JPH07944A - Garbage treating device - Google Patents
Garbage treating deviceInfo
- Publication number
- JPH07944A JPH07944A JP4186956A JP18695692A JPH07944A JP H07944 A JPH07944 A JP H07944A JP 4186956 A JP4186956 A JP 4186956A JP 18695692 A JP18695692 A JP 18695692A JP H07944 A JPH07944 A JP H07944A
- Authority
- JP
- Japan
- Prior art keywords
- anaerobic
- garbage
- layer
- aerobic
- treated 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.)
- Pending
Links
- 239000010813 municipal solid waste Substances 0.000 title claims abstract description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 29
- 239000007787 solid Substances 0.000 claims abstract description 27
- 238000011282 treatment Methods 0.000 claims abstract description 26
- 239000007788 liquid Substances 0.000 claims abstract description 19
- 241001148471 unidentified anaerobic bacterium Species 0.000 claims abstract description 7
- 238000000926 separation method Methods 0.000 claims description 20
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 10
- 229910052760 oxygen Inorganic materials 0.000 claims description 10
- 239000001301 oxygen Substances 0.000 claims description 10
- 239000010806 kitchen waste Substances 0.000 claims description 6
- 238000007599 discharging Methods 0.000 claims description 2
- 238000011221 initial treatment Methods 0.000 claims 2
- 239000000463 material Substances 0.000 abstract description 9
- 241001148470 aerobic bacillus Species 0.000 abstract description 7
- 239000012528 membrane Substances 0.000 abstract description 5
- 238000000354 decomposition reaction Methods 0.000 abstract description 3
- 238000012423 maintenance Methods 0.000 abstract description 2
- 241000894006 Bacteria Species 0.000 description 5
- 238000009434 installation Methods 0.000 description 5
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 239000002253 acid Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 235000014113 dietary fatty acids Nutrition 0.000 description 2
- 229930195729 fatty acid Natural products 0.000 description 2
- 239000000194 fatty acid Substances 0.000 description 2
- 150000004665 fatty acids Chemical class 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 230000007062 hydrolysis Effects 0.000 description 2
- 238000006460 hydrolysis reaction Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000000696 methanogenic effect Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- -1 and conversely Chemical compound 0.000 description 1
- 230000001174 ascending effect Effects 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 230000003301 hydrolyzing effect Effects 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000010802 sludge 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Landscapes
- Processing Of Solid Wastes (AREA)
- Treatment Of Sludge (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】この発明は、特に、家庭から出る
厨芥の処理に適した厨芥処理装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a kitchen waste treating apparatus suitable for treating kitchen garbage produced at home.
【0002】[0002]
【従来の技術】従来、集合住宅や多数の家庭から出る生
ゴミ等の厨芥をまとめて処理する手段として厨芥処理装
置が知られている。2. Description of the Related Art Conventionally, a garbage disposal device has been known as a means for collectively disposing of garbage such as garbage from an apartment house or a large number of households.
【0003】厨芥処理装置の概要は、前処理槽、発酵
槽、汚泥分離槽、調整槽、曝気槽、沈澱槽等多数の処理
槽を有し、前半側は有機固形物を嫌気性菌により分解す
る嫌気性処理となっている。また、後半側は嫌気性処理
された溶解した有機物をさらに好気性菌により分解する
好気性処理となっていて、好気性処理した処理水を下水
へ流すシステムとなっている。An outline of the kitchen waste treatment apparatus has a large number of treatment tanks such as a pretreatment tank, a fermentation tank, a sludge separation tank, a conditioning tank, an aeration tank, and a precipitation tank. The first half side decomposes organic solid matter by anaerobic bacteria. It is an anaerobic treatment. On the other hand, the latter half is an aerobic treatment in which dissolved organic substances subjected to anaerobic treatment are further decomposed by aerobic bacteria, and the system is a system in which treated water subjected to aerobic treatment is passed to sewage.
【0004】[0004]
【発明が解決しようとする課題】前記した如く従来の厨
芥処理装置において、好気性菌による好気性処理にあっ
ては、多量の酸素を必要とする反面、嫌気性菌による嫌
気性処理にあっては、酸素を必要とせず、逆に嫌気性処
理にあたって酸素は、分解処理能力を低下させる要因と
なっている。このために、、嫌気性処理槽と好気性処理
槽とはそれぞれ独立して設ける必要があるため、大きな
設置スペースが必要になると共にシステム自体も複雑化
する等の問題があったものである。As described above, in the conventional garbage treating apparatus, the aerobic treatment with aerobic bacteria requires a large amount of oxygen, while the anaerobic treatment with anaerobic bacteria is required. Does not require oxygen, and conversely, oxygen is a factor that reduces the decomposition treatment capacity during anaerobic treatment. For this reason, since the anaerobic treatment tank and the aerobic treatment tank need to be provided separately, a large installation space is required and the system itself becomes complicated.
【0005】そこで、この発明は、システムの簡素化を
図ると共に占有設置スペースも小さくて済む厨芥処理装
置を提供することを目的としている。Therefore, an object of the present invention is to provide a garbage disposal device which simplifies the system and requires a small installation space.
【0006】[0006]
【課題を解決するための手段】前記目的を達成するため
に、この発明は、処理槽の下から順に配置されると共に
最下位に設けられ粉砕した厨芥を取入れる取入部と、取
入部から取入れた厨芥を嫌気性菌により分解処理する嫌
気性層と、嫌気性層により分解処理された固形物と一次
処理水とに分離する固・液分離層と、酸素が与えられ前
記固・液分離層によって分離された一次処理水を二次処
理水とする好気性層と、好気性層からの二次処理水を外
部へ排出する排水部とを備えている。In order to achieve the above-mentioned object, the present invention is arranged in order from the bottom of a processing tank and is provided at the lowest position to take in crushed kitchen waste and to take in from the taking-in section. An anaerobic layer that decomposes kitchen waste with anaerobic bacteria, a solid / liquid separation layer that separates solid matter decomposed by the anaerobic layer into primary treated water, and the solid / liquid separation layer to which oxygen is applied. An aerobic layer that uses the primary treated water separated as a secondary treated water as a secondary treated water and a drainage unit that discharges the secondary treated water from the aerobic layer to the outside are provided.
【0007】[0007]
【作用】かかる厨芥処理装置によれば、最下位の取入部
から取入れられた粉砕した厨芥等の有機性固形物は、嫌
気性層により溶解性有機物へ分解処理され、上方の固・
液分離層に送られる。According to such a garbage treatment device, the organic solid matter such as crushed kitchen refuse taken in from the lowest intake portion is decomposed into the soluble organic matter by the anaerobic layer, and the solid matter above
It is sent to the liquid separation layer.
【0008】この固・液分離層において固形物と一次処
理水とに分離され、一次処理水のみ、上方の好気性層へ
送られ、好気性層において、さらに、分解処理される。
この時、処理槽内の流れは下から上方へ向かう流れとな
っていることと併せて、嫌気性層と好気性層との間に固
・液分離層が配置されるため好気性層の酸素が下方の嫌
気性層に流れ込むことはなく嫌気性処理に悪影響を与え
ることはない。In this solid / liquid separation layer, solid matter and primary treated water are separated, and only the primary treated water is sent to the upper aerobic layer and further decomposed in the aerobic layer.
At this time, the flow in the treatment tank is from the bottom to the top, and since the solid / liquid separation layer is arranged between the anaerobic layer and the aerobic layer, the oxygen in the aerobic layer is increased. Does not flow into the lower anaerobic layer and does not adversely affect the anaerobic treatment.
【0009】一方、固・液分離層からの一次処理水は、
好気性層にてさらに分解処理され、分解処理された二次
処理水は排水部から外へ排水されるようになる。On the other hand, the primary treated water from the solid / liquid separation layer is
Further decomposed in the aerobic layer, the decomposed secondary treated water is drained to the outside from the drainage section.
【0010】したがって、処理槽は一つで済むようにな
ると共に大きな占有設置スペースを必要としない。ま
た、システムも簡単となる。Therefore, only one processing tank is required and a large occupied installation space is not required. Also, the system becomes simple.
【0011】[0011]
【実施例】以下、図1乃至図6の図面を参照しながらこ
の発明の一実施例を詳細に説明する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described in detail below with reference to the drawings of FIGS.
【0012】図中1は厨芥処理装置3の処理槽を示して
おり、処理槽1には下から順に取入部5、嫌気性層7、
固・液分離層9、嫌気性層11、排水部13がそれぞれ
設けられている。In FIG. 1, reference numeral 1 denotes a processing tank of the garbage processing apparatus 3, and the processing tank 1 has an intake section 5, an anaerobic layer 7, and an order from the bottom.
A solid / liquid separation layer 9, an anaerobic layer 11, and a drainage section 13 are provided respectively.
【0013】最下位の取入部5は、三方弁15を有して
おり、この三方弁15は図2に示すように処理槽1の底
部1aへ続く第1ポートP1と、図示してない流し台の
設けられた厨芥粉砕機で粉砕された厨芥を流し台からの
排水とともに強制的に送り出すポンプ17へ続く第2ポ
ートP2と、ドレンパイプ19へ続く第3ポートP3を
有し、三方弁15を操作して第1・第2・第3ポートP
1・P2・P3を選択することで、図2の如く処理槽1
の底部1aとポンプ17が、また、図3の如く処理槽1
の底部1aとドレンパイプ19がそれぞれ接続連通し合
うようになっている。The lowest intake part 5 has a three-way valve 15, which is shown in FIG. 2 and has a first port P1 leading to the bottom 1a of the treatment tank 1 and a sink (not shown). Has a second port P2 leading to a pump 17 that compulsorily discharges the garbage crushed by the garbage crusher provided with the drainage from the sink and a third port P3 leading to the drain pipe 19, and operates the three-way valve 15. And then the 1st, 2nd, 3rd port P
By selecting 1, P2, and P3, processing tank 1 as shown in Fig. 2
As shown in FIG. 3, the bottom portion 1a and the pump 17 of the processing tank 1
The bottom portion 1a and the drain pipe 19 are connected and communicate with each other.
【0014】嫌気性層7は、取入部5の上方に位置し嫌
気性菌となるメインの加水分解細菌の他に、酸生成細
菌、メタン生成細菌等を有し、加水分解細菌による固形
物あるいは高分子有機物から溶解性有機物を生成する加
水分解過程が得られるようになる。また、酸生成細菌に
よる加水分解生成物から脂肪酸及び水素などを生成する
酸生成過程と、メタン生成細菌による水素や脂肪酸など
からメタンと二酸化炭素を生成するメタン生成過程が得
られ、分解処理された固形物は沈澱し、分解処理水は上
昇流にのって上方へ流れるようになる。The anaerobic layer 7 has acid-producing bacteria, methanogenic bacteria, etc. in addition to main hydrolyzing bacteria which are located above the intake part 5 and become anaerobic bacteria. A hydrolysis process for producing soluble organic substances from high molecular weight organic substances can be obtained. In addition, the acid production process of producing fatty acids and hydrogen from the hydrolysis products of acid-producing bacteria and the methane production process of producing methane and carbon dioxide from hydrogen and fatty acids by methanogenic bacteria were obtained and decomposed. The solid matter precipitates, and the decomposed water flows upward in an upward flow.
【0015】固・液分離層9は、下方の嫌気性層7及び
上方の好気性層11を仕切る液層となっており、嫌気性
層7で分解処理された一次処理水が通過する分離膜21
を有している。固・液分離層9の領域は下から上方へ向
けてゆっくり上昇流が流れると共に、この流れは、好気
性層11からの溶存酸素が嫌気性層7側へ流入する拡散
速度より速くなるよう設定され、嫌気性層7への酸素の
流入が阻止されるようになっている。The solid / liquid separation layer 9 is a liquid layer that partitions the lower anaerobic layer 7 and the upper aerobic layer 11, and a separation membrane through which the primary treated water decomposed in the anaerobic layer 7 passes. 21
have. In the region of the solid / liquid separation layer 9, an upward flow slowly flows from the bottom to the top, and this flow is set so as to be faster than the diffusion rate of the dissolved oxygen from the aerobic layer 11 flowing into the anaerobic layer 7 side. Thus, the inflow of oxygen to the anaerobic layer 7 is blocked.
【0016】好気性層11は、固・液分離層9の上方に
位置し、好気性菌により分解処理し、外部へ排水可能な
二次処理水が得られるよう機能するもので、支持部材2
3によって固定支持された好気性菌濾床材25と、その
下部に空気供給管27を有している。The aerobic layer 11 is located above the solid / liquid separation layer 9 and functions to obtain secondary treated water that can be discharged to the outside after being decomposed by aerobic bacteria and treated.
3 has an aerobic filter bed material 25 fixed and supported thereon, and an air supply pipe 27 in the lower part thereof.
【0017】好気性菌濾床材25は、図4に示すように
蛇腹状の形状となっているが、図5に示すようにブロッ
ク状のものであってもよい。また、図6に示すように円
板状のものであってもよい。The aerobic filter bed material 25 has a bellows shape as shown in FIG. 4, but may have a block shape as shown in FIG. Further, as shown in FIG. 6, it may have a disc shape.
【0018】なお、好気性菌濾床材25を円板状にする
ことで、図7に示すごとく、モータ29からの回転動力
を減速機31を介して与えられる回転軸33に回転自在
に装着することで、回転時において、上方からの酸素の
取入れが可能となり空気供給管27の省略が可能とな
る。この結果、処理槽1の全高Hを低く抑えることがで
きるメリットが得られる。By making the aerobic filter bed material 25 into a disk shape, as shown in FIG. 7, the rotary power from the motor 29 is rotatably mounted on the rotary shaft 33 given through the speed reducer 31. By doing so, during rotation, it is possible to take in oxygen from above and to omit the air supply pipe 27. As a result, there is an advantage that the total height H of the processing tank 1 can be suppressed low.
【0019】一方、空気供給管27は、図外のエアポン
プと接続し、エアポンプからエアが供給されるようにな
っている。On the other hand, the air supply pipe 27 is connected to an air pump (not shown) so that air is supplied from the air pump.
【0020】排出部13は、好気性層11で分解処理さ
れた二次処理水を外部へ排出するよう機能し、排水弁3
5を作動制御することで開閉が可能となっている。The discharge part 13 functions to discharge the secondary treated water decomposed by the aerobic layer 11 to the outside, and the drain valve 3
It can be opened and closed by controlling the operation of 5.
【0021】このように構成された厨芥処理装置によれ
ば、三方弁15を図2に切換えることでポンプ17によ
って粉砕された厨芥は最下位の取入部5から嫌気性層7
に送り込まれる。送り込まれた厨芥は嫌気性層7におい
て嫌気性菌により溶解性有機物に分解処理される。分解
処理された一次処理水は、固・液分離層9の分離膜21
を通過する。一方、固形物は分離膜21によって阻止さ
れ自重により嫌気性層7の底部に沈澱するようになり、
以下、取入部5からの粉砕した厨芥は嫌気性層7におい
て順次嫌気性処理されるようになる。この場合、上方の
好気性層11と下方の嫌気性層7の間に位置する固・液
分離層9によって、又、上方へ流れる上昇流によって好
気性層11の酸素(空気)が嫌気性層7に流れ込む虞れ
はなく、良好な嫌気性処理が可能となる。According to the garbage treatment apparatus thus constructed, the garbage that is crushed by the pump 17 by switching the three-way valve 15 to the one shown in FIG. 2 is fed from the lowest intake portion 5 to the anaerobic layer 7.
Sent to. The sent garbage is decomposed in the anaerobic layer 7 by anaerobic bacteria into soluble organic substances. The decomposed primary treated water is passed through the separation membrane 21 of the solid / liquid separation layer 9.
Pass through. On the other hand, the solid matter is blocked by the separation membrane 21 and begins to settle on the bottom of the anaerobic layer 7 due to its own weight.
After that, the crushed kitchen waste from the intake section 5 is sequentially subjected to anaerobic treatment in the anaerobic layer 7. In this case, oxygen (air) in the aerobic layer 11 is removed by the solid / liquid separation layer 9 located between the upper aerobic layer 11 and the lower anaerobic layer 7 and by the upward flow flowing upward. There is no possibility of flowing into 7, and good anaerobic treatment becomes possible.
【0022】一方、固・液分離層9において、固形物と
一次処理水とに分離された一次処理水はゆっくりとした
上昇流にのって上方の好気性層11に送り込まれる。On the other hand, in the solid / liquid separation layer 9, the primary treated water separated into the solid matter and the primary treated water is sent to the upper aerobic layer 11 in a slow ascending flow.
【0023】好気性層11に送り込まれた一次処理水
は、空気供給管27から与えられる空気と好気性菌濾床
材25とによってさらに良質な二次処理水に分解処理さ
れた後、二次処理水は、排水部13から外へ排水される
ようになる。The primary treated water sent to the aerobic layer 11 is decomposed into the secondary treated water of higher quality by the air supplied from the air supply pipe 27 and the aerobic bacteria filter bed material 25, and then the secondary treated water is subjected to the secondary treatment. The treated water is drained from the drainage unit 13 to the outside.
【0024】この一連の動作において、処理槽1は一つ
で済むため占有設置スペースは小さくて済むようにな
る。しかも、各処理層が一つの処理槽1内に納まってい
るためシステムも簡単となる。In this series of operations, since only one processing tank 1 is required, the occupied installation space can be made small. Moreover, the system is simplified because each processing layer is housed in one processing tank 1.
【0025】また、処理槽1の底に溜まった沈澱物は、
三方弁15を図3のように切換えることで簡単に外へ排
出処理できるようになる。Further, the precipitate accumulated at the bottom of the processing tank 1 is
By switching the three-way valve 15 as shown in FIG. 3, it becomes possible to easily perform the discharging process to the outside.
【0026】[0026]
【発明の効果】以上、説明したように、この発明の厨芥
処理装置によれば、占有設置スペースが小さくて済むと
共にシステムの簡素化が図れる。また、メンテナンスの
面でも大変好ましいものとなる。As described above, according to the garbage processing apparatus of the present invention, the occupied installation space can be small and the system can be simplified. Also, it is very preferable in terms of maintenance.
【図1】この発明を実施した厨芥処理装置の概要切断面
図、FIG. 1 is a schematic cross-sectional view of a garbage processing device embodying the present invention,
【図2】三方弁の動作図、FIG. 2 is an operation diagram of a three-way valve,
【図3】三方弁の動作図、FIG. 3 is an operation diagram of a three-way valve,
【図4】好気性菌濾床材の斜視図、FIG. 4 is a perspective view of an aerobic filter bed material,
【図5】好気性菌濾床材の変形例を示した図4と同様の
斜視図、FIG. 5 is a perspective view similar to FIG. 4 showing a modified example of a filter bed material for aerobic bacteria.
【図6】好気性菌濾床材の変形例を示した図4と同様の
斜視図、FIG. 6 is a perspective view similar to FIG. 4, showing a modified example of a filter bed material for aerobic bacteria.
【図7】円板タイプの好気性菌濾床材を好気性層に実施
した図1と同様の概要切断面図、FIG. 7 is a schematic sectional view similar to FIG. 1, in which a disk-type aerobic filter bed material is applied to the aerobic layer.
1 処理槽 5 取入部 7 嫌気性層 9 固・液分離層 11 好気性層 13 排水部 1 Treatment Tank 5 Intake Port 7 Anaerobic Layer 9 Solid / Liquid Separation Layer 11 Aerobic Layer 13 Drainage Portion
Claims (1)
下位に設けられ粉砕した厨芥を取入れる取入部と、取入
部から取入れた粉砕した厨芥を嫌気性菌により分解処理
する嫌気性層と、嫌気性層により分解処理された固形物
と一次処理水とに分離する固・液分離層と、酸素が与え
られ前記固・液分離層によって分離された一次処理水を
二次処理水とする好気性層と、好気性層からの二次処理
水を外部へ排出する排水部とを備えていることを特徴と
する厨芥処理装置。1. An intake section, which is arranged in order from the bottom of the treatment tank and is provided at the lowest position, for receiving crushed garbage, and an anaerobic layer for decomposing the crushed garbage taken from the intake section with anaerobic bacteria. The solid / liquid separation layer for separating the solid matter decomposed by the anaerobic layer into the primary treatment water and the primary treatment water separated by the solid / liquid separation layer to which oxygen is applied are used as the secondary treatment water. A kitchen waste treatment device comprising an aerobic layer and a drainage section for discharging secondary treated water from the aerobic layer to the outside.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4186956A JPH07944A (en) | 1992-07-14 | 1992-07-14 | Garbage treating device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4186956A JPH07944A (en) | 1992-07-14 | 1992-07-14 | Garbage treating device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH07944A true JPH07944A (en) | 1995-01-06 |
Family
ID=16197670
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4186956A Pending JPH07944A (en) | 1992-07-14 | 1992-07-14 | Garbage treating device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH07944A (en) |
-
1992
- 1992-07-14 JP JP4186956A patent/JPH07944A/en active Pending
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