JP2580449B2 - Oil-water separator - Google Patents
Oil-water separatorInfo
- Publication number
- JP2580449B2 JP2580449B2 JP4288897A JP28889792A JP2580449B2 JP 2580449 B2 JP2580449 B2 JP 2580449B2 JP 4288897 A JP4288897 A JP 4288897A JP 28889792 A JP28889792 A JP 28889792A JP 2580449 B2 JP2580449 B2 JP 2580449B2
- Authority
- JP
- Japan
- Prior art keywords
- tank
- separation
- oil
- separation tank
- 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
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims description 44
- 238000000926 separation method Methods 0.000 claims description 88
- 239000003921 oil Substances 0.000 claims description 30
- 235000019198 oils Nutrition 0.000 claims description 30
- 239000002351 wastewater Substances 0.000 claims description 27
- 239000003795 chemical substances by application Substances 0.000 claims description 16
- 230000003472 neutralizing effect Effects 0.000 claims description 16
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 15
- 238000004062 sedimentation Methods 0.000 claims description 14
- 239000010802 sludge Substances 0.000 claims description 9
- 239000010775 animal oil Substances 0.000 claims description 7
- 235000015112 vegetable and seed oil Nutrition 0.000 claims description 7
- 239000008158 vegetable oil Substances 0.000 claims description 7
- 235000011121 sodium hydroxide Nutrition 0.000 claims description 5
- 239000008213 purified water Substances 0.000 claims description 4
- XLYOFNOQVPJJNP-DYCDLGHISA-N deuterium hydrogen oxide Chemical compound [2H]O XLYOFNOQVPJJNP-DYCDLGHISA-N 0.000 claims 2
- 239000003925 fat Substances 0.000 description 18
- 238000001556 precipitation Methods 0.000 description 15
- 238000005345 coagulation Methods 0.000 description 3
- 230000015271 coagulation Effects 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 239000004519 grease Substances 0.000 description 3
- 239000000701 coagulant Substances 0.000 description 2
- 235000014113 dietary fatty acids Nutrition 0.000 description 2
- 239000000194 fatty acid Substances 0.000 description 2
- 229930195729 fatty acid Natural products 0.000 description 2
- 150000004665 fatty acids Chemical class 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000010813 municipal solid waste Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
Landscapes
- Removal Of Floating Material (AREA)
Description
【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION
【0001】[0001]
【産業上の利用分野】本発明はレストランなどより排出
される廃水を油成分と水とに分離する油水分離装置に関
する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an oil / water separator for separating waste water discharged from a restaurant or the like into an oil component and water.
【0002】[0002]
【従来の技術】従来、レストランなどより排出される廃
水には動植物油が混入されており、同廃水は、沈澱槽を
有する分離槽で油成分と水とを分離するものであった。2. Description of the Related Art Conventionally, wastewater discharged from a restaurant or the like is mixed with animal and vegetable oils, and the wastewater separates oil components and water in a separation tank having a sedimentation tank.
【0003】また、同廃水は、沈澱槽に溜めた状態で中
和剤を混合させて処理するものであった。Further, the wastewater is treated by mixing a neutralizing agent in a state of being stored in a settling tank.
【0004】[0004]
【発明が解決しようとする課題】ところが、上記従来例
においては、沈澱槽内において、不純物が沈澱するまで
時間をおく必要があるために装置全体を間歇運転してい
た。したがって、廃水の分離が量的及び質的に低く、ま
た、作業を能率的にできなかった。However, in the above-mentioned prior art, the entire apparatus is operated intermittently in the precipitation tank because it is necessary to allow time for the impurities to precipitate in the precipitation tank. Therefore, the separation of wastewater is low in quantity and quality, and the operation cannot be performed efficiently.
【0005】[0005]
【課題を解決するための手段】本発明では、底部を有し
タンク状に形成され分離外槽の内部に、下側開口部を有
する分離内槽を位置させて二重構造とした分離槽を設け
て、同分離槽の分離内槽側に、動植物油が混入された廃
水を供給して、油脂成分と一次中間水及び汚泥とに分離
可能とし、かつ、分離外槽側より取り出した一次中間水
に苛性ソーダなどの中和剤を注入混合する混和装置を設
けると共に、中和剤が混合された凝集中間水を油脂成分
と浄水とに分離する沈澱分離槽を設け、しかも、同沈澱
分離槽には、分離浮上した油脂成分を、分離内槽側へ返
送する油脂戻し管を具備せしめていることを特徴とする
油水分離装置を提供せんとするものである。According to the present invention, there is provided a separation tank having a double structure in which a separation inner tank having a bottom portion and having a lower opening is formed inside a tank having a bottom and having a lower opening. A wastewater mixed with animal and vegetable oils is supplied to the separation inner tank side of the separation tank to enable separation into oil and fat components, primary intermediate water and sludge, and the primary intermediate taken out from the separation outer tank side. In addition to a mixing device that injects and mixes a neutralizing agent such as caustic soda into water, a sedimentation separation tank that separates the coagulated intermediate water mixed with the neutralizing agent into oil and fat components and purified water is provided. The present invention provides an oil / water separation device having an oil / fat return pipe for returning an oil / fat component separated and floated to the inner side of the separation tank.
【0006】[0006]
【実施例】本発明の実施例を図面に基づき具体的に説明
すると、1はレストランなどより排出される廃水Aを浄
水Bと、油脂成分及び汚泥などの不純物Cとに分離する
油水分離装置である。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described in detail with reference to the drawings. Reference numeral 1 denotes an oil / water separator for separating waste water A discharged from a restaurant or the like into purified water B and impurities C such as fats and oils and sludge. is there.
【0007】2は分離槽であって、同分離槽2は、底部
3を有しタンク状に形成された分離外槽4の内部に、下
側開口部5を有する分離内槽6を位置させて二重構造と
している。そして、同分離槽2の上部には、分離内槽6
の内室6-1 に廃水Aを導入する流入管7を設けている。Reference numeral 2 denotes a separation tank. In the separation tank 2, a separation inner tank 6 having a lower opening 5 is located inside a separation outer tank 4 having a bottom 3 and formed in a tank shape. It has a double structure. The upper part of the separation tank 2 is provided with an inner separation tank 6.
An inflow pipe 7 for introducing wastewater A is provided in the inner chamber 6-1.
【0008】また、流入管7の基端には、廃水投入口に
廃水Aを投入するポンプ手段8を設けている。9は分離
内槽6の内部で中間位置に設置するヒーター、10は二重
構造となっている分離槽2の分離外槽4と分離内槽6と
の間に形成された外室であって、分離内槽6により分離
された一次中間水Dが貯溜される。At the base end of the inflow pipe 7, there is provided a pump means 8 for introducing wastewater A into a wastewater inlet. 9 is a heater installed at an intermediate position inside the inner separation tank 6, and 10 is an outer chamber formed between the outer separation tank 4 and the inner separation tank 6 of the separation tank 2 having a double structure. The primary intermediate water D separated by the separation inner tank 6 is stored.
【0009】11は分離外槽4の底部に設ける汚泥物排出
パイプ、12は分離内槽6の上部位置より外部に向けて水
平状に突設した油脂取出管、13は油脂取出管12の先端に
接続され、かつ、微細目状スクリーン14を有する濾過
槽、15は濾過槽13に接続する油脂貯溜槽であって、ヒー
ター16及び汚泥物排水パイプ17を設置している。Reference numeral 11 denotes a sludge discharge pipe provided at the bottom of the outer separation tank 4, 12 denotes an oil / fat extraction pipe projecting horizontally from an upper position of the inner separation tank 6 to the outside, and 13 denotes a tip of the oil / fat extraction pipe 12. , And a filtration tank 15 having a fine-meshed screen 14, and 15 is an oil / fat storage tank connected to the filtration tank 13, in which a heater 16 and a sludge drainage pipe 17 are installed.
【0010】18は分離外槽4の外室10より一次中間水D
を取出す取出口であって、中和剤などを混合する混和装
置19に接続している。Reference numeral 18 denotes a primary intermediate water D from the outer chamber 10 of the outer separation tank 4.
It is an outlet for taking out, and is connected to a mixing device 19 for mixing a neutralizing agent and the like.
【0011】20は苛性ソーダなどの中和剤Eを容れた中
和剤槽で、中和剤Eはパイプ21及び定量ポンプ22により
混和装置19側へ送るようにしている。23は撹拌機、24は
パック等の凝集剤Fを収納した凝集剤槽であって、凝集
剤Fは、パイプ25及び定量ポンプ26により混和装置19側
へ送られる。Reference numeral 20 denotes a neutralizing agent tank containing a neutralizing agent E such as caustic soda. The neutralizing agent E is sent to the mixing device 19 by a pipe 21 and a metering pump 22. Reference numeral 23 denotes a stirrer, and reference numeral 24 denotes a flocculant tank containing a flocculant F such as a pack. The flocculant F is sent to the mixing device 19 by a pipe 25 and a metering pump 26.
【0012】27は凝集補助剤Gを収納した凝集補助剤槽
であって、上記と同様に凝集補助剤Gはパイプ28と定量
ポンプ29により混和装置19側へ送られる。Reference numeral 27 denotes a coagulation aid tank containing the coagulation aid G. The coagulation aid G is sent to the mixing device 19 by a pipe 28 and a metering pump 29 in the same manner as described above.
【0013】30は沈澱分離槽であって、同沈澱分離槽30
は、沈澱分離外槽31の内部に沈澱分離内槽32を位置させ
て二重構造としている。19A は混和装置19から排出され
る凝集中間水A-1 を沈澱分離槽30内に導く供給パイプ、
33は沈澱分離内槽32の下側開口部、34は沈澱分離外槽31
と沈澱分離内槽32との間に形成された外室であって、沈
澱分離内槽32により分離された二次中間水Hが貯溜され
る。35は沈澱分離外槽31の底部に設ける汚泥物排出パイ
プ、36は沈澱分離内槽32の内部側の上部位置37と、前記
分離内槽6の内部とを接続する油脂戻し管であって、同
油脂戻し管36により沈澱分離内槽32内に溜った油脂成分
などを分離内槽6に向けて排出することができる。Reference numeral 30 denotes a sedimentation / separation tank.
Has a double structure in which the inner precipitation separation tank 32 is positioned inside the outer precipitation separation tank 31. 19A is a supply pipe for guiding the coagulated intermediate water A-1 discharged from the mixing device 19 into the precipitation / separation tank 30,
33 is a lower opening of the inner tank 32 for sedimentation separation, and 34 is an outer tank 31 for the sedimentation separation.
And the secondary intermediate water H separated by the internal precipitation separation tank 32. Reference numeral 35 denotes a sludge discharge pipe provided at the bottom of the outer tank 31 for sedimentation separation. Reference numeral 36 denotes an oil / fat return pipe connecting an upper position 37 on the inner side of the inner tank 32 for sedimentation separation and the inside of the inner tank 6 for separation. The oil / fat component or the like accumulated in the inner precipitation separation tank 32 can be discharged toward the inner separation tank 6 by the oil / fat return pipe 36.
【0014】38は、沈澱分離槽30の外室34より二次中間
水Hを外部に取出す取出パイプで、同取出パイプ38の後
端は、下水道に接続されている。39は沈澱分離槽32の内
部で中間位置に設置するヒーターである。Reference numeral 38 denotes an outlet pipe for taking out the secondary intermediate water H from the outer chamber 34 of the precipitation / separation tank 30, and the rear end of the outlet pipe 38 is connected to a sewer. Reference numeral 39 denotes a heater installed at an intermediate position inside the precipitation separation tank 32.
【0015】本発明の実施例は上記のように構成されて
おり、レストランなどよりは排出された廃水Aは、ポン
プ手段8によって分離槽2内の分離内槽6に供給され
る。The embodiment of the present invention is configured as described above, and the wastewater A discharged from a restaurant or the like is supplied to the inner separation tank 6 in the separation tank 2 by the pump means 8.
【0016】そして、同分離内槽6に貯溜された廃水A
はヒーター9により加熱され、汚泥物は底部に沈澱して
汚泥物排出パイプ11より外部に排出される。The wastewater A stored in the inner separation tank 6
Is heated by the heater 9, and the sludge precipitates at the bottom and is discharged outside through the sludge discharge pipe 11.
【0017】また、廃水A中の油脂成分は上部に浮いた
状態となり、油脂取出管12により濾過槽13の微細目状ス
クリーン14により濾過されて油脂貯溜槽15へ送られる。The grease component in the waste water A floats on the top, is filtered by the grease extraction pipe 12 through the fine mesh screen 14 of the filtration tank 13, and is sent to the grease storage tank 15.
【0018】また、分離槽2内にて分離された一次中間
水Dは、分離内槽6の下側開口部5を通って分離外槽4
の外室10に貯溜される。The primary intermediate water D separated in the separation tank 2 passes through the lower opening 5 of the separation inner tank 6 and passes through the separation outer tank 4.
Is stored in the outer room 10.
【0019】上記一次中間水Dは、取出口18を通って混
和装置19側へ排出されて、同混和装置19にて、中和剤E
や凝集剤F及び凝集補助剤Gを混和して凝集一次中間水
A-1を供給パイプ19A を介して沈澱分離槽30内へ送り込
む。The primary intermediate water D is discharged to the mixing device 19 through the outlet 18, and the neutralizing agent E is mixed in the mixing device 19.
And coagulant F and coagulant G by mixing
A-1 is fed into the precipitation / separation tank 30 via the supply pipe 19A.
【0020】次に、沈澱分離槽30の沈澱分離内槽32に供
給された凝集一次中間水A-1 は、沈澱分離内槽32内にて
沈澱分離されて油脂成分と汚泥及び二次中間水Hとに分
離される。Next, the coagulated primary intermediate water A-1 supplied to the inner sedimentation separation tank 32 of the sedimentation separation tank 30 is sedimented and separated in the inner sedimentation separation tank 32, and the oil and fat component, the sludge, and the second intermediate water are separated. H.
【0021】そして、沈澱分離槽30の外室34に貯溜され
た二次中間水Hは、上澄水としてパイプ38を介して浄水
が排出される。The secondary intermediate water H stored in the outer chamber 34 of the precipitation / separation tank 30 is discharged as purified water through a pipe 38 as supernatant water.
【0022】また、沈澱分離槽30内の沈澱分離内槽32に
浮上して貯溜された油脂成分や浮渣44は、油脂戻し管36
を介して分離内槽6へ戻される。The fat and oil component and the floating residue 44 floating and stored in the inner precipitation separation tank 32 in the precipitation and separation tank 30 are removed from the oil and fat return pipe 36.
Is returned to the inner tank for separation 6.
【0023】以上の如く、上記実施例においては、底部
3を有しタンク状に形成され分離外槽4の内部に、下側
開口部5を有する分離内槽6を位置させて二重構造とし
た分離槽2を設けて、同分離内槽6に、動植物油が混入
された廃水Aを供給して、油脂成分と一次中間水Dとに
分離可能とし、かつ、分離外槽4側より取り出した一次
中間水Dに苛性ソーダなどの中和剤Eを注入混合する混
和装置19を設けると共に、中和剤が混合された凝集中間
水A-1 を沈澱・浮上分離する沈澱分離槽30を設けたもの
であるから、レストランなどから排出される廃水は、同
廃水中に含まれた遊離状態の動植物油や残飯などが二重
構造の分離槽2により確実に分離されて一次中間水が取
り出され、さらに、同一次中間水は、混和装置19におい
ては中和剤などの注入によって沈澱分離槽内での分離が
迅速に、かつ、確実に行われるものである。As described above, in the above embodiment, the separation inner tank 6 having the bottom 3 and formed in the shape of a tank and having the lower opening 5 is positioned inside the outer separation tank 4 to form a double structure. The separation tank 2 is provided, and wastewater A containing animal and vegetable oils is supplied to the separation inner tank 6 so that it can be separated into the oil and fat component and the primary intermediate water D, and is taken out from the separation outer tank 4 side. A mixing device 19 is provided for injecting and mixing a neutralizing agent E such as caustic soda into the primary intermediate water D, and a sedimentation separation tank 30 is provided for separating / floating the coagulated intermediate water A-1 mixed with the neutralizing agent. Since the wastewater discharged from restaurants, etc., the separated animal and vegetable oils and residual rice contained in the wastewater are surely separated by the double-structure separation tank 2, and the primary intermediate water is taken out. Further, the same intermediate water is injected into the mixing device 19 with a neutralizing agent or the like. Thus, the separation in the precipitation separation tank is performed quickly and reliably.
【0024】そして、廃水から油脂成分をとり出して脂
肪酸工業原料としての脂肪酸を容易に製造できるもので
ある。[0024] The fatty acid component can be easily produced from the wastewater by extracting the fat component from the wastewater.
【0025】また、廃水の処理が連続的に可能であり、
かつ、処理水の質が安定していると共に、処理コストを
節減できるものである。Further, it is possible to continuously treat wastewater,
In addition, the quality of the treated water is stable and the treatment cost can be reduced.
【0026】しかも、上記油水分離装置は廃水を自動的
に処理できるから労力が少なくてすみ、また安全であ
る。Moreover, the oil-water separator can automatically treat the wastewater, so that it requires less labor and is safe.
【0027】[0027]
【発明の効果】本発明によれば、底部を有しタンク状に
形成され分離外槽の内部に、下側開口部を有する分離内
槽を位置させて二重構造とした分離槽を設けて、同分離
槽の分離内槽側に、動植物油が混入された廃水を供給し
て、油脂成分と一次中間水とに分離可能とし、かつ、分
離外槽側より取り出した一次中間水に苛性ソーダなどの
中和剤を注入混合する混和装置を設けると共に、中和剤
が混合された凝集中間水を分離する沈澱分離槽を設けた
ものであるから、レストランなどから排出される廃水
は、同廃水中に含まれた動植物油や残飯などが二重構造
の分離槽により確実に分離されて一次中間水が取り出さ
れ、さらに、同一次中間水は、混和装置において中和剤
などの注入によって沈澱分離槽内での分離が迅速に、か
つ、確実に行われるものである。According to the present invention, a separation tank having a double structure is provided by positioning a separation inner tank having a bottom portion and formed in a tank shape and having a lower opening inside a separation outer tank. The wastewater mixed with animal and vegetable oils is supplied to the separation inner tank side of the separation tank to enable separation into oil and fat components and the primary intermediate water, and the primary intermediate water taken out from the separation outer tank side to caustic soda etc. Since a mixing device for injecting and mixing the neutralizing agent is provided and a sedimentation separation tank for separating the coagulated intermediate water mixed with the neutralizing agent is provided, wastewater discharged from restaurants and the like is The animal and vegetable oils and garbage contained in the water are surely separated by the double-structured separation tank, the primary intermediate water is taken out, and the same intermediate water is separated into the sedimentation separation tank by injection of a neutralizing agent in a mixing device. Separation is quickly and reliably performed within Than it is.
【0028】そして、廃水から油脂成分をとり出して脂
肪酸工業原料を容易に製造できるものである。The fat and oil component is taken out from the waste water to easily produce a fatty acid industrial raw material.
【0029】また、廃水の処理が連続的に可能であり、
かつ、処理水の質が安定してよくなると共に、処理コス
トを節減できるものである。Further, it is possible to continuously treat wastewater,
In addition, the quality of the treated water can be stabilized and improved, and the treatment cost can be reduced.
【0030】しかも、上記油分離装置は廃水を自動的に
処理できるから労力が少なくてすみ、また安全である。In addition, the oil separation device can automatically treat wastewater, so that it requires less labor and is safe.
【図1】本発明に係る油水分離装置を示す概略側面図。FIG. 1 is a schematic side view showing an oil-water separation device according to the present invention.
A 廃水 A-1 凝集中間水 D 一次中間水 E 中和剤 1 油水分離装置 2 分離槽 3 底部 4 分離外槽 6 分離内槽 30 沈澱分離槽 36 油脂戻し管 A Wastewater A-1 Coagulated intermediate water D Primary intermediate water E Neutralizer 1 Oil / water separator 2 Separation tank 3 Bottom 4 Separation outer tank 6 Separation inner tank 30 Precipitation separation tank 36 Oil return pipe
Claims (1)
外槽(4) の内部に、下側開口部(5) を有する分離内槽
(6) を位置させて二重構造とした分離槽(2) を設けて、
同分離槽(2) の分離内槽(6) 側に、動植物油が混入され
た廃水(A) を供給して、油脂成分と一次中間水(D) 及び
汚泥とに分離可能とし、かつ、分離外槽(4) 側より取り
出した一次中間水(D) に苛性ソーダなどの中和剤(E) を
注入混合する混和装置(19)を設けると共に、中和剤(E)
が混合された凝集中間水(A-1) を油脂成分と浄水とに分
離する沈澱分離槽(30)を設け、しかも、同沈澱分離槽(3
0)には、分離浮上した油脂成分を、分離内槽(6) 側へ返
送する油脂戻し管(36)を具備せしめていることを特徴と
する油水分離装置。1. A separation inner tank having a bottom (3) and formed in a tank shape and having a lower opening (5) inside a separation outer tank (4).
(6) is located and a separation tank (2) with a double structure is provided.
The wastewater (A) mixed with animal and vegetable oils is supplied to the separation tank (6) side of the separation tank (2) so that the oil and fat component can be separated into primary intermediate water (D) and sludge, and A mixing device (19) for injecting and mixing a neutralizing agent (E) such as caustic soda into the primary intermediate water (D) taken out from the outer separation tank (4) side is provided, and the neutralizing agent (E)
A sedimentation separation tank (30) for separating the coagulated intermediate water (A-1) into which the oil and fat components and purified water have been mixed.
0) An oil / water separation device comprising an oil / fat return pipe (36) for returning the separated and floated oil / fat component to the inner separation tank (6).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4288897A JP2580449B2 (en) | 1992-10-27 | 1992-10-27 | Oil-water separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4288897A JP2580449B2 (en) | 1992-10-27 | 1992-10-27 | Oil-water separator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH06134207A JPH06134207A (en) | 1994-05-17 |
| JP2580449B2 true JP2580449B2 (en) | 1997-02-12 |
Family
ID=17736204
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4288897A Expired - Lifetime JP2580449B2 (en) | 1992-10-27 | 1992-10-27 | Oil-water separator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2580449B2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20050043555A1 (en) * | 2000-05-02 | 2005-02-24 | Garro Juan Miguel | Production of high grade and high concentration of free fatty acids from residual residual oils, fats and greases |
| US8900460B2 (en) | 2011-09-29 | 2014-12-02 | Cameron International Corporation | Method to process effluent brine and interface rag from an oil dehydration/desalting system |
| CN108905290B (en) * | 2018-09-25 | 2023-09-26 | 江西中医药大学 | Oil-water separator with interception device and volatile oil extraction system |
-
1992
- 1992-10-27 JP JP4288897A patent/JP2580449B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH06134207A (en) | 1994-05-17 |
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