JP2002241537A - Apparatus for waste disposal - Google Patents
Apparatus for waste disposalInfo
- Publication number
- JP2002241537A JP2002241537A JP2001035583A JP2001035583A JP2002241537A JP 2002241537 A JP2002241537 A JP 2002241537A JP 2001035583 A JP2001035583 A JP 2001035583A JP 2001035583 A JP2001035583 A JP 2001035583A JP 2002241537 A JP2002241537 A JP 2002241537A
- Authority
- JP
- Japan
- Prior art keywords
- waste
- adjusting means
- microorganisms
- treatment tank
- concentration
- 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
- 239000002699 waste material Substances 0.000 title claims abstract description 19
- 244000005700 microbiome Species 0.000 claims abstract description 17
- 238000000855 fermentation Methods 0.000 claims abstract description 12
- 230000004151 fermentation Effects 0.000 claims abstract description 12
- 230000001737 promoting effect Effects 0.000 claims abstract 3
- 241000894006 Bacteria Species 0.000 claims description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 17
- 239000012153 distilled water Substances 0.000 claims description 12
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 11
- 150000003839 salts Chemical class 0.000 claims description 11
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims description 10
- 235000011114 ammonium hydroxide Nutrition 0.000 claims description 10
- 238000003756 stirring Methods 0.000 claims description 9
- 238000000354 decomposition reaction Methods 0.000 claims description 3
- 239000012895 dilution Substances 0.000 claims description 2
- 238000010790 dilution Methods 0.000 claims description 2
- 239000000243 solution Substances 0.000 claims description 2
- 230000035755 proliferation Effects 0.000 abstract 2
- 230000029219 regulation of pH Effects 0.000 abstract 1
- 239000002904 solvent Substances 0.000 description 14
- 229920001971 elastomer Polymers 0.000 description 6
- 239000005060 rubber Substances 0.000 description 6
- QMMFVYPAHWMCMS-UHFFFAOYSA-N Dimethyl sulfide Chemical compound CSC QMMFVYPAHWMCMS-UHFFFAOYSA-N 0.000 description 3
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- ZTQSAGDEMFDKMZ-UHFFFAOYSA-N butyric aldehyde Natural products CCCC=O ZTQSAGDEMFDKMZ-UHFFFAOYSA-N 0.000 description 3
- YGHRJJRRZDOVPD-UHFFFAOYSA-N 3-methylbutanal Chemical compound CC(C)CC=O YGHRJJRRZDOVPD-UHFFFAOYSA-N 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 235000014469 Bacillus subtilis Nutrition 0.000 description 2
- 101000707152 Homo sapiens SH2B adapter protein 1 Proteins 0.000 description 2
- AMIMRNSIRUDHCM-UHFFFAOYSA-N Isopropylaldehyde Chemical compound CC(C)C=O AMIMRNSIRUDHCM-UHFFFAOYSA-N 0.000 description 2
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical compound SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 description 2
- NBBJYMSMWIIQGU-UHFFFAOYSA-N Propionic aldehyde Chemical compound CCC=O NBBJYMSMWIIQGU-UHFFFAOYSA-N 0.000 description 2
- 102100031770 SH2B adapter protein 1 Human genes 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- 241001148470 aerobic bacillus Species 0.000 description 2
- 230000001580 bacterial effect Effects 0.000 description 2
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- ZXEKIIBDNHEJCQ-UHFFFAOYSA-N isobutanol Chemical compound CC(C)CO ZXEKIIBDNHEJCQ-UHFFFAOYSA-N 0.000 description 2
- HGBOYTHUEUWSSQ-UHFFFAOYSA-N pentanal Chemical compound CCCCC=O HGBOYTHUEUWSSQ-UHFFFAOYSA-N 0.000 description 2
- 239000002861 polymer material Substances 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical compound CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 description 2
- NQPDZGIKBAWPEJ-UHFFFAOYSA-N valeric acid Chemical compound CCCCC(O)=O NQPDZGIKBAWPEJ-UHFFFAOYSA-N 0.000 description 2
- XYHKNCXZYYTLRG-UHFFFAOYSA-N 1h-imidazole-2-carbaldehyde Chemical compound O=CC1=NC=CN1 XYHKNCXZYYTLRG-UHFFFAOYSA-N 0.000 description 1
- GWYFCOCPABKNJV-UHFFFAOYSA-M 3-Methylbutanoic acid Natural products CC(C)CC([O-])=O GWYFCOCPABKNJV-UHFFFAOYSA-M 0.000 description 1
- 241000251468 Actinopterygii Species 0.000 description 1
- 241000193830 Bacillus <bacterium> Species 0.000 description 1
- 241000194110 Bacillus sp. (in: Bacteria) Species 0.000 description 1
- FERIUCNNQQJTOY-UHFFFAOYSA-N Butyric acid Chemical compound CCCC(O)=O FERIUCNNQQJTOY-UHFFFAOYSA-N 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- NTIZESTWPVYFNL-UHFFFAOYSA-N Methyl isobutyl ketone Chemical compound CC(C)CC(C)=O NTIZESTWPVYFNL-UHFFFAOYSA-N 0.000 description 1
- UIHCLUNTQKBZGK-UHFFFAOYSA-N Methyl isobutyl ketone Natural products CCC(C)C(C)=O UIHCLUNTQKBZGK-UHFFFAOYSA-N 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- IKHGUXGNUITLKF-XPULMUKRSA-N acetaldehyde Chemical compound [14CH]([14CH3])=O IKHGUXGNUITLKF-XPULMUKRSA-N 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- GWYFCOCPABKNJV-UHFFFAOYSA-N beta-methyl-butyric acid Natural products CC(C)CC(O)=O GWYFCOCPABKNJV-UHFFFAOYSA-N 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000000644 propagated effect Effects 0.000 description 1
- 235000019260 propionic acid Nutrition 0.000 description 1
- IUVKMZGDUIUOCP-BTNSXGMBSA-N quinbolone Chemical compound O([C@H]1CC[C@H]2[C@H]3[C@@H]([C@]4(C=CC(=O)C=C4CC3)C)CC[C@@]21C)C1=CCCC1 IUVKMZGDUIUOCP-BTNSXGMBSA-N 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229940005605 valeric acid Drugs 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
- 239000008096 xylene 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Landscapes
- Processing Of Solid Wastes (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、主にゴム手袋等の
高分子材料から成る廃棄物を微生物を用いて分解処理す
る廃棄物処理装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a waste treatment apparatus for decomposing a waste mainly composed of a polymer material such as rubber gloves using a microorganism.
【0002】[0002]
【従来の技術】野菜類や魚等の生ゴミは、例えば特開平
9−174026号公報等に示される様に、微生物を用
いることで比較的容易に分解処理する事が出来るが、ゴ
ム手袋等のゴム類の場合では、そのまま微生物を混ぜて
発酵させてもなかなか分解できないという問題がある。2. Description of the Related Art Garbage such as vegetables and fish can be relatively easily decomposed by using microorganisms, as shown in, for example, Japanese Patent Application Laid-Open No. 9-174026. In the case of the rubbers described above, there is a problem that it is difficult to decompose even if the microorganisms are mixed and fermented as they are.
【0003】[0003]
【発明が解決しようとする課題】そこで本発明は、より
短時間で効率的にゴム手袋等の廃棄物を分解処理する事
を目的とするものである。SUMMARY OF THE INVENTION Accordingly, an object of the present invention is to decompose waste such as rubber gloves in a shorter time and more efficiently.
【0004】[0004]
【課題を解決するための手段】本発明は、増殖させた発
酵菌を収容する処理槽と、前記処理槽内に設けた前記発
酵菌の攪拌手段と、微生物の増殖を促進するph調整手
段とを備え、廃棄物を処理槽内に投入し前記攪拌手段に
より攪拌して分解処理を行うと共に、ph調整手段によ
りph値を調整するものである。According to the present invention, there is provided a treatment tank for accommodating grown fermentation bacteria, stirring means for the fermentation bacteria provided in the treatment tank, and ph adjusting means for accelerating the growth of microorganisms. In addition to the above, the waste is put into the treatment tank, and the waste is stirred by the stirring means to perform the decomposition treatment, and the ph value is adjusted by the ph adjusting means.
【0005】また前記ph調整手段は、希釈塩酸、希釈
アンモニア水、蒸留水の溶液をph濃度に応じて希釈率
を調整するものである。The ph adjusting means adjusts the dilution rate of a solution of diluted hydrochloric acid, diluted ammonia water and distilled water according to the ph concentration.
【0006】そして、前記処理槽には塩分濃度調整手段
を設け、処理槽内の微生物中の塩分濃度が最適値よりも
濃い場合は蒸留水を加水して調整するものである。The treatment tank is provided with a salt concentration adjusting means, and when the salt concentration in microorganisms in the treatment tank is higher than an optimum value, the concentration is adjusted by adding distilled water.
【0007】[0007]
【発明の実施の形態】本発明による実施例を先ず図1に
基づき説明すると、1は装置本体で、一側に底面をU字
状に形成した有底角筒状の処理槽2を区画形成し底部に
菌床を備えていると共に、他側の底部に収納室3を区画
形成し、かつこの収納室の上方に排気処理槽4を区画形
成している。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment according to the present invention will be described first with reference to FIG. 1. Reference numeral 1 denotes an apparatus main body, which forms a bottomed rectangular cylindrical processing tank 2 having a U-shaped bottom on one side. At the bottom, a bacterial bed is provided, and a storage chamber 3 is defined at the bottom on the other side, and an exhaust treatment tank 4 is defined above the storage chamber.
【0008】5は上記処理槽2内に装着した攪拌手段
で、両端を一対の軸受6、6にて略水平方向に軸支した
回転シャフト7と、この回転シャフトの周囲に固着した
攪拌翼8と、上記収納室3内に設置され、ベルト9、プ
ーリー10を介して上記回転シャフト7を回転駆動する
モータ11とから主に構成している。Reference numeral 5 denotes a stirring means mounted in the processing tank 2. A rotating shaft 7 having both ends supported in a substantially horizontal direction by a pair of bearings 6, 6 and a stirring blade 8 fixed around the rotating shaft. And a motor 11 that is installed in the storage chamber 3 and drives the rotary shaft 7 to rotate via a belt 9 and a pulley 10.
【0009】12は上記処理槽2の上部側壁に開口した
排気孔で、先端に開口した排出孔13を、上記排気処理
槽4内に貯溜した脱臭用の処理水14の水中に開口した
排気ダクト15を連結していると共に、この排気ダクト
の途中に排気ファン16を装着している。Reference numeral 12 denotes an exhaust hole opened in the upper side wall of the processing tank 2, and an exhaust hole 13 opened at the tip is provided with an exhaust duct opened in the water of the deodorized treatment water 14 stored in the exhaust processing tank 4. 15 and an exhaust fan 16 is mounted in the exhaust duct.
【0010】尚、上記処理水14には、例えば好気性枯
草菌(バチラス属菌)を主体としてその他の菌を消臭用
にブレンドした有効微生物複合菌を投入し、一方、上記
排気孔12から排気される排気中の悪臭物質として、ア
ンモニア、メチルメルカブタン、硫化水素、硫化メチ
ル、一硫化メチル、トリメチルアミン、アセトアルデヒ
ド、スチレン、プロピオン酸、ノルマル酪酸、ノルマル
吉草酸、イソ吉草酸、トルエン、キシレン、メチルイソ
ブチルケトン、酢酸エチル、イソブタノール、プロピオ
ンアルデヒド、イソバレルアルデヒド、イソブチルアル
デヒド、ノルマルバレルアルデヒド、ノルマルブチルア
ルデヒド等があり、これらを分解する菌を用いる。The treated water 14 is filled with an effective microbial complex, for example, mainly composed of aerobic Bacillus subtilis (Bacillus sp.) And blended with other bacteria for deodorization. As the malodorous substances in the exhaust gas, ammonia, methyl mercaptan, hydrogen sulfide, methyl sulfide, methyl monosulfide, trimethylamine, acetaldehyde, styrene, propionic acid, normal butyric acid, normal valeric acid, isovaleric acid, toluene, xylene, There are methyl isobutyl ketone, ethyl acetate, isobutanol, propionaldehyde, isovaleraldehyde, isobutyraldehyde, normal valeraldehyde, normal butyraldehyde, etc., and a bacterium that decomposes these is used.
【0011】又、上記処理槽2の外底壁面には、シーズ
ヒータ等のヒータ17を埋設し、図示しない周知のサー
ミスタ等の温度センサにて処理槽2内の温度を検出して
通電制御し、廃棄物処理用の例えば好気性枯草菌(バチ
ラス、サチラス属菌)を主体に、発酵菌やその他の菌を
廃棄物の種類に応じてブレンドした廃棄物処理用の微生
物が増殖し易い温度に加熱制御する様に構成している。A heater 17 such as a sheathed heater is buried in the outer bottom wall surface of the processing tank 2, and the temperature in the processing tank 2 is detected by a not-shown temperature sensor such as a thermistor to control the power supply. For example, aerobic Bacillus subtilis (Bacillus, Sachira spp.) For waste treatment is mainly used, and fermentation bacteria and other bacteria are blended according to the type of waste. It is configured to control heating.
【0012】更に、上記処理水14を貯溜する排気処理
槽4の上面には、この処理水表面より発生する排気を排
出する排気ファン18を設けている。Further, an exhaust fan 18 for discharging exhaust gas generated from the surface of the treated water is provided on the upper surface of the exhaust treatment tank 4 for storing the treated water 14.
【0013】19は上記処理槽2の上部に配設した粉砕
手段で、円筒状の破砕室20内の略中心位置に、モータ
21にて直接或いは間接的に回転駆動される回転軸22
を略垂直に配設すると共に、この回転軸の周囲に多数の
粉砕刀23・・を櫛歯状に配設し、かつこれら粉砕刃間
に対向位置して対向刃24・・を上記破砕室20の内壁
より穿設している。Numeral 19 denotes a crushing means disposed on the upper part of the processing tank 2, and a rotary shaft 22 directly or indirectly driven by a motor 21 at a substantially central position in a cylindrical crushing chamber 20.
Are arranged substantially vertically, a large number of crushing knives 23 are arranged in a comb-like shape around the rotating shaft, and the opposing blades 24 are arranged between the crushing blades so as to face each other. 20 are pierced from the inner wall.
【0014】又、上記破砕室20の上部側壁には廃棄物
を投入する投入口25を開口していると共に、破砕室2
0の底面には、破砕された廃棄物を処理室2内に落下す
る供給口26を穿孔している。The upper side wall of the crushing chamber 20 has an opening 25 for charging waste, and the crushing chamber 2
A supply port 26 for dropping the crushed waste into the processing chamber 2 is perforated in the bottom surface of the container 0.
【0015】27は上記粉砕手段19に隣接配設したp
h調整手段で、希釈塩酸28を貯める溶剤タンク29の
下方に、例えば電磁弁30により上記溶剤タンク29内
の希釈塩酸を流量制御しながら、上記処理室2内に供給
する溶剤供給パイプ31を装着している。Reference numeral 27 denotes a p disposed adjacent to the crushing means 19.
A solvent supply pipe 31 for supplying the inside of the processing chamber 2 while controlling the flow rate of the diluted hydrochloric acid in the solvent tank 29 by, for example, an electromagnetic valve 30 is attached below the solvent tank 29 for storing the diluted hydrochloric acid 28 by the h adjusting means. are doing.
【0016】尚、上記溶剤供給パイプ31は、希釈塩酸
を噴出する噴出口に図示しないノズルを設け、溶剤を霧
状に噴射したり、図示しない回転ノズルにより処理室2
内に略均一に噴射する様に構成しても良い。The solvent supply pipe 31 is provided with a nozzle (not shown) at an ejection port for ejecting the diluted hydrochloric acid, and sprays the solvent in a mist state or rotates the processing chamber 2 by a rotary nozzle (not shown).
May be configured so as to be injected substantially uniformly into the inside.
【0017】32は上記溶剤タンク24に隣接配置した
希釈アンモニア水33を貯める溶剤タンクで、電磁弁3
4により流量制御しながら上記処理室2内に供給する溶
剤供給パイプ35を装着している。Numeral 32 denotes a solvent tank for storing diluted ammonia water 33 disposed adjacent to the solvent tank 24.
4, a solvent supply pipe 35 for supplying the inside of the processing chamber 2 while controlling the flow rate is mounted.
【0018】尚、上記菌液供給パイプ35は、上記溶剤
供給パイプ31と同様なノズルを設け、希釈アンモニア
水33を上記処理室2内に略均一に噴射する様に構成し
ても良く、かつ上記電磁弁30、34は、ポンプやモー
タバルブ等により構成しても良い。The bacteria liquid supply pipe 35 may be provided with a nozzle similar to the solvent supply pipe 31 so as to spray the diluted ammonia water 33 into the processing chamber 2 substantially uniformly. The electromagnetic valves 30 and 34 may be configured by a pump, a motor valve, or the like.
【0019】35は上記溶剤タンク32に隣接配置した
蒸留水36を貯める溶剤タンクで、電磁弁37により流
量制御しながら処理室2内に供給する溶剤供給パイプ3
8を装着している。溶剤タンク35と蒸留水36と電磁
弁37は塩分濃度調整手段39をも構成する。A solvent tank 35 is disposed adjacent to the solvent tank 32 and stores distilled water 36. The solvent supply pipe 3 supplies the solvent supply pipe 3 into the processing chamber 2 while controlling the flow rate by an electromagnetic valve 37.
8 is attached. The solvent tank 35, the distilled water 36 and the solenoid valve 37 also constitute a salt concentration adjusting means 39.
【0020】40は上記処理室2の上方の排気孔12に
近接して配設した湿度センサーで、処理室内の廃棄物の
湿度を検出して前記蒸留水等を供給する。Reference numeral 40 denotes a humidity sensor disposed in proximity to the exhaust hole 12 above the processing chamber 2 for detecting the humidity of waste in the processing chamber and supplying the distilled water or the like.
【0021】41は前記処理室2の内側壁に取り付けた
phセンサーで、微生物の活動や繁殖に適した濃度にな
るように前記ph調整手段27を調整する。Reference numeral 41 denotes a ph sensor attached to the inner wall of the processing chamber 2, and adjusts the ph adjusting means 27 so as to have a concentration suitable for the activity and propagation of microorganisms.
【0022】ここで、微生物が増殖(繁殖)するための
要素を整理する。Here, factors for the growth (propagation) of microorganisms will be summarized.
【0023】増殖に必要な要素として、温度、酸素、水
分、塩分濃度等があるが、本願出願人は、さらにphも
大きな要素であることを着目し、このph濃度は発酵菌
の種類がSH2B菌で8〜9が最適であることが判明し
た。The factors necessary for growth include temperature, oxygen, moisture, salt concentration, etc. The applicant of the present application has noticed that ph is an even larger factor, and this ph concentration depends on the type of fermentation bacterium SH2B. 8-9 bacteria proved to be optimal.
【0024】而して、このph濃度を8〜9に維持する
ために、特に前述の希釈塩酸28や希釈アンモニア水3
3、蒸留水36を添加する。In order to maintain the ph concentration at 8 to 9, particularly, the diluted hydrochloric acid 28 and the diluted ammonia water 3 described above are used.
3, the addition of distilled water 36.
【0025】次に使用状態について述べる。あらかじめ
発酵菌(SH2B菌)を増殖させて処理槽2内の底部に
収容し菌床を構成する。Next, the state of use will be described. A fermentation bacterium (SH2B bacterium) is propagated in advance and stored in the bottom of the treatment tank 2 to constitute a bacterial bed.
【0026】高分子材料の廃棄物であるゴム手袋Gを投
入口25から投入し、モータ11、21の作動により攪
拌翼8を回転することで、ゴム手袋は粉砕手段19の粉
砕刃23・・と対向刃24・・により粉砕されて供給口
26より処理室2内に落下した後、攪拌手段5の攪拌翼
8により攪拌されながら発酵菌に触れ微生物によって分
解処理がされる。A rubber glove G, which is a waste material of a polymer material, is charged through the inlet 25, and the stirring blades 8 are rotated by the operation of the motors 11 and 21. After being pulverized by the opposed blades 24 and falling into the processing chamber 2 from the supply port 26, the fermentation bacteria are brought into contact with the fermentation bacteria while being agitated by the agitating blades 8 of the agitating means 5 and decomposed by the microorganisms.
【0027】そして、ゴム手袋の粉砕、分解処理が終了
すると、粉砕手段19の作動を停止する。When the crushing and disassembling processing of the rubber glove is completed, the operation of the crushing means 19 is stopped.
【0028】ところで、ゴム手袋を分解処理する微生物
は、十分に活性があり増殖していることが必要である
が、時間の経過や累計処理時間が長くなったような場合
には発酵菌のph値が変換する。By the way, the microorganisms for decomposing rubber gloves need to be sufficiently active and proliferate, but when the time elapses or the total treatment time becomes long, the pH of the fermentation bacteria is increased. The value is converted.
【0029】この時の変化をphセンサー41が検出
し、もしphが最適値の8〜9より高い場合には、その
上昇値に応じて電磁弁30の開放時間を決定しphセン
サーで実測しながら希釈塩酸28を落下し濃度を低くす
る。The change at this time is detected by the ph sensor 41. If the ph is higher than the optimum value of 8 to 9, the opening time of the solenoid valve 30 is determined according to the rise value and measured by the ph sensor. Then, the diluted hydrochloric acid 28 is dropped to lower the concentration.
【0030】反対に、phが最適値よりも低い場合に
は、その下降値に応じて電磁弁34の開放時間を決定し
phセンサーで実測しながら希釈アンモニア水33を落
下し濃度を高くする。On the other hand, if ph is lower than the optimum value, the opening time of the solenoid valve 34 is determined according to the decrease value, and the concentration is increased by dropping the diluted ammonia water 33 while actually measuring with the ph sensor.
【0031】そして、前述の希釈塩酸や希釈アンモニア
水によるphの調整時には、同時に電磁弁37を開放し
て蒸留水を落下し濃度を薄める。At the time of adjusting the pH with the diluted hydrochloric acid or the diluted ammonia water, the solenoid valve 37 is opened at the same time to drop the distilled water to reduce the concentration.
【0032】そして、前記塩分濃度の管理は、前述のp
hの測定により希釈塩酸や希釈アンモニア水とは別に行
うこともでき、塩分濃度が必要以上に濃くなって発酵菌
が耐海水用菌に変異するのを防止する。The management of the salt concentration is based on the aforementioned p
The measurement of h can be performed separately from the diluted hydrochloric acid and the diluted ammonia water, thereby preventing the salt concentration from becoming unnecessarily high and the fermentative bacteria from mutating to seawater resistant bacteria.
【0033】[0033]
【発明の効果】以上の様に本発明は、処理槽内に収容し
た発酵菌による微生物のph値をph調整手段により必
要に応じて調整するものであるから、ph値を見ながら
調整し微生物に活性化を与え、且つ増殖を早めて分解処
理を早めることができる。As described above, according to the present invention, the ph value of the microorganism by the fermenting bacteria contained in the treatment tank is adjusted as required by the ph adjusting means. To promote the degradation and to accelerate the decomposition process.
【0034】また、ph調整手段は、希釈塩酸と希釈ア
ンモニア水と蒸留水を用いるため、何れも発酵菌に対す
る影響が少なく微生物の増殖を妨げることがない。Further, since the ph adjusting means uses diluted hydrochloric acid, diluted ammonia water and distilled water, any of them has little influence on fermentation bacteria and does not hinder the growth of microorganisms.
【0035】さらに、仮に、処理槽内の塩分濃度が低く
なった場合には塩分濃度調整手段によって蒸留水を加水
して高めることができ、微生物の環境を良好にして増殖
を助長する。Further, if the salt concentration in the treatment tank becomes low, distilled water can be increased by adding salt concentration adjusting means, and the environment of microorganisms is improved to promote growth.
【図1】本発明の廃棄物処理装置の全体断面図である。FIG. 1 is an overall sectional view of a waste disposal apparatus according to the present invention.
1 装置本体 2 処理槽 5 攪拌手段 27 ph調整手段 28 希釈塩酸 33 希釈アンモニア水 36 蒸留水 39 塩分濃度調整手段 41 phセンサー DESCRIPTION OF SYMBOLS 1 Apparatus main body 2 Processing tank 5 Stirring means 27 Ph adjusting means 28 Dilute hydrochloric acid 33 Dilute ammonia water 36 Distilled water 39 Salt concentration adjusting means 41 Ph sensor
───────────────────────────────────────────────────── フロントページの続き (72)発明者 平野 典昭 鳥取県鳥取市南吉方3丁目201番地 鳥取 三洋電機株式会社内 (72)発明者 奥田 輝雄 鳥取県鳥取市南吉方3丁目201番地 鳥取 三洋電機株式会社内 (72)発明者 井尻 準之介 鳥取県鳥取市南吉方3丁目201番地 鳥取 三洋電機株式会社内 (72)発明者 岩村 康弘 鳥取県鳥取市南吉方3丁目201番地 鳥取 三洋電機株式会社内 Fターム(参考) 4D004 AA07 CA04 CA15 CA19 CA35 CA48 CB04 CB13 CB28 CB32 CC07 CC12 DA01 DA02 DA06 DA20 4F301 AA03 CA09 CA22 CA33 CA51 CA71 CA72 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Noriaki Hirano 3-201 Minamiyoshikata, Tottori City, Tottori Prefecture Inside Sanyo Electric Co., Ltd. (72) Inventor Teruo Okuda 3-201 Minamiyoshikata, Tottori City, Tottori Sanyo Electric Tottori (72) Inventor Junnosuke Ijiri 3-201 Minamiyoshikata, Tottori City, Tottori Prefecture Sanyo Electric Co., Ltd. (72) Inventor Yasuhiro Iwamura 3-201 Minamiyoshikata, Tottori City, Tottori Sanyo Electric Tottori F term (reference) 4D004 AA07 CA04 CA15 CA19 CA35 CA48 CB04 CB13 CB28 CB32 CC07 CC12 DA01 DA02 DA06 DA20 4F301 AA03 CA09 CA22 CA33 CA51 CA71 CA72
Claims (3)
前記処理槽内に設けた前記発酵菌の攪拌手段と、微生物
の増殖を促進するph調整手段とを備え、廃棄物を処理
槽内に投入し前記攪拌手段により攪拌して分解処理を行
うと共に、ph調整手段によりph値を調整することを
特徴とする廃棄物処理装置。Claims: 1. A treatment tank containing a grown fermentation bacterium,
The fermentation bacteria stirring means provided in the treatment tank, and a ph adjusting means for promoting the growth of microorganisms, while performing a decomposition treatment by throwing waste into the treatment tank and stirring by the stirring means, A waste treatment apparatus wherein a ph value is adjusted by ph adjusting means.
ンモニア水、蒸留水の溶液をph濃度に応じて希釈率を
調整することを特徴とする請求項1に記載の廃棄物処理
装置。2. The waste treatment apparatus according to claim 1, wherein said ph adjusting means adjusts a dilution rate of a solution of diluted hydrochloric acid, diluted ammonia water, and distilled water according to a ph concentration.
け、処理槽内の微生物中の塩分濃度が最適値よりも濃い
場合は蒸留水を加水して調整することを特徴とする請求
項1に記載の廃棄物処理装置。3. The treatment tank is provided with a salt concentration adjusting means, and when the salt concentration of microorganisms in the treatment tank is higher than an optimum value, the concentration is adjusted by adding distilled water. A waste treatment apparatus according to claim 1.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001035583A JP2002241537A (en) | 2001-02-13 | 2001-02-13 | Apparatus for waste disposal |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001035583A JP2002241537A (en) | 2001-02-13 | 2001-02-13 | Apparatus for waste disposal |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2002241537A true JP2002241537A (en) | 2002-08-28 |
Family
ID=18899008
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2001035583A Pending JP2002241537A (en) | 2001-02-13 | 2001-02-13 | Apparatus for waste disposal |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2002241537A (en) |
-
2001
- 2001-02-13 JP JP2001035583A patent/JP2002241537A/en active Pending
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