱された空気Cを被処理ガスA中に混入する
ブロワである。8は外気温により加熱ラインが冷却され
、水分が結露しないように装置及び配管等を被覆した保
温材である.
臭気或分を含有する被処理ガスAを脱臭処理する方法に
おいて、従来は、第3図に記載されているように、ミス
トセパーレータ1でミスト等の粒子が除去された被処理
ガスAを、ガス加熱器7で直接加熱して2〜5℃程度昇
温したのち、ファン2で脱臭塔3へ導入している.従っ
て、加熱器7の内壁面やヒータエレメント5は高温でガ
ス加熱器7内の多湿雰囲気に晒されるため、被処理ガス
Aに含有する臭気或分中の硫化水素等の腐食性ガスによ
る影響を大きく受け、腐食されやすい.本発明の実施例
を示した第1図においては、空気加熱器4で加熱された
空気Cを、ファン2の前段の被処理ガスA中へ混入して
、被処理ガスAを加熱しており、又他の実施例の第2図
においては、ファン2の後段の被処理ガスA中へ混入し
ている。4 is a heater for air C, and an electric heater equipped with a heater element 5 is preferable due to ease of temperature control and maintenance, but even a heat exchange type heater using a heating medium such as steam, Heating may also be done using a burner. As the heater 7 for the gas to be processed A used in the conventional method, an electric heater equipped with a heater element 5 is mainly used. A blower 6 mixes heated air C into the gas A to be treated. 8 is a heat insulating material that covers the equipment, piping, etc. so that the heating line is cooled by the outside temperature and moisture does not condense. Conventionally, in a method for deodorizing a gas A to be treated that contains a certain amount of odor, as shown in FIG. After being directly heated with a gas heater 7 to raise the temperature by about 2 to 5°C, it is introduced into a deodorizing tower 3 with a fan 2. Therefore, since the inner wall surface of the heater 7 and the heater element 5 are exposed to the high temperature and humid atmosphere inside the gas heater 7, they are not affected by the odor contained in the gas A to be treated or by corrosive gases such as hydrogen sulfide in the gas. It is highly susceptible to corrosion and is easily corroded. In FIG. 1 showing an embodiment of the present invention, air C heated by an air heater 4 is mixed into the gas to be treated A at the front stage of the fan 2 to heat the gas to be treated A. , and in another embodiment shown in FIG. 2, the gas is mixed into the gas A to be treated after the fan 2.
従って加熱器4は、腐食成分と接触せず、その影響を受
けない.尚被処理ガスAの昇温温度を従来と同様に2〜
5℃位に調節するべく、加熱空気Cの混入量及び温度が
制御されるが、通常混入量は全ガス量の約10voj%
程度に調節される.本発明の実施例において、ファン2
の送風量に余裕がある場合には第1図の実施例を用い、
ファン2に余裕がない場合には、設置面積は大きくなる
が、第2図の実施例を用いるのが好ましい.しかしそれ
らに限定されるものではない.
〔発明の効果〕
本発明は、加熱空気の混入により脱臭装置での処理ガス
量も若干増加するが、加熱器の腐食、特にヒータエレメ
ントの腐食問題が防止され、耐食性の高価な材料を用い
る必要がなく、又空気の混入希釈によって湿度が低下さ
れるため、より結露しにくくなり、確実に脱臭装置内の
吸着剤表面等で結露が防止され、吸着剤寿命を大巾に延
ばすことができ、且つ温度制御も容易となる等の大きな
効果が得られる。Therefore, the heater 4 does not come into contact with corrosive components and is not affected by them. In addition, the heating temperature of the gas to be processed A is 2 to 2 as before.
The amount of heated air C mixed in and the temperature are controlled to adjust the temperature to about 5°C, but usually the mixed amount is about 10 voj% of the total gas amount.
It is adjusted accordingly. In an embodiment of the invention, the fan 2
If there is enough air flow, use the embodiment shown in Figure 1.
If there is not enough room for the fan 2, it is preferable to use the embodiment shown in FIG. 2, although the installation area will be large. However, it is not limited to these. [Effects of the Invention] Although the amount of gas to be processed in the deodorizing device increases slightly due to the mixing of heated air, the present invention prevents corrosion of the heater, especially corrosion of the heater element, and eliminates the need to use expensive corrosion-resistant materials. In addition, since the humidity is lowered by the dilution of air, dew condensation is less likely to occur, and dew condensation is reliably prevented on the surface of the adsorbent in the deodorizing device, greatly extending the life of the adsorbent. In addition, great effects such as easy temperature control can be obtained.
第1図は本発明の一実施例の系統図、第2図は他の実施
例の系統図、第3図は従来方法の系統図である.
1;ミストセバレータ、2;ファン、3;脱臭塔、4;
空気加熱器、5;ヒータエレメント、6;ブロワ、7;
ガス加熱器、8;保温材、A;被処理ガス、B;処理ガ
ス、C;空気.Fig. 1 is a system diagram of one embodiment of the present invention, Fig. 2 is a system diagram of another embodiment, and Fig. 3 is a system diagram of a conventional method. 1; Mist separator, 2; Fan, 3; Deodorizing tower, 4;
Air heater, 5; Heater element, 6; Blower, 7;
Gas heater, 8; Heat insulating material, A; Gas to be treated, B; Processing gas, C; Air.
Claims (1)
方法において、前記被処理ガスに加熱空気を混入して昇
温したのち乾式脱臭装置へ導入することを特徴とする乾
式脱臭装置の結露防止法。Preventing condensation in a dry deodorizing device, in a method of deodorizing a gas containing odor components by a dry method, characterized in that the gas to be treated is mixed with heated air to raise its temperature and then introduced into the dry deodorizing device. Law.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1183579A JPH0352617A (en) | 1989-07-18 | 1989-07-18 | Method for preventing dew condensation in dry deodorizing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1183579A JPH0352617A (en) | 1989-07-18 | 1989-07-18 | Method for preventing dew condensation in dry deodorizing device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0352617A true JPH0352617A (en) | 1991-03-06 |
| JPH0512008B2 JPH0512008B2 (en) | 1993-02-17 |
Family
ID=16138285
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1183579A Granted JPH0352617A (en) | 1989-07-18 | 1989-07-18 | Method for preventing dew condensation in dry deodorizing device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0352617A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH08196860A (en) * | 1995-01-30 | 1996-08-06 | Dia Tec Kk | Deodorizing device |
| JP2000051647A (en) * | 1998-01-23 | 2000-02-22 | Shigeru Tanaka | Gas purifier, substance collector and deodorizer |
| JP2006329596A (en) * | 2005-05-30 | 2006-12-07 | Daikin Ind Ltd | Humidity control device |
| JP2013545592A (en) * | 2010-10-01 | 2013-12-26 | ダニエリ アンド シー.オフィス メカニケ エスピーエー | Scrap cutting machine powder removing device and related method |
| JP2019037312A (en) * | 2017-08-22 | 2019-03-14 | メタウォーター株式会社 | Deodorization system |
-
1989
- 1989-07-18 JP JP1183579A patent/JPH0352617A/en active Granted
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH08196860A (en) * | 1995-01-30 | 1996-08-06 | Dia Tec Kk | Deodorizing device |
| JP2000051647A (en) * | 1998-01-23 | 2000-02-22 | Shigeru Tanaka | Gas purifier, substance collector and deodorizer |
| JP2006329596A (en) * | 2005-05-30 | 2006-12-07 | Daikin Ind Ltd | Humidity control device |
| JP2013545592A (en) * | 2010-10-01 | 2013-12-26 | ダニエリ アンド シー.オフィス メカニケ エスピーエー | Scrap cutting machine powder removing device and related method |
| JP2019037312A (en) * | 2017-08-22 | 2019-03-14 | メタウォーター株式会社 | Deodorization system |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0512008B2 (en) | 1993-02-17 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP4174969B2 (en) | Garbage disposal equipment | |
| JPH11137950A (en) | Treatment of waste gas of hot drying process and more particularly sludge drying process of sewer sludge drying device and equipment for execution this method | |
| JPWO1999038624A1 (en) | Food waste treatment equipment | |
| KR100231651B1 (en) | Apparatus and method fermentation for food waste | |
| JPH0512008B2 (en) | ||
| KR101138500B1 (en) | Food Waste Treatment Apparatus having Dehumidification Device | |
| KR100743544B1 (en) | Deodorization System of Environment-Friendly Food Waste Disposer | |
| JP4972987B2 (en) | Gas processing equipment | |
| WO2002051454A1 (en) | Device and method for treatment of polluted air | |
| KR101929418B1 (en) | Apparauts for removing odor in cooking process using heat pipe | |
| JP3551278B2 (en) | Deodorizing method and device for kitchen waste treatment device | |
| JP3929719B2 (en) | Deodorizing apparatus and deodorizing method | |
| JP3149498B2 (en) | Garbage processing machine | |
| JPH07253226A (en) | Air purifier with humidification function | |
| KR101229985B1 (en) | Device for pre-treating contaminated air and deordorizing system using the same | |
| JPS6321312Y2 (en) | ||
| JP3377724B2 (en) | Heat exchanger used for fermentation equipment | |
| CN105873620A (en) | Method and device for performing PCO reaction and air purifier comprising the device | |
| JP3637807B2 (en) | Hot air generator, air purifier, dehumidifier, waste disposal device, garbage disposal device | |
| KR20090100085A (en) | Food Waste Disposal Device | |
| JP3240844B2 (en) | Garbage processing equipment | |
| JP3549574B2 (en) | Deodorizing device | |
| Wolstenholme | The Latest Odor Control Issues and Solutions for Wastewater Systems | |
| JPH08946A (en) | Deodorizing process for exhaust gas | |
| KR102811663B1 (en) | Deodorizing apparatus |