Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0438430B2 - - Google Patents
[go: Go Back, main page]

JPH0438430B2 - - Google Patents

Info

Publication number
JPH0438430B2
JPH0438430B2 JP63092969A JP9296988A JPH0438430B2 JP H0438430 B2 JPH0438430 B2 JP H0438430B2 JP 63092969 A JP63092969 A JP 63092969A JP 9296988 A JP9296988 A JP 9296988A JP H0438430 B2 JPH0438430 B2 JP H0438430B2
Authority
JP
Japan
Prior art keywords
filter
holes
deodorizing
small
layered
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.)
Expired - Lifetime
Application number
JP63092969A
Other languages
Japanese (ja)
Other versions
JPH01265966A (en
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 filed Critical
Priority to JP63092969A priority Critical patent/JPH01265966A/en
Publication of JPH01265966A publication Critical patent/JPH01265966A/en
Publication of JPH0438430B2 publication Critical patent/JPH0438430B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Disinfection, Sterilisation Or Deodorisation Of Air (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

〔産業上の利用分野〕 本発明は、脱臭作用を営む微生物あるいは酵素
を利用して悪臭気体中の悪臭成分を処理するため
に用いる脱臭フイルターに関する。 〔従来の技術〕 し尿処理場、下水処理場、廃棄物処理場、と殺
場、食品工場、魚腸骨処理場、養豚場、養鶏場、
パルプ製造工場等では悪臭が問題となる。 そして、かかる悪臭成分としては、一般にアン
モニア、硫化水素、硫化メチル、メルカプタン、
アミン類が主成分で、いずれもその成分中にアン
モニアやアミン類のように窒素原子が、又一方に
は硫化水素、硫化メチル、メルカプタンのように
硫黄原子が含まれている。 これらの悪臭成分を除去する脱臭方法として
は、従来、燃焼法、活性炭吸着法、洗浄法等が知
られているが、近年、微生物を用いた生物学的脱
臭法が、ランニングコストが低い等の利点を有す
るために注目されてきており、その装置の開発が
進められている。 例えば、特開昭57−200158号公報のように好気
性細菌の生化学的反応を利用したものが提案され
ている。この方法は、アンモニア、硫化水素、硫
化メチル、メルカプタン、アミン類等を含有する
悪臭気体を、好気性細菌群を含む培養液と気液接
触させることによつて悪臭気体から悪臭成分をこ
れら細菌群と酵素によつて酸化、還元させて悪臭
成分を無臭化することを内容とするものである。 ところが、前記気液接触の例として充填部とあ
るだけでその具体例は示されていない。また、特
開昭59−98717号公報では、充填物として木材チ
ツプ等の成型品や、アセテート不織布、グラスウ
ール、アスベスト、素焼き、木クズ、合成樹脂等
の多孔質成型品からなる球状及び円筒状にした直
径10mm〜35mmのもの、又は厚さ10mm〜35mmの板状
のものが示されており、特開昭62−7425号公報で
は、充填物として、木材、多孔質の石、素焼又は
合成樹脂製の一辺の長さが5mm〜50mmの大きさの
板状もしくは球状体からなるものが示されている
が、かかる充填物を用いたときに気液接触を行う
ための流路の確保などは充分とはいえなかつた。 また、特開昭61−271017号公報では、水または
栄養塩水からなるガス吸収液を悪臭気体に噴霧・
接触させて悪臭成分を溶解吸収させた後に、吸収
液と固定化微生物とを接触させて無臭化させるも
のが提案されているが、噴霧液による気液接触
は、処理ガスの量や噴霧に使用する液量などで難
点があるとともに、吸収液の循環利用の際には一
度吸収した悪臭成分を放出する危険がある。 一方、特開昭62−221354号公報では、貫通小孔
を多数有する紙製フイルターに悪臭作用を営む微
生物液等を含浸させ、このフイルターをカセツト
体として悪臭空気流路に配設するものが提案され
ている。 その具体例としては該カセツト体は段ボール紙
を中の波形紙で形成される貫通小孔がすべて同一
方向に並ぶように複数枚積層させてブロツク状と
したものであり、このブロツク状の紙製フイルタ
ーのカセツト体に脱臭作用を営む細菌の酵素液あ
るいは酵素液と菌液からなる液を含浸させて悪臭
空気路に配設している。 〔発明が解決しようとする課題〕 この特開昭62−221354号公報のものでは、貫通
小孔は直線状の流路であり悪臭空気はこの小孔の
数だけ分散されてある程度の気液接触は得られる
が、処理ガス量が増大した場合などには脱臭効率
の点などで充分とはいえず、脱臭効率を向上させ
るためには多数のカセツト体を必要とし、その結
果装置全体が大型化してしまう欠点もある。 本発明の目的は前記従来例の不都合を解消し、
効果的に気液接触を行うことができ、脱臭効率が
良好な脱臭フイルターを提供することにある。 〔課題を解消するための手段〕 本発明は前記目的を達成するため、脱臭作用を
営む微生物あるいは酵素を付着又は含浸させて使
用する脱臭フイルターにおいて、該フイルターは
段ボールを多数積層させて貫通小孔群を有したも
のをブロツク状のフイルター層状部材とし、この
貫通小孔群をもつフイルターの層状部材が貫通方
向に複数個層状に重ねられてなるとともに、その
隣接したフイルター層状部材間の前記貫通小孔群
の各小孔位置がずれを生じて組合わされることを
要旨とするものである。 〔作用〕 本発明によれば、悪臭空気は流路中で段ボール
製フイルターにぶつかり、フイルターの貫通小孔
内に分散して入り込む。このフイルターは、貫通
小孔群層が幾重にも重なつて組み込まれており、
各層の小孔位置がずれているため、小孔内に入り
込んだ悪臭空気は常に各層入口で小孔縁にぶつか
り、次の小孔群層へ分散して入り込む。そして悪
臭空気の流れは常に乱気流と化して小孔壁に接触
することになり、ここで悪臭作用を営む微生物と
接触して脱臭される。 また、フイルターは、カセツト体として簡単に
交換可能であり、紙製なので使用済みのものは堆
肥化するか乾燥後燃焼で楽に廃棄できる。 〔実施例〕 以下、本発明の実施例を詳細に説明する。 まず、フイルターの全体構造から先に説明する
と、フイルター1は、段ボール2の波形紙による
中しん2bで形成されてなる貫通小孔2aがすべ
て同一方向に並ぶように多数積層させてブロツク
体とし、このブロツク状のものをフイルター層状
部材3とする。そして、このフイルター層状部材
3を貫通小孔2aの方向が等しくなるように重ね
合わせたものである。ここで、フイルター層状部
材3の層厚さb(貫通小孔の長さ)は20mm〜250mm
程度が好ましい。 第1a図は本発明の脱臭フイルターの第1実施
例を示す分解斜視図、第1b図は同上斜視図で、
このようにしてフイルター層状部材3を重ね合わ
せる場合に本実施例では、1つおきにフイルター
層状部材3を裏返して裏表を交互に重ね合わせる
ようにした。 前記中しん2bは正弦波に近い波形紙によるも
のであるが、貫通小孔2a群はその小孔の位置が
ずれて組合わされることになる。 第2a図、第2b図は本発明の第2実施例を示
すもので、フイルター層状部材3を重ね合わせる
場合に、中しん2bの連続方向、すなわち段ボー
ルの積層方向が直交するように重ね合わせた。 このようにした場合中しん2bの山の向きは
90°相違することになり、貫通小孔2a群もその
小孔の位置がずれて組合わされることになる。 さらに、第3実施例として第3a図、第3b図
に示すようにフイルター層状部材3の端縁におけ
る中しん2bの切口をわずかにずらすことにより
該フイルター層状部材3を重ね合わせる場合に中
しん2bの山頂がわずかにずれるようにしてもよ
い。 この場合、前記第1実施例とほぼ同様のものが
得られるが、中しん2bの波の山頂は完全に交互
に逆になり半ピツチずつにずれるものでなく、半
ピツチ以下にずれていくものである。 また、段ボールの段の高さの種類には、段の高
さが4.8mm程度のAフルートと称するもの、段の
高さが2.5mm程度のBフルートと称するもの、段
の高さが3.7mm程度のCフルートと称するもの、
および段の高さが1.2mm程度のEフルートと称す
るものがある。 そこで、第4a図、第4b図に示すように第4
実施例として合わせるフイルター層状部材3は貫
通小孔2aの大きさが異なるものとした。このよ
うにすれば貫通小孔2aは大小のものが組合わせ
られ、位置がずれることになる。 一方、前記第1〜第4実施例ではすべてフイル
ター層状部材3は段ボール2の積層が平行する場
合について説明したが、第5a図、第5b図に示
すように段ボール2を渦巻状にして積層させて作
られるフイルターの層状部材3を、前記第1〜第
4実施例に示したような方法で重ね合せ、円柱形
のフイルター1を形成してもよい。 このような段ボール製フイルター1に脱臭作用
を営む微生物液あるいは酵素液を付着又は含浸さ
せるのであるが、かかる微生物液の付着又は含浸
方法は微生物を液体培地で培養させた溶液を直接
用いるか、又は固体培地で培養した培養物を水に
溶解させて、噴霧あるいは浸漬にて含浸させる。 脱臭作用を営む微生物としては、セルロース分
解菌、糸状菌、硫化菌、空中窒素固定化細菌、根
粒菌、硫黄菌、放線菌、酵母、シウドモナス菌の
中から選ばれたものが該当し、必要に応じて複数
の微生物を混合したりしてもよい。 このようにして、前記脱臭作用を営む微生物を
含浸させた段ボール製フイルター1は、それ単
独、もしくは枠体などと組合わされてカセツト体
として、悪臭空気路に貫通小孔2aが空気の流れ
方向に向くように配設され、悪臭空気を通過させ
る。 その際、悪臭空気は流路中で段ボール製フイル
ター1にぶつかり、フイルター1の貫通小孔2a
内に分散して入り込む。このフイルター1は、貫
通小孔2a群層が幾重にも重なつて組み込まれて
おり、各層の小孔2a位置がずれているため、小
孔2a内に入り込んだ悪臭空気は常に各層入口で
小孔縁にぶつかり、次の小孔2a群層へ分散して
入り込む。そして悪臭空気の流れは、常に乱気流
と化して小孔壁に接触することになり,ここで脱
臭作用を営む微生物と接触して脱臭される。 一方、使用済みのフイルター1は、これを燃焼
させるか堆肥化すれば簡単に処分できる。 次に、本発明におけるフイルターの脱臭性能に
ついての試験を第6図に示すような試験装置によ
り行つたので、その結果を示す。 第6図中4は脱臭塔カラム、5はH2Sガスボ
ンベである。 試験 1 脱臭塔カラム 100mmφ×500mm 使用フイルター (1) Bフルートの片面段ボールを渦巻状に積層し
て100mmφ×200mmとしたフイルター。 (2) Bフルートの片面段ボールを渦巻状に積層し
て100mmφ×100mmとしたフイルター層状部材を
2個重ね合わせたフイルター。 (3) Bフルートの片面段ボールを渦巻状に積層し
て、100mmφ×50mmとし、このフイルター層状
部材を4個重ね合わせたフイルター。 (4) Bフルートの片面段ボールを渦巻状に積層し
て、100mmφ×25mmとし、このフイルター層状
部材を8個重ね合わせたフイルター。 フイルターの設置位置 脱臭塔カラム中央(カラム底部より150mmの
位置) 使用微生物 硫黄細菌を主体とするもの 補充する水量130g/日(フイルターが乾燥し
ない程度の水量) 悪臭気体送入量 8.12/min 悪臭気体流速2.0cm/s(フイルターとの接触時
間10s) 悪臭気体の脱臭カラム入口濃度 5ppmH2
(一定)の条件で30日間実験を行つた結果を下記
第1表に示す。
[Industrial Field of Application] The present invention relates to a deodorizing filter used to treat malodorous components in malodorous gases using microorganisms or enzymes that perform deodorizing action. [Conventional technology] Human waste treatment plants, sewage treatment plants, waste treatment plants, slaughterhouses, food factories, fish iliac treatment plants, pig farms, poultry farms,
Odors are a problem in pulp manufacturing plants. Such malodorous components generally include ammonia, hydrogen sulfide, methyl sulfide, mercaptan,
The main component is amines, and all of them contain nitrogen atoms as in ammonia and amines, and sulfur atoms as in hydrogen sulfide, methyl sulfide, and mercaptans. Conventionally, combustion methods, activated carbon adsorption methods, cleaning methods, etc. have been known as deodorization methods to remove these malodorous components, but in recent years, biological deodorization methods using microorganisms have become popular due to their low running costs, etc. It has attracted attention because of its advantages, and the development of such devices is progressing. For example, methods utilizing the biochemical reactions of aerobic bacteria have been proposed, as in Japanese Patent Application Laid-Open No. 57-200158. This method removes malodorous components from the malodorous gas by bringing the malodorous gas containing ammonia, hydrogen sulfide, methyl sulfide, mercaptan, amines, etc. into gas-liquid contact with a culture medium containing aerobic bacteria. The content is to make malodorous components odorless by oxidizing and reducing them with enzymes. However, as an example of the gas-liquid contact, a filling section is mentioned, but no specific example thereof is given. In addition, in JP-A No. 59-98717, the filler is made of molded products such as wood chips, or porous molded products such as acetate non-woven fabric, glass wool, asbestos, unglazed ceramics, wood chips, synthetic resin, etc. in spherical and cylindrical shapes. JP-A No. 62-7425 discloses that the filling material is wood, porous stone, unglazed or synthetic resin. There is a planar or spherical body with a side length of 5 mm to 50 mm, but it is difficult to secure a flow path for gas-liquid contact when using such a filler. It wasn't enough. Furthermore, in Japanese Patent Application Laid-Open No. 61-271017, a gas absorbing liquid consisting of water or nutrient salt water is sprayed onto malodorous gases.
It has been proposed to bring the absorbent solution into contact with immobilized microorganisms after dissolving and absorbing malodorous components to make them odorless. There are problems with the amount of liquid used, and when the absorbing liquid is recycled, there is a risk of releasing malodorous components that have been absorbed. On the other hand, Japanese Patent Application Laid-open No. 62-221354 proposes impregnating a paper filter with a large number of small through holes with a microorganism liquid that causes malodor, and disposing this filter as a cassette in a malodorous air flow path. has been done. As a specific example, the cassette body is made into a block shape by stacking a plurality of sheets of corrugated paper so that the small through holes formed by the corrugated paper inside are all lined up in the same direction. The cassette body of the filter is impregnated with a bacterial enzyme solution or a solution consisting of an enzyme solution and a bacterial solution that performs a deodorizing action, and is placed in the foul-smelling air path. [Problems to be Solved by the Invention] In the device disclosed in JP-A No. 62-221354, the small through holes are linear flow paths, and the foul-smelling air is dispersed by the number of small holes, and a certain amount of gas-liquid contact is achieved. However, when the amount of gas to be processed increases, the deodorizing efficiency is not sufficient, and in order to improve the deodorizing efficiency, a large number of cassettes are required, resulting in an increase in the size of the entire device. There are some disadvantages as well. The purpose of the present invention is to eliminate the disadvantages of the conventional example,
It is an object of the present invention to provide a deodorizing filter that can effectively carry out gas-liquid contact and has good deodorizing efficiency. [Means for Solving the Problems] In order to achieve the above object, the present invention provides a deodorizing filter to which microorganisms or enzymes that perform a deodorizing action are attached or impregnated. A filter layered member having a group of through holes is a block-shaped filter layered member, and a plurality of filter layered members having this through hole group are stacked in a layered manner in the penetration direction, and the through holes between adjacent filter layered members are The gist is that the positions of the small holes in the hole group are combined with deviations. [Function] According to the present invention, malodorous air collides with the cardboard filter in the flow path and disperses into the small through holes of the filter. This filter is built with multiple layers of through-holes,
Since the positions of the pores in each layer are shifted, the foul-smelling air that enters the pores always collides with the pore edges at the entrance of each layer, and then disperses and enters the next layer of pores. The flow of malodorous air always becomes turbulent and comes into contact with the pore walls, where it comes into contact with malodor-producing microorganisms and is deodorized. Furthermore, the filter can be easily replaced as a cassette, and since it is made of paper, used filters can be easily disposed of by composting or drying and burning. [Examples] Examples of the present invention will be described in detail below. First, the overall structure of the filter will be explained. The filter 1 is made into a block body by stacking a large number of through holes 2a formed by the corrugated paper core 2b of the corrugated cardboard 2 so that they are all lined up in the same direction. This block-like member is referred to as a filter layer member 3. The filter layered members 3 are stacked one on top of the other so that the directions of the small through holes 2a are the same. Here, the layer thickness b (length of the small through hole) of the filter layered member 3 is 20 mm to 250 mm.
degree is preferred. FIG. 1a is an exploded perspective view showing a first embodiment of the deodorizing filter of the present invention, and FIG. 1b is a perspective view of the same.
In the case where the filter layered members 3 are stacked in this manner, in this embodiment, every other filter layered member 3 is turned over so that the front and back sides are stacked alternately. Although the medium 2b is made of corrugated paper with a nearly sinusoidal waveform, the groups of through holes 2a are combined with the positions of the holes shifted. Figures 2a and 2b show a second embodiment of the present invention, in which the filter layered members 3 are stacked so that the continuous direction of the corrugated cardboard 2b, that is, the stacking direction of the corrugated cardboard, is perpendicular to each other. . In this case, the direction of the mountain of core 2b is
This results in a 90° difference, and the through holes 2a group are also combined with the positions of the holes shifted. Furthermore, as a third embodiment, as shown in FIGS. 3a and 3b, by slightly shifting the cuts of the inserts 2b at the edges of the filter layered members 3, when the filter layered members 3 are overlapped, the inserts 2b The top of the mountain may be slightly shifted. In this case, almost the same thing as in the first embodiment is obtained, but the crests of the waves in the middle 2b are completely reversed alternately and do not shift by half a pitch, but shift by less than half a pitch. It is. In addition, the types of corrugated cardboard corrugation heights include A flute, which has a corrugated height of approximately 4.8 mm, B flute, which has a corrugated height of approximately 2.5 mm, and B flute, which has a corrugated height of approximately 3.7 mm. What is called a degree C flute,
There is also a flute called E flute with a flute height of about 1.2 mm. Therefore, as shown in Figures 4a and 4b, the fourth
As an example, the filter layered members 3 to be combined have different sizes of small through holes 2a. In this way, the small and large through holes 2a are combined, and the positions of the small through holes 2a are shifted. On the other hand, in all of the first to fourth embodiments, the filter layered member 3 has been described in which the cardboards 2 are stacked in parallel, but as shown in FIGS. 5a and 5b, the cardboards 2 are stacked in a spiral shape. The cylindrical filter 1 may be formed by stacking the layered members 3 of the filter made in the same manner as shown in the first to fourth embodiments. Such a cardboard filter 1 is attached to or impregnated with a microbial solution or an enzyme solution that performs a deodorizing action. A culture cultured in a solid medium is dissolved in water and impregnated by spraying or immersion. Microorganisms that carry out the deodorizing action include those selected from cellulose-degrading bacteria, filamentous fungi, sulfur bacteria, air nitrogen-fixing bacteria, rhizobia, sulfur bacteria, actinomycetes, yeast, and pseudomonas bacteria. Depending on the situation, a plurality of microorganisms may be mixed. In this way, the cardboard filter 1 impregnated with the microorganisms that perform the deodorizing action can be used alone or in combination with a frame etc. to form a cassette body, with small through holes 2a arranged in the odor air path in the direction of air flow. It is placed so that foul-smelling air can pass through. At that time, the foul-smelling air hits the cardboard filter 1 in the flow path, and the small through hole 2a of the filter 1
Disperse and enter within. This filter 1 is built with multiple layers of through-holes 2a, and the positions of the holes 2a in each layer are shifted, so the foul-smelling air that has entered the holes 2a is always small at the entrance of each layer. It collides with the pore edge and disperses into the next layer of small pores 2a group. The flow of foul-smelling air always becomes turbulent and comes into contact with the walls of the pores, where it comes into contact with the microorganisms that carry out the deodorizing action and is deodorized. On the other hand, the used filter 1 can be easily disposed of by burning it or composting it. Next, a test on the deodorizing performance of the filter of the present invention was conducted using a testing apparatus as shown in FIG. 6, and the results are shown below. In FIG. 6, 4 is a deodorizing column, and 5 is a H 2 S gas cylinder. Test 1 Deodorizing tower column 100mmφ x 500mm Filter used (1) A 100mmφ x 200mm filter made by stacking B flute single-sided cardboard in a spiral shape. (2) A filter made by stacking two B-flute single-sided corrugated cardboard layers stacked in a spiral shape, each measuring 100mmφ x 100mm. (3) A filter made by laminating B-flute single-sided corrugated cardboard in a spiral shape to a size of 100mmφ x 50mm, and stacking four of these filter layered members. (4) A filter made by laminating B-flute single-sided cardboard in a spiral shape to a size of 100 mmφ x 25 mm, and stacking 8 of these filter layered members. Filter installation location Center of deodorizing tower column (150mm from the bottom of the column) Microorganisms used Mainly sulfur bacteria Amount of water to be replenished 130g/day (amount of water that does not dry the filter) Amount of malodorous gas fed 8.12/min Malodorous gas Flow rate 2.0cm/s (contact time with filter 10s) Deodorizing column inlet concentration of malodorous gas 5ppmH 2 S
The results of an experiment conducted under (constant) conditions for 30 days are shown in Table 1 below.

【表】 試験 2 脱臭塔カラム 100mmφ×500mm 使用フイルター (1) Bフルートの片面段ボールを渦巻状に積層し
て100mmφ×25mmとし、このフイルター層状部
材を8個重ね合わせたフイルター。 (2) Bフルートの片面段ボールを渦巻状に積層し
て100mmφ×25mmとし、このフイルター層状部
材6個と、Eフルートの片面段ボールを渦巻状
に積層して100mmφ×25mmとし、このフイルタ
ー層状部材2個とを、BBEBBEBBの形に重ね
合わせたフイルター。 (3) BフルートおよびEフルートとからなる100
mmφ×25mmのフイルター層状部材をそれぞれ4
個ずつ用い、BEBEBEBEの形に重ね合わせた
フイルター。 フイルターの設置位置 脱臭塔カラム中央(カラム底部より150mmの
位置) 使用微生物 硫黄細菌を主体とするもの 補充する水量130g/日(フイルターが乾燥し
ない程度の水量) 悪臭気体送入量 8.12/min 悪臭気体流速2.0cm/s(フイルターとの接触時
間10s) 悪臭気体の脱臭カラム入口濃度 5ppmH2
(一定)の条件で30日間実験を行つた結果を下記
第2表に示す。
[Table] Test 2 Deodorizing tower column 100mmφ x 500mm Filter used (1) A filter made by stacking B flute single-sided cardboard in a spiral shape to a size of 100mmφ x 25mm, and stacking 8 of these filter layered members. (2) B-flute single-sided cardboard is stacked in a spiral shape to make 100mmφ x 25mm, six filter layered members and E-flute single-sided cardboard are stacked in a spiral shape to make 100mmφ×25mm, and this filter layered member 2 A filter that overlaps individual pieces in the shape of BBEBBEBB. (3) 100 consisting of B flute and E flute
4 mmφ×25mm filter layer members each
Filters are used individually and stacked in the shape of BEBEBEBE. Filter installation location Center of deodorizing tower column (150mm from the bottom of the column) Microorganisms used Mainly sulfur bacteria Amount of water to be replenished 130g/day (amount of water that does not dry the filter) Amount of malodorous gas fed 8.12/min Malodorous gas Flow rate 2.0cm/s (contact time with filter 10s) Deodorizing column inlet concentration of malodorous gas 5ppmH 2 S
The results of an experiment conducted under (constant) conditions for 30 days are shown in Table 2 below.

〔発明の効果〕〔Effect of the invention〕

以上述べたように、本発明の脱臭フイルター
は、脱臭作用を営む微生物あるいは酵素によつて
悪臭成分を除去する紙製フイルターにおいて、該
フイルターを段ボールで構成した場合に、フイル
ターを通過する悪臭空気の流れを常に乱気流化す
ることができ、その結果、効果的に気液接触を生
じさせ、効率的に脱臭作業が実現できる。
As described above, the deodorizing filter of the present invention is a paper filter that removes malodorous components using microorganisms or enzymes that perform a deodorizing action. The flow can always be made turbulent, resulting in effective gas-liquid contact and efficient deodorization.

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

第1a図は本発明の脱臭フイルターの第1実施
例を示す分解斜視図、第1b図は同上組立状態の
斜視図、第2a図は第2実施例を示す分解斜視
図、第2b図は同上組立状態の斜視図、第3a図
は第3実施例を示す分解斜視図、第3b図は同上
組立状態の斜視図、第4a図は第4実施例を示す
分解斜視図、第4b図は同上組立状態の斜視図、
第5a図は第5実施例を示す分解斜視図、第5b
図は同上組立状態の斜視図、第6図は試験を行う
ために用いた装置の説明図である。 1……フイルター、2……段ボール、2a……
貫通小孔、2b……中しん、3……フイルター層
状部材、4……脱臭塔カラム、5……H2Sガス
ボンベ。
Fig. 1a is an exploded perspective view showing the first embodiment of the deodorizing filter of the present invention, Fig. 1b is a perspective view of the same in the assembled state, Fig. 2a is an exploded perspective view showing the second embodiment, and Fig. 2b is the same as the above. Figure 3a is an exploded perspective view showing the third embodiment; Figure 3b is a perspective view of the same assembled state; Figure 4a is an exploded perspective view showing the fourth embodiment; Figure 4b is the same as the above. A perspective view of the assembled state,
Fig. 5a is an exploded perspective view showing the fifth embodiment; Fig. 5b is an exploded perspective view showing the fifth embodiment;
The figure is a perspective view of the assembled state of the same as above, and FIG. 6 is an explanatory view of the apparatus used for conducting the test. 1...Filter, 2...Cardboard, 2a...
Small through hole, 2b...Inner core, 3...Filter layered member, 4...Deodorizing column, 5... H2S gas cylinder.

Claims (1)

【特許請求の範囲】 1 脱臭作用を営む微生物あるいは酵素を付着又
は含浸させて使用する脱臭フイルターにおいて、
該フイルターは段ボールを多数積層させて貫通小
孔群を有したものをブロツク状のフイルター層状
部材とし、この貫通小孔群をもつフイルターの層
状部材が貫通方向に複数個層状に重ねられてなる
とともに、その隣接したフイルター層状部材間の
前記貫通小孔群の各小孔位置がずれを生じて組合
わされることを特徴とした脱臭フイルター。 2 貫通小孔群の各小孔位置のずれは、段ボール
の積層方向を隣接するフイルター層状部材間で直
交させて形成される請求項第1項記載の脱臭フイ
ルター。 3 貫通小孔群の各小孔位置のずれは、フイルタ
ー層状部材の貫通小孔の小孔の大きさが異なるも
のを重ねて形成される請求項第1項記載の脱臭フ
イルター。
[Scope of Claims] 1. A deodorizing filter attached or impregnated with microorganisms or enzymes that perform a deodorizing action,
The filter is made of a block-shaped filter layered member made by laminating a large number of cardboard boxes and having a group of through holes, and a plurality of filter layered members having the through hole groups are stacked in a layered manner in the penetration direction. A deodorizing filter, characterized in that the positions of the small holes in the group of through holes between adjacent filter layer members are offset from each other when combined. 2. The deodorizing filter according to claim 1, wherein the positional deviation of each small hole in the group of through holes is made such that the stacking direction of the cardboard is orthogonal to the adjacent filter layer members. 3. The deodorizing filter according to claim 1, wherein the deviation in the position of each small hole in the group of through holes is formed by overlapping the small through holes of different sizes in the filter layered member.
JP63092969A 1988-04-15 1988-04-15 Deodorizing filter Granted JPH01265966A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63092969A JPH01265966A (en) 1988-04-15 1988-04-15 Deodorizing filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63092969A JPH01265966A (en) 1988-04-15 1988-04-15 Deodorizing filter

Publications (2)

Publication Number Publication Date
JPH01265966A JPH01265966A (en) 1989-10-24
JPH0438430B2 true JPH0438430B2 (en) 1992-06-24

Family

ID=14069242

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63092969A Granted JPH01265966A (en) 1988-04-15 1988-04-15 Deodorizing filter

Country Status (1)

Country Link
JP (1) JPH01265966A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4908876B2 (en) * 2006-02-27 2012-04-04 三洋電機株式会社 Air sanitizer

Also Published As

Publication number Publication date
JPH01265966A (en) 1989-10-24

Similar Documents

Publication Publication Date Title
Van Groenestijn et al. Recent developments in biological waste gas purification in Europe
US6403366B1 (en) Method and apparatus for treating volatile organic compounds, odors, and biogradable aerosol/particulates in air emissions
US20060027099A1 (en) Method and system for treating contaminants and odors in airborne emissions
JPH11169654A (en) Circulation type microbial deodorization apparatus
CN102091599A (en) Biomass adsorbent and preparation method thereof
CN1015693B (en) Apparatus for deodorisation
CN101112673A (en) Biological deodorization filler and preparation method thereof
RU197539U1 (en) MODULAR BIOFILTER FOR CLEANING GASES
JPH0438430B2 (en)
KR100371501B1 (en) Biofilter for purification of waste gas
JPH046409B2 (en)
KR101816518B1 (en) Package odor removal system
Baltrėnas et al. Removal of ammonia by biofilters with straight and wavy lamellar plates
CN220047707U (en) Biological SOx/NOx control dust collector of flue gas
JPH0790143B2 (en) Microbial filter for use in deodorizers, etc.
US20010053546A1 (en) Biological filter structures
JPH0441928Y2 (en)
CN102688670A (en) Method and system for processing bad smell
JP2000033229A (en) Deodorization of sulfur based offensive odor gas
JPH0534746Y2 (en)
RU2761898C2 (en) Mobile biofilter mbf
CN223570420U (en) Biological filter deodorizing device of institutional advancement type
KR20210064882A (en) System and method for reducing offensive odor from organic waste using micro-organism
CN121082104A (en) Multistage biological deodorization system in two fungus district
JPH0435208B2 (en)