JPH0777601B2 - Method for removing adhered microorganisms - Google Patents
Method for removing adhered microorganismsInfo
- Publication number
- JPH0777601B2 JPH0777601B2 JP2284364A JP28436490A JPH0777601B2 JP H0777601 B2 JPH0777601 B2 JP H0777601B2 JP 2284364 A JP2284364 A JP 2284364A JP 28436490 A JP28436490 A JP 28436490A JP H0777601 B2 JPH0777601 B2 JP H0777601B2
- Authority
- JP
- Japan
- Prior art keywords
- microorganisms
- gas
- packed bed
- tower
- water
- 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
Links
- 244000005700 microbiome Species 0.000 title claims description 27
- 238000000034 method Methods 0.000 title claims description 13
- 239000007788 liquid Substances 0.000 claims description 24
- 239000000463 material Substances 0.000 claims description 11
- 230000001877 deodorizing effect Effects 0.000 claims description 9
- 238000012856 packing Methods 0.000 claims description 7
- 239000007789 gas Substances 0.000 description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 22
- 239000000945 filler Substances 0.000 description 14
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 9
- 238000002474 experimental method Methods 0.000 description 8
- 239000012530 fluid Substances 0.000 description 8
- DWAQJAXMDSEUJJ-UHFFFAOYSA-M Sodium bisulfite Chemical compound [Na+].OS([O-])=O DWAQJAXMDSEUJJ-UHFFFAOYSA-M 0.000 description 7
- 235000010267 sodium hydrogen sulphite Nutrition 0.000 description 7
- 239000003638 chemical reducing agent Substances 0.000 description 6
- 241000894006 Bacteria Species 0.000 description 4
- 238000001816 cooling Methods 0.000 description 4
- 235000014113 dietary fatty acids Nutrition 0.000 description 4
- 229930195729 fatty acid Natural products 0.000 description 4
- 239000000194 fatty acid Substances 0.000 description 4
- 150000004665 fatty acids Chemical class 0.000 description 4
- 238000005406 washing Methods 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- -1 acetic acid Chemical class 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 229920000642 polymer Polymers 0.000 description 3
- 235000011121 sodium hydroxide Nutrition 0.000 description 3
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 239000005708 Sodium hypochlorite Substances 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 229940079827 sodium hydrogen sulfite Drugs 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 239000002349 well water Substances 0.000 description 2
- 235000020681 well water Nutrition 0.000 description 2
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 229910019093 NaOCl Inorganic materials 0.000 description 1
- 102220474974 POTE ankyrin domain family member C_F28C_mutation Human genes 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 230000001464 adherent effect Effects 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 230000010261 cell growth Effects 0.000 description 1
- 238000009264 composting Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000003292 diminished effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004299 exfoliation Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 230000012010 growth Effects 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 239000008235 industrial water Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 239000003415 peat Substances 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Landscapes
- Treating Waste Gases (AREA)
- Gas Separation By Absorption (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、気液接触塔における付着微生物のはく離方法
に係り、特に、充填材を用いた悪臭ガスの脱臭塔又は高
温ガスの冷却塔における付着微生物のはく離方法に関す
るものである。Description: TECHNICAL FIELD The present invention relates to a method for removing adhered microorganisms in a gas-liquid contact tower, and more particularly in a deodorizing tower for malodorous gas using a packing material or a cooling tower for high temperature gas. The present invention relates to a method for removing adhered microorganisms.
〔従来の技術〕 アンモニアや硫化水素を含む悪臭ガスを、ピート等の市
販充填材やスポンジ充填材を用いて、生物学的に脱臭す
る方法においては、充填層の圧力損失はほとんど増大せ
ず、問題とならない。[Prior Art] A malodorous gas containing ammonia and hydrogen sulfide, using a commercially available filling material such as peat or a sponge filling material, in the method of biologically deodorizing, the pressure loss of the packed bed hardly increases, It doesn't matter.
しかしながら、上記の悪臭ガスに有機性ガス、例えば酢
酸のような揮発性脂肪酸が含まれると、充填層内で著し
く微生物が増殖し、圧力損失が増加する。However, when the above malodorous gas contains an organic gas, for example, a volatile fatty acid such as acetic acid, microorganisms significantly grow in the packed bed, resulting in an increase in pressure loss.
また、脱臭が主目的でなく、減温が目的のスクラバー方
式の冷却装置においても、流入する高温ガス(乾燥排ガ
スやコンポスト処理の排ガス)に揮発性脂肪酸等の有機
性ガスが含まれると、同様に充填層内に微生物が増殖し
圧力損失が増す。Also, even in a scrubber type cooling device whose purpose is to reduce temperature rather than deodorizing, the same applies when the inflowing high-temperature gas (dry exhaust gas or exhaust gas from composting treatment) contains organic gases such as volatile fatty acids. At the same time, microorganisms grow in the packed bed and pressure loss increases.
従来、このような場合は、充填材を系外に取り出し水流
などで機械的に付着微生物をはく離させたり、あるいは
充填材を充填した状態で次亜塩素酸ソーダまたは次亜塩
素酸ソーダと苛性ソーダを併用する薬品洗浄を実施して
いた。Conventionally, in such a case, the filler is taken out of the system to mechanically remove the adhering microorganisms with a water stream or the like, or sodium hypochlorite or sodium hypochlorite and caustic soda are filled with the filler. We were carrying out chemical cleaning to be used together.
前記したように、従来技術では次に示す問題を有してい
る。As described above, the related art has the following problems.
(1) 機械的はく離法では充填材の取り出し、洗浄、
再充填作業に手間がかかりかつ作業性が悪い。(1) In the mechanical peeling method, the filler is taken out, washed,
Refilling work is troublesome and workability is poor.
(2) 薬品洗浄法は危険な薬品を使用しなければなら
ず、使用後の廃液処理が必要である。(2) The chemical cleaning method requires the use of dangerous chemicals, and requires waste liquid treatment after use.
そこで、本発明は、気液接触塔の充填層の圧力損失の増
大を防ぐために、安全で効率よく充填層に付着する微生
物をはく離除去する方法を提供することを目的とする。Therefore, an object of the present invention is to provide a method for safely and efficiently peeling and removing microorganisms adhering to a packed bed in order to prevent an increase in pressure loss in the packed bed of a gas-liquid contact tower.
上記目的を達成するために、本発明では、微生物が付着
した充填材を充填した充填層を有する気液接触塔におい
て、該塔内又は充填層内を嫌気的条件にすることを特徴
とする付着微生物のはく離方法としたものである。In order to achieve the above object, in the present invention, in a gas-liquid contact column having a packed bed filled with a filler to which microorganisms are adhered, characterized in that the inside of the tower or the packed bed is anaerobic conditions This is a method for removing microorganisms.
上記の気液接触塔は、微生物による悪臭ガスの脱臭塔又
は高温ガスを減温するスクラバー塔が特に有効に適用す
ることができる。The above gas-liquid contact tower can be particularly effectively applied to a deodorizing tower for a malodorous gas caused by microorganisms or a scrubber tower for reducing the temperature of a high temperature gas.
本発明は、具体的には、脱臭塔あるいは冷却塔等の気液
接触塔に流入するガスを止めたのち、好ましくは装置内
を循環する液(以下循環液)に還元剤を加え、必要なら
加温することにより、充填層及び循環液を嫌気的状態に
することによって、充填材から付着性微生物をはく離さ
せ、除去するものである。Specifically, the present invention specifically stops a gas flowing into a gas-liquid contact tower such as a deodorizing tower or a cooling tower, and then preferably adds a reducing agent to the liquid circulating in the apparatus (hereinafter, circulating liquid), and if necessary, By heating, the packed bed and the circulating liquid are brought into an anaerobic state, so that the adherent microorganisms are peeled off from the packing material and removed.
以下に本発明を詳細に説明する。The present invention will be described in detail below.
本発明は悪臭ガスの生物学的脱臭装置や水洗浄装置及び
高温ガスの冷却装置等、いずれの気液接触装置において
も同一の方法でその充填材に付着する微生物をはく離さ
せることが可能である。INDUSTRIAL APPLICABILITY The present invention can remove microorganisms attached to the packing material by the same method in any gas-liquid contact device such as a biological deodorizing device for malodorous gas, a water cleaning device, and a cooling device for high temperature gas. .
まず、装置に流入するガスをしゃ断し、空気または酸素
の充填層への供給を停止させる。密閉状態で嫌気状態を
形成させるだけでもよいが、その後、循環液に還元剤を
添加し、循環液を嫌気状態とし、この循環液を微生物が
付着する充填層に供給することにより充填層全体をも嫌
気状態とすることができる。First, the gas flowing into the apparatus is shut off, and the supply of air or oxygen to the packed bed is stopped. Although it is only necessary to form an anaerobic state in a sealed state, after that, a reducing agent is added to the circulating liquid to make the circulating liquid anaerobic, and this circulating liquid is supplied to the packed bed on which microorganisms adhere to thereby make the entire packed bed. Can also be anaerobic.
循環液のpHは6〜8が良い。The pH of the circulating fluid is preferably 6-8.
公知のいずれの還元剤でも使用可能であるが、循環液の
pH低下が小さく安価な亜硫酸水素ナトリウムが特に望ま
しい。Although any known reducing agent can be used,
Particularly preferred is sodium bisulfite, which has a low pH drop and is inexpensive.
還元剤の添加量は通常、全循環液に対して1w/v%程度で
良い。酸化還元電位(ORP)で循環液の嫌気性を管理し
ても良い。循環液のORPを−50mV〜−300mV(内部液:飽
和KC1、比較電極:甘汞電極)に維持するように亜硫酸
水素ナトリウムを循環液に適宜、添加する。The amount of the reducing agent added is usually about 1 w / v% with respect to the total circulating fluid. The anaerobic properties of the circulating fluid may be controlled by the redox potential (ORP). Sodium bisulfite is appropriately added to the circulating liquid so as to maintain the ORP of the circulating liquid at −50 mV to −300 mV (internal liquid: saturated KC1, reference electrode: Amano electrode).
また、循環液を30℃〜50℃に加温することで、循環液お
よび充填層に付着する微生物に対して嫌気状態が促進さ
れる。Further, by heating the circulating liquid to 30 ° C to 50 ° C, the anaerobic state is promoted for the microorganisms adhering to the circulating liquid and the packed bed.
加温はヒーター等を使用しても良いが、充填層に散水す
るための循環ポンプを連続運転することが、循環液の水
温が上昇し、嫌気状態の促進に必要な温度の確保が可能
となる。A heater or the like may be used for heating, but continuous operation of the circulation pump for watering the packed bed increases the water temperature of the circulating liquid and makes it possible to secure the temperature required to promote the anaerobic state. Become.
系全体が嫌気状態になったことをORP等で確認後、循環
ポンプを停止する。水温が30℃以上では30分間、30℃未
満では1〜5時間程度そのままの状態にしておいた後、
循環水槽内の循環液を系外に排出するのと同時に充填層
の水洗浄を行う。井水、工業用水等のSSを含まない洗浄
水で充填層を洗浄し、はく離しやすくなった微生物の除
去を行う。はく離した微生物を含む洗浄水はすぐに系外
へ排出し、循環使用しない。After confirming that the whole system has become anaerobic by ORP etc., stop the circulation pump. If the water temperature is 30 ° C or higher, leave it for 30 minutes, and if it is lower than 30 ° C, leave it for 1 to 5 hours.
The circulating fluid in the circulating water tank is discharged to the outside of the system and at the same time, the packed bed is washed with water. The packed bed is washed with SS-free wash water such as well water and industrial water to remove microorganisms that have become easy to peel off. The wash water containing the separated microorganisms is immediately discharged to the outside of the system and is not reused.
次に、本発明についてその概略断面図を示した第1図で
説明する。Next, the present invention will be described with reference to FIG. 1 showing a schematic sectional view thereof.
原ガス流入管のダンパー1を閉とする。循環ポンプ8を
常時運転しつつ、循環水槽内10に還元剤として、亜硫酸
水素ナトリウムを全循環液量に対して1w/v%を添加す
る。The damper 1 of the raw gas inflow pipe is closed. While constantly operating the circulation pump 8, 1 w / v% of sodium bisulfite as a reducing agent is added to the circulating water tank 10 as a reducing agent.
その後、30分間程度循環ポンプを運転したのち、その運
転を停止する。循環液の温度が30℃以下なら循環ポンプ
を運転しつづけて循環液を加温する。ヒーター等で加温
することも可能である。After that, the circulation pump is operated for about 30 minutes and then stopped. If the temperature of the circulating fluid is 30 ° C or lower, continue operating the circulation pump to warm the circulating fluid. It is also possible to heat with a heater or the like.
循環ポンプを停止し、30分後に循環ポンプの吐出弁7を
閉、排水弁9を開、洗浄水ライン弁6を開として充填層
2を洗浄する。The circulation pump is stopped, and after 30 minutes, the discharge valve 7 of the circulation pump is closed, the drain valve 9 is opened, and the washing water line valve 6 is opened to wash the packed bed 2.
水洗浄は、洗浄排水にSSか認められなくなるまで連続し
て行う。水洗浄方式は一過性の押し出し水洗とする。Wash with water continuously until SS is no longer recognized in the wash drain. The water washing method is temporary extruded water washing.
充填層の圧力損失の上昇原因は、原ガス中の揮発性脂肪
酸等が従属栄養菌によって資化されることにより、その
菌が増殖するためである。従属栄養菌は基質当たりの菌
体増殖量が大きく、加えて粘性の高い菌体外ポリマーを
生成する。The cause of the increase in the pressure loss of the packed bed is that the volatile fatty acids and the like in the raw gas are assimilated by the heterotrophic bacteria and the bacteria grow. Heterotrophic bacteria have a large amount of microbial cell growth per substrate and, in addition, produce a highly viscous extracellular polymer.
好気状態下では、この菌体外ポリマーは強力に微生物と
充填材または微生物同士を結び付けているが、絶対嫌気
性下では酸素がなくて前記の従属栄養菌は活動できず、
菌体外ポリマーによる結合力が消失する。Under aerobic conditions, this extracellular polymer strongly binds the microorganisms to the packing material or the microorganisms, but under absolute anaerobic conditions, the heterotrophic bacteria cannot operate without oxygen,
The binding force of the extracellular polymer disappears.
このために、個々の微生物は微粒子状で粘着性の全くな
いサラサラした状態となり、自然に充填材表面からはく
離する。また、はく離した微生物は、充填材に再付着お
よび再捕捉されずに洗浄水の水流と共に系外へ排出され
る。For this reason, the individual microorganisms are in a fine particle-like and non-sticky state, and are naturally separated from the surface of the filler. Further, the separated microorganisms are discharged to the outside of the system together with the water flow of the washing water without being reattached to the packing material and re-captured.
以下に本発明を実施例により具体的に説明するが、本発
明はこの実施例に限定されない。The present invention will be specifically described below with reference to examples, but the present invention is not limited to these examples.
実施例1 汚泥乾燥機の乾燥排ガスを減温および脱臭処理する目的
で使用される減温塔から、採取した充填材ポリエチレン
(直径74mmテラレット商品名)を用いてスライム除去実
験を行った。Example 1 A slime removal experiment was conducted using a polyethylene filler (trade name: 74 mm in diameter 74 mm) collected from a temperature reducing tower used for the purpose of reducing the temperature and deodorizing the dry exhaust gas of a sludge dryer.
実験に用いた充填材へのスライム付着量は、0.5g−乾燥
SS/個−充填材であった。実験にはこの充填材10個を使
用した。The amount of slime attached to the filler used in the experiment was 0.5 g-dry
SS / piece-filler. Ten fillers were used in the experiment.
本発明では、4の密閉容器に充填材を入れて、1%亜
硫酸水素ナトリウム水溶液4を注入し、40℃で約8時
間放置した。In the present invention, the filling material was placed in a closed container 4 and 1% aqueous sodium hydrogen sulfite solution 4 was injected and left at 40 ° C. for about 8 hours.
従来法は、本発明の亜硫酸水素ナトリウム水溶液の代わ
りに、0.1%Cl2(NaOCl使用)および3%NaOHの混合液
4を注入し、開放系で40℃、8時間放置した。In the conventional method, a mixed solution 4 of 0.1% Cl 2 (using NaOCl) and 3% NaOH was poured in place of the aqueous sodium hydrogen sulfite solution of the present invention, and left at 40 ° C. for 8 hours in an open system.
8時間後、静かに充填材を取り出し、スライム付着量を
測定した。スライム除去量は、実験前の付着量から実験
後の付着量を差し引いて求めた。本発明におけるスライ
ム除去量は、0.48g−乾燥SS/個−充填材(平均値)、従
来法では0.4g−乾燥SS/個−充填材(平均値)であっ
た。After 8 hours, the filler was gently removed and the amount of slime adhered was measured. The slime removal amount was obtained by subtracting the adhesion amount after the experiment from the adhesion amount before the experiment. The amount of slime removed in the present invention was 0.48 g-dry SS / piece-filler (average value), and in the conventional method 0.4 g-dry SS / piece-filler (average value).
本発明によって充填材からはく離したスライムは、微粒
子状であった。The slime peeled from the filler according to the present invention was in the form of fine particles.
実施例2 充填材としてポリプロピレン(ハイレックス商品名)
(外径30mm)を1m充填し、主に揮発性脂肪酸を含む悪臭
ガスを生物学的に脱臭する脱臭装置(第1図)を用い
て、本発明による微生物のはく離実験を行った。Example 2 Polypropylene (Hilex brand name) as a filler
Using the deodorizing device (FIG. 1) which was filled with 1 m (outer diameter 30 mm) and biologically deodorizes malodorous gas containing mainly volatile fatty acids, the microbial exfoliation experiment according to the present invention was conducted.
原ガス流入管のダンパーを閉にした後、循環水槽(保有
水量約200)に亜硫酸水素ナトリウム2kgを添加した。
循環ポンプを運転し亜硫酸水素ナトリウムを含んだ循環
液を150/分で30分間、充填層に散水した。循環液のp
HはNaOHで6−8に調整した。水温は30℃であった。After closing the damper of the raw gas inflow pipe, 2 kg of sodium bisulfite was added to the circulating water tank (holding water amount about 200).
The circulating pump was operated and the circulating liquid containing sodium bisulfite was sprinkled on the packed bed at 150 / min for 30 minutes. Circulating fluid p
H was adjusted to 6-8 with NaOH. The water temperature was 30 ° C.
循環水槽内の循環液を排出し、30分後に井水を用い50
/分で30分間充填層を水洗浄した。Drain the circulating fluid from the circulating water tank and use well water after 30 minutes.
The packed bed was washed with water / min for 30 minutes.
その結果は、実験前にはLV 0.4m/sec、L/G 30/m3で
充填層の圧力損失は100mmH2Oであったが、実験後には同
条件下で圧力損失が25mmH2Oまで減少した。As a result, the pressure loss of the packed bed was 100 mmH 2 O at LV 0.4 m / sec and L / G 30 / m 3 before the experiment, but after the experiment, the pressure loss was up to 25 mmH 2 O under the same conditions. Diminished.
本発明は、微生物の増殖による充填層の圧力損失の増大
を防止するために、充填材に付着した微生物のはく離方
法を提供する。本発明によれば、非常に簡単な方法で、
容易にかつ安全に微生物のはく離除去が可能となる。The present invention provides a method for removing microorganisms attached to a packing material in order to prevent an increase in pressure loss of the packed bed due to the growth of microorganisms. According to the invention, in a very simple way,
It is possible to easily and safely remove and remove microorganisms.
第1図は、本発明の一実施例に係る気液接触装置の構成
を示す概略図である。 1……原ガス流入管のダンパー、2……充填材、3……
気液接触塔、4……散水部、5……ガス出口部、6……
洗浄水ライン弁、7……循環ポンプ吐出弁、8……循環
ポンプ、9……排水弁、10……循環水槽、11……NaHSO3
注入ラインFIG. 1 is a schematic diagram showing the structure of a gas-liquid contact device according to an embodiment of the present invention. 1 ... Damper for raw gas inflow pipe, 2 ... Filling material, 3 ...
Gas-liquid contact tower, 4 ... Sprinkler, 5 ... Gas outlet, 6 ...
Wash water line valve, 7 ... Circulation pump discharge valve, 8 ... Circulation pump, 9 ... Drain valve, 10 ... Circulation water tank, 11 ... NaHSO 3
Injection line
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 B01D 53/77 C02F 1/00 ZAB U F28C 1/00 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI Technical display location B01D 53/77 C02F 1/00 ZAB U F28C 1/00
Claims (2)
を有する気液接触塔において、該塔内又は充填層を嫌気
的条件にすることを特徴とする付着微生物のはく離方
法。1. A method for separating adhered microorganisms, characterized in that in a gas-liquid contact tower having a packed bed packed with a packing material to which microorganisms adhere, the inside of the tower or the packed bed is subjected to anaerobic conditions.
臭塔又は高温ガスを減温するスクラバー塔である請求項
1記載の付着微生物のはく離方法。2. The method for removing adhered microorganisms according to claim 1, wherein the gas-liquid contact tower is a deodorizing tower for offensive odor gas by microorganisms or a scrubber tower for reducing the temperature of high temperature gas.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2284364A JPH0777601B2 (en) | 1990-10-24 | 1990-10-24 | Method for removing adhered microorganisms |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2284364A JPH0777601B2 (en) | 1990-10-24 | 1990-10-24 | Method for removing adhered microorganisms |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04161216A JPH04161216A (en) | 1992-06-04 |
| JPH0777601B2 true JPH0777601B2 (en) | 1995-08-23 |
Family
ID=17677633
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2284364A Expired - Lifetime JPH0777601B2 (en) | 1990-10-24 | 1990-10-24 | Method for removing adhered microorganisms |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0777601B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6511844B1 (en) * | 2000-02-11 | 2003-01-28 | Michael A. Smith | Air purification system and method of using the same |
| JP2003130558A (en) * | 2001-10-30 | 2003-05-08 | Sanki Eng Co Ltd | Strainer attached to cooling tower |
-
1990
- 1990-10-24 JP JP2284364A patent/JPH0777601B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH04161216A (en) | 1992-06-04 |
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