JP2003019420A - Method for cleaning volatile organic halogen compound- containing air - Google Patents
Method for cleaning volatile organic halogen compound- containing airInfo
- Publication number
- JP2003019420A JP2003019420A JP2001245794A JP2001245794A JP2003019420A JP 2003019420 A JP2003019420 A JP 2003019420A JP 2001245794 A JP2001245794 A JP 2001245794A JP 2001245794 A JP2001245794 A JP 2001245794A JP 2003019420 A JP2003019420 A JP 2003019420A
- Authority
- JP
- Japan
- Prior art keywords
- discharge
- air
- activated carbon
- halogen compound
- hollow fiber
- 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
Links
Landscapes
- Treating Waste Gases (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】この発明は、トリクロロエチ
レン、テトラクロロエチレン、メチルブロマイドなどの
有害な揮発性有機ハロゲン化合物(以下汚染物質と言
う)に汚染された空気の浄化技術に関するものである。TECHNICAL FIELD The present invention relates to a technology for purifying air contaminated with harmful volatile organic halogen compounds (hereinafter referred to as pollutants) such as trichloroethylene, tetrachloroethylene, and methyl bromide.
【0002】[0002]
【従来の技術】人体に有害なトリクロロエチレンなどの
汚染物質を含有する空気を浄化するには幾つかの技術が
あるが、活性炭による吸着法が一般的である。ここで汚
染物質を吸収した使用済みの活性炭は、過熱蒸気による
再生で再使用するか、あるいは焼却処理している。しか
し過熱蒸気による再生では、加熱蒸気の発生装置が別途
必要であるばかりか、再生された汚染物質とそれに汚染
された凝縮水の無害化処理が更に必要とする。一方焼却
処理法では、燃焼時発生する無機ハロゲンによって焼却
炉の損傷が激しく、更には猛毒なダイオキシン類の発生
の恐れがある。また紫外線による分解法も提案されてい
るが、この方法では汚染物質濃度が低い時は有効である
が、高濃度では充分に分解出来ない欠点があり、また四
塩化炭素などの難分解性物質は処理困難である。2. Description of the Related Art There are several techniques for purifying air containing pollutants such as trichlorethylene, which are harmful to the human body, but the adsorption method using activated carbon is generally used. The used activated carbon that has absorbed pollutants is either reused by regeneration with superheated steam or incinerated. However, in the case of regeneration with superheated steam, not only a generator for heating steam is separately required, but also decontamination treatment of regenerated pollutants and condensed water contaminated with the pollutants is further required. On the other hand, in the incineration method, the inorganic halogen generated during combustion causes severe damage to the incinerator, and furthermore, there is a possibility that toxic dioxins are generated. Although a decomposition method using ultraviolet rays has also been proposed, this method is effective when the concentration of pollutants is low, but it has the drawback that it cannot be decomposed sufficiently at high concentrations. It is difficult to process.
【0003】[0003]
【発明が解決しようとしている課題】従来の汚染物質を
含有する空気を浄化する方法のうち、活性炭法では使用
済み活性炭の焼却、あるいは再生汚染物質の処理工程が
別途必要であり、紫外線法では高濃度の汚染物質を含有
する空気の場合充分に浄化するには処理装置が大型にな
り、広い設置面積を要する。本発明では、汚染物質の回
収と無害化処理を同一装置内で行うように工夫して装置
の小型化を計り、特に敷地に余裕のない街中の小規模な
クリーニング店などの土壌浄化に伴なって発生する汚染
空気の浄化に寄与するものである。また放電処理では、
温度が低くても難分解性の有機物を分解するので、ダイ
オキシン類の発生を実質皆無にすることが出来る。Among the conventional methods for purifying air containing pollutants, the activated carbon method requires incineration of used activated carbon or a treatment step of regenerated pollutants, and the ultraviolet method requires high processing. In the case of air containing a high concentration of pollutants, the processing equipment becomes large and a large installation area is required for sufficient purification. In the present invention, the device is downsized by devising the collection and detoxification treatment of pollutants in the same device, and is particularly associated with soil purification such as a small-scale cleaning shop in a city where there is no room on the site. It contributes to the purification of polluted air generated as a result. Also, in the discharge treatment,
Even if the temperature is low, it decomposes hardly-decomposable organic substances, so that generation of dioxins can be virtually eliminated.
【0004】[0004]
【課題を解決するための手段】本発明は、汚染物質を含
有する空気を加熱空気再生型活性炭あるいは中空糸膜に
よって汚染物質を回収濃縮して浄化し、汚染物質を高濃
度に含有する再生空気または透過空気を直ちに放電部に
導入して分解して無害化する連続した方法である。この
方法では再生空気または透過空気の体積は被処理空気量
よりはるかに少なくすることが出来るので、放電部で処
理する空気量が少なくなり、放電処理に要する電力を最
小限にし、その結果浄化コストを大幅に軽減することが
出来る。また処理によって生成するハロゲン化ナトリウ
ムあるいはカルシウムは無害物質であり、さらなる処理
の必要が無い。DISCLOSURE OF THE INVENTION According to the present invention, regenerated air containing pollutants at a high concentration is obtained by recovering and concentrating pollutants with heated air regenerated activated carbon or hollow fiber membranes to purify air containing pollutants. Alternatively, it is a continuous method in which the permeated air is immediately introduced into the discharge part and decomposed to render it harmless. With this method, the volume of regenerated air or permeated air can be made much smaller than the amount of air to be treated, so the amount of air to be treated in the discharge part is reduced and the electric power required for discharge treatment is minimized, resulting in purification cost. Can be significantly reduced. Further, sodium halide or calcium halide generated by the treatment is a harmless substance and does not require further treatment.
【0005】[0005]
【発明の実施の形態】本発明では、先ず汚染した空気を
活性炭部に接触せしめて汚染物質を除去し放出する。活
性炭から汚染物質が漏洩しだす直前に通気を中止し、少
量の空気を通気しながら活性炭を加熱して、吸着してい
た汚染物質を追い出す。その汚染物質を高濃度に含有し
た空気を放電部に直接導入して分解する。放電部から排
出した空気は無機アルカリ性物質を入れた中和部に導入
して分解で生じた無機ハロゲンを除去する。ここで活性
炭部を2個設け、一方が吸着している時間に他方は再生
しているようにする。吸着の終点直前に2個を交代させ
れば、汚染空気を連続的に浄化することが可能になる。
本発明で使用する活性炭部は、外部あるいは内部に加熱
用ヒーターを備える。具体的には2筒式ヒートレスエア
ドライヤーを転用して充填剤を粒状活性炭に置き換え、
ヒーターを備え、タイマーで吸着と再生を交互に切り替
える。BEST MODE FOR CARRYING OUT THE INVENTION In the present invention, first, contaminated air is brought into contact with an activated carbon portion to remove and release pollutants. Immediately before the pollutant begins to leak from the activated carbon, the ventilation is stopped, and the activated carbon is heated while ventilating a small amount of air to expel the adsorbed contaminant. Air containing a high concentration of the pollutant is directly introduced into the discharge part to decompose it. The air discharged from the discharge part is introduced into a neutralization part containing an inorganic alkaline substance to remove the inorganic halogen generated by the decomposition. Here, two activated carbon parts are provided so that one is adsorbed and the other is regenerated. By replacing two immediately before the end point of adsorption, it becomes possible to continuously purify contaminated air.
The activated carbon part used in the present invention is equipped with a heater for heating on the outside or inside. Specifically, divert a two-cylinder heatless air dryer to replace the filler with granular activated carbon,
Equipped with a heater, the timer alternately switches between adsorption and regeneration.
【0006】一方汚染物質の回収濃縮に中空糸膜を使用
する場合は、汚染空気を中空糸内部に導入し、外部を真
空ポンプで減圧にする。ポンプの排気を放電部に導入す
る。ここで膜の材質は非多孔質シリコーンが好適であ
る。On the other hand, when a hollow fiber membrane is used for collecting and concentrating pollutants, contaminated air is introduced into the hollow fiber and the outside is depressurized by a vacuum pump. The pump exhaust is introduced into the discharge section. Here, the material of the membrane is preferably non-porous silicone.
【0007】放電部は、接ガス部が耐酸性であれば無声
放電式あるいは沿面放電式の市販のオゾン発生器が使用
出来る。As the discharge part, a commercially available ozone generator of silent discharge type or creeping discharge type can be used if the gas contact part is acid resistant.
【0008】中和部は、粒状の石灰石またはソーダライ
ムの充填筒あるいは炭酸ナトリウム水溶液または石灰乳
の洗浄塔が適当である。ここで無機ハロゲンは、ハロゲ
ン化ナトリウムまたはカルシウム、あるいは次亜ハロゲ
ン酸ナトリウムまたはカルシウムなどの無害物質になり
下水道に放流することが出来る。As the neutralizing section, a packed cylinder of granular limestone or soda lime, or a washing tower of sodium carbonate aqueous solution or lime milk is suitable. Here, the inorganic halogen becomes a harmless substance such as sodium or calcium halide, or sodium or calcium hypohalite and can be discharged into the sewer.
【0009】本発明を実施するには、汚染物質の濃度に
よって回収濃縮部を選択する。即ち、空気中の汚染物質
の濃度が比較的低い場合は中空糸膜を、濃度が高い場合
は活性炭を採用することが望ましい。また放電部は、汚
染物質が比較的分解し易い臭素系の場合は無声放電が、
難分解性の塩素系の場合は沿面放電が適当である。In practicing the present invention, the recovery concentrator is selected according to the concentration of contaminants. That is, it is desirable to use a hollow fiber membrane when the concentration of pollutants in the air is relatively low, and to use activated carbon when the concentration is high. In addition, the discharge part uses silent discharge when pollutants are relatively easy to decompose,
In the case of persistent chlorine-based materials, creeping discharge is suitable.
【00010】[00010]
【発明の効果】本発明で無害化される揮発性有機ハロゲ
ン化合物には、テトラクロロエチレン、トリクロロエチ
レン、1.2−ジクロロエチレン、クロロエチレン、四
塩化炭素、クロロフォルム、メチレンクロライド、1.
1.1−トリクロロエタン、1.2−ジクロロエタン、
メチレンブロマイド、メチルブロマイドなどが挙げられ
る。本発明による装置は、構造上小型にすることが容易
なので設置面積が少なくて済み、たとえば街中のクリー
ニング工場において操業しながらテトラクロロエチレン
に汚染された敷地の土壌浄化を実施することが可能であ
る。また平常時のメンテナンスは、中和剤の補給のみで
あるので省力化することが出来る。EFFECTS OF THE INVENTION Volatile organic halogen compounds which are rendered harmless in the present invention include tetrachloroethylene, trichloroethylene, 1.2-dichloroethylene, chloroethylene, carbon tetrachloride, chloroform, methylene chloride, and 1.
1.1-trichloroethane, 1.2-dichloroethane,
Examples thereof include methylene bromide and methyl bromide. Since the apparatus according to the present invention can be easily made compact due to its structure, it requires a small installation area. For example, it is possible to carry out soil purification on a site contaminated with tetrachlorethylene while operating in a cleaning plant in the city. Further, since maintenance in normal times is only replenishment of the neutralizing agent, labor can be saved.
【00011】[00011]
【実施例】本発明では、汚染物質の種類および濃度によ
って好適な回収濃縮部と放電部の組み合わせが選択され
る。その例を表−1に示す。
EXAMPLES In the present invention, a suitable combination of the collecting and concentrating section and the discharging section is selected according to the kind and concentration of the pollutant. An example is shown in Table-1.
【0012】[0012]
【発明の効果】本発明によれば、汚染物質を同一装置内
で回収−無害化処理ができ、小型化によって小規模な場
面に適合し、かつメンテナンスも最小限に止めることが
出来るので省力化、コスト削減に寄与する効果が大であ
る。According to the present invention, the pollutants can be collected and detoxified in the same apparatus, the miniaturization can be adapted to a small-scale scene, and the maintenance can be minimized. The effect of contributing to cost reduction is great.
Claims (6)
糸膜あるいは活性炭によって回収濃縮し、放電部によっ
て分解し、ついで生成した無機ハロゲンをアルカリ性物
質で中和処理する連続した空気の浄化方法。1. A continuous air purification method in which a volatile organic halogen compound in the air is recovered and concentrated by a hollow fiber membrane or activated carbon, decomposed by a discharge part, and then the produced inorganic halogen is neutralized with an alkaline substance.
1の浄化方法。2. The purification method according to claim 1, wherein the material of the hollow fiber membrane is silicone.
化方法3. The purification method according to claim 1, wherein the activated carbon is an air heat regeneration type.
方法。4. The cleaning method according to claim 1, wherein the discharge part is a silent discharge type.
方法。5. The purification method according to claim 1, wherein the discharge part is a creeping discharge type.
ルシウム、水酸化カルシウムまたはソーダライムである
請求項1の浄化方法。6. The purification method according to claim 1, wherein the alkaline substance is sodium carbonate, calcium carbonate, calcium hydroxide or soda lime.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001245794A JP2003019420A (en) | 2001-07-09 | 2001-07-09 | Method for cleaning volatile organic halogen compound- containing air |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001245794A JP2003019420A (en) | 2001-07-09 | 2001-07-09 | Method for cleaning volatile organic halogen compound- containing air |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2003019420A true JP2003019420A (en) | 2003-01-21 |
Family
ID=19075474
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2001245794A Pending JP2003019420A (en) | 2001-07-09 | 2001-07-09 | Method for cleaning volatile organic halogen compound- containing air |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2003019420A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011220915A (en) * | 2010-04-13 | 2011-11-04 | Shimadzu Corp | Air purifier and total organic carbon measuring device using the same |
-
2001
- 2001-07-09 JP JP2001245794A patent/JP2003019420A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011220915A (en) * | 2010-04-13 | 2011-11-04 | Shimadzu Corp | Air purifier and total organic carbon measuring device using the same |
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