EP0098811B1 - Method of decontaminating electro-mechanic apparatus from polychlorobiphenyl - Google Patents
Method of decontaminating electro-mechanic apparatus from polychlorobiphenyl Download PDFInfo
- Publication number
- EP0098811B1 EP0098811B1 EP83830130A EP83830130A EP0098811B1 EP 0098811 B1 EP0098811 B1 EP 0098811B1 EP 83830130 A EP83830130 A EP 83830130A EP 83830130 A EP83830130 A EP 83830130A EP 0098811 B1 EP0098811 B1 EP 0098811B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- solvent
- vapours
- temperature
- sealed chamber
- pcb
- 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
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B08—CLEANING
- B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
- B08B3/00—Cleaning by methods involving the use or presence of liquid or steam
- B08B3/04—Cleaning involving contact with liquid
- B08B3/08—Cleaning involving contact with liquid the liquid having chemical or dissolving effect
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G21/00—Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents
- C10G21/006—Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents of waste oils, e.g. PCB's containing oils
Definitions
- the present invention generally relates to a method of decontaminating from polychlorobiphenyl electro-mechanic apparatus.
- PCB polychlorobiphenyl
- the PCB absorbed by materials such as paper and wood which are normally present in most apparatus and the PCB adsorbed by the inner portion of the magnetic lamination pack or the electric windings cannot be totally removed, at least in a short time, because of its aggressiveness and therefore a portion thereof remains attached to these apparatus so that, with the passing of time, it can be dissolved in the new liquid used in substitution thereof, thereby forming a contaminating element for the latter.
- US ⁇ A ⁇ 4.008.729 discloses an apparatus for cleaning articles in volatile solvent wherein the article to be cleaned is placed in a container connected to a solvent collector with siphon and provided with a condenser.
- the solvent in the container is heated to boiling temperature to generate solvent vapours to bathe the article in solvent vapours and condensate which forms on the condenser and drips into the container to wash impurities from the article.
- the article to be cleaned is immersed in the liquid solvent up to the level of the siphon tube extending in the container and therefore the solvent vapours are not in contact with all the article, but only with the portion thereof emerging from the siphon level. Furthermore this treatment is carried out at atmospheric pressure.
- the solvent vapours are generated in a sealed chamber.
- the solvent vapours are generated by heating means and condensed at the top of the sealed chamer so as to perform a reflux washing of the apparatus.
- the solvent vapours are generated outside the sealed chamber and then injected therein to wash the apparatus.
- the solvent is non-toxic and also compatible with the apparatus materials and has a distillation temperature lower than that of PCB.
- the distillation temperature of the solvent is lower than the maximum temperature tolerable by the apparatus to be decontaminated and higher than the room temperature for handling and conservation facility thereof.
- dearomated heptane or trichioro- ethane is employed as solvent.
- the temperature of the solvent vapours is increased stepwise as a function of the average temperature of the apparatus to be decontaminated.
- the apparatus under treatment is put in a box B which is heated on the bottom and on the four lateral walls by means of jackets E through which a suitable heating fluid passes, which is fed through an inlet G, through a valve I and is discharged through an outlet H.
- a condenser L is arranged through which water flows, the temperature of which is controlled by a thermostat M controlling a water discharge valve N.
- the temperature is controlled by a thermostat F controlling the valve I and the pressure is controlled by a vacuostat 0 controlling a solvent discharge valve P, everything so as to keep constantly the apparatus A submerged in the solvent vapours under vacuum and to cause the solvent vapours to be always condensed on the walls thereof and to flow downwardly thereon thereby developing their flooding action according to the plot of Fig. 4, where T1 designates the vapour condensation temperature and T2 designates the average temperature of the apparatus A under treatment.
- the solvent used in this case is dearomated eptane which exhibits all of the above mentioned features for performing the washing operation.
- the temperature T1 is stepwise controlled as a function of the temperature T2 taken over by the apparatus A, i.e. as the temperature T2 of the apparatus A approaches to vapour condensation temperature T1, the latter is increased of a step ⁇ T, and this operation is repeated until the washing is ended.
- the box B is further provided with a solvent inlet S. a thermometer V for measuring the solvent vapour temperature and an inert gas source R connected to the box through a valve Z, a non- return safety valve Q calibrated so as to assure that the pressure inside the box B does not exceed the safety values and a drainage tube D for the gravity discharge of the polychlorobiphenyl.
- the inert gas source R during the solvent discharge operation is connected to the box B in order to avoid the air to enter therein, which could give rise to possible combustion of the hot solvent.
- the described embodiment shows a washing method with solvent reflux
- the same method could be carried out without the top condenser, or it could be otherwise carried out by providing outside the box B a solvent vapour source and then injecting the solvent vapours into the box B following the requirements for performing the washing operation.
- Figs. 2 and 3 diagrammatically show the action of the solvent on the PCB during a liquid phase washing operation and during a vapour phase washing operation, respectively.
- the area A is static and therefore there is a poor solvent substitution which, when it is saturated, stops its penetration, whereas in Fig. 3 there is a continuous solvent substitution with resulting higher penetrability into the components of the apparatus to be decontaminated.
- an automatic washing without the intervention of operators in contact with the PCB occurs.
- all the necessary equipment does not come into contact with PCB and, once the washing operation is ended, it is fully cleaned and decontaminated, with the exception of the lower PCB collecting zone.
- any possibility of environmental contamination is avoided since the system does not provide circuits for the PCB containing solvent (pumps, pipes, connectors etc.), which could give rise to contamination problems.
- the washing efficiency is very good since the solvent retains always its dissolving capacity without ever reaching the saturation and moreover the solvent can completely penetrate within interstices also of capillary nature.
- Another advantage of this invention is the very low amount of solvent required for the decontamination and easy recovery thereof since it is sufficient an amount less than 1% of the amount required for carrying out the liquid phase washing, which results in a lower cost of solvent recovery, asthis can be recovered by taking advantage of the heat supplied by the heaters by simply evacuating the box once the washing is ended and the PCB has been separated therefrom.
- the so decontaminated apparatus can then be recovered and reused by substituting forthe PCB a usual oil or a silicone oil or a liquid usually employed to this end.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Cleaning By Liquid Or Steam (AREA)
- Organic Insulating Materials (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Extraction Or Liquid Replacement (AREA)
Abstract
Description
- The present invention generally relates to a method of decontaminating from polychlorobiphenyl electro-mechanic apparatus.
- As known, for antifire purposes, fluids on the basis of polychlorobiphenyl (PCB) as insulating fluids in electrical apparatus or as hydraulic liquids in mechanical apparatus have been often used in the past. These fluids, generally a mixture of 40% of hexachlorobenzene and 60% of polychlorobiphenyl, exhibit antifire properties which assure a reliable operation of electrical or mechanical apparatus even in environments in which the fire conditions could be promoted.
- For example, there are in Italy only tens of thousands of transformators, circuit breakers and other electric apparatus still filled with this fluid and an undefined number of hydraulic apparatus almost certainly still contaminated by PCB.
- The suspected cancerous action or at any rate the harmfulness of PCB has caused the use of these fluids in the above mentioned apparatus to be suspended, which fluids are gradually substituted by other less dangerous fluids.
- The aggressiveness of fluids on the basis of PCB towards the components of these apparatus is so greatthat their decontamination becomes an extremely difficult operation and the great harmfulness thereby exhibited causes it to be more convenient to bury all the apparatus into suitably prepared pits than to try a decontamination thereof.
- Of course, for economical reasons, this has given rise to the problem of the recovery of these apparatus by trying to decontaminate them as much as possible by reducing the PCB contents at least within limits which are permissible and tolerable from the ecological standpoint.
- Recently, attempts have been made to wash the contaminated apparatus with suitable solvents in a liquid phase,.however this method has proved to be difficult, time consuming, expensive and it has not successfully.
- In fact, the PCB absorbed by materials such as paper and wood which are normally present in most apparatus and the PCB adsorbed by the inner portion of the magnetic lamination pack or the electric windings cannot be totally removed, at least in a short time, because of its aggressiveness and therefore a portion thereof remains attached to these apparatus so that, with the passing of time, it can be dissolved in the new liquid used in substitution thereof, thereby forming a contaminating element for the latter.
- US―A―4.008.729 discloses an apparatus for cleaning articles in volatile solvent wherein the article to be cleaned is placed in a container connected to a solvent collector with siphon and provided with a condenser. The solvent in the container is heated to boiling temperature to generate solvent vapours to bathe the article in solvent vapours and condensate which forms on the condenser and drips into the container to wash impurities from the article.
- In this apparatus the article to be cleaned is immersed in the liquid solvent up to the level of the siphon tube extending in the container and therefore the solvent vapours are not in contact with all the article, but only with the portion thereof emerging from the siphon level. Furthermore this treatment is carried out at atmospheric pressure.
- It is therefore the main object of the present invention to obviate the above mentioned disadvantages of the known method by providing a new method permitting the above mentioned apparatus to be decontaminated as much as possible, however within ecological acceptable limits so that the apparatus can be reused.
- It is another object of the present invention to provide a method of decontaminating from PCB electrical and mechanical apparatus, which can be carried out without the intervention of operators in contact with the PCB.
- It is still another object of the present invention to provide a method of the abovementioned kind, which assures in the most absolute way any possibility of environment contaminations.
- It is a further object of the present invention to provide a method of the abovementioned kind, which provides a quick decontaminating action so as to be inexpensive, and which can be carried out as simply as possible without requiring sophisticated and expensive equipment.
- These and other objects of the present invention, which will be more apparent from the following description, are attained according to the invention by a method of decontaminating an electrical or mechanical apparatus contaminated with polychlorobiphenyl using a solvent for polychlorobiphenyl which is chemically inert thereto, which method is characterized by:
- maintaining the apparatus to be decontaminated submerged in a sealed chamber in vapours of the solvent; and
- controlling the pressure and temperature of the solvent vapours so as to permit at all times a condensation of the solvent vapours on the surfaces under treatment.
- According to a feature of the present invention, the solvent vapours are generated in a sealed chamber.
- According to another feature of the present invention the solvent vapours are generated by heating means and condensed at the top of the sealed chamer so as to perform a reflux washing of the apparatus.
- According to a further feature of the invention, the solvent vapours are generated outside the sealed chamber and then injected therein to wash the apparatus.
- The solvent is non-toxic and also compatible with the apparatus materials and has a distillation temperature lower than that of PCB.
- Advantageously, the distillation temperature of the solvent is lower than the maximum temperature tolerable by the apparatus to be decontaminated and higher than the room temperature for handling and conservation facility thereof.
- Preferably, dearomated heptane or trichioro- ethane is employed as solvent.
- According to still another feature of the invention the temperature of the solvent vapours is increased stepwise as a function of the average temperature of the apparatus to be decontaminated.
- The invention will be now described in more detail in connection with a preferred embodiment thereof, given by way of example only and therefore not intended in a limiting sense, which is shown in the accompanying drawing, wherein:
- Fig. 1 is a diagrammatic sectioned view of a box containing the electric apparatus to be decontaminated, for example a transformer, and provided with the necessary means for carrying out the method of the invention;
- Fig. 2 diagrammatically shows the solvent action during the washing step in liquid phase;
- Fig. 3 diagrammatically shows the solvent action during the washing step in a vapour phase;
- Fig. 4 is a plot of the diagram of the solvent condensation temperature vs. time, during the washing process;
- Figs. 5 and 6 show a diagram of the PCB contents in the apparatus under treatment vs. the removal time thereof for the liquid phase washing and the vapour phase washing respectively, showing the more than good results obtained by means of the method of the invention.
- As can be seen from Fig. 1, the apparatus under treatment is put in a box B which is heated on the bottom and on the four lateral walls by means of jackets E through which a suitable heating fluid passes, which is fed through an inlet G, through a valve I and is discharged through an outlet H. On the top of the box B a condenser L is arranged through which water flows, the temperature of which is controlled by a thermostat M controlling a water discharge valve N.
- Inside the box B the temperature is controlled by a thermostat F controlling the valve I and the pressure is controlled by a vacuostat 0 controlling a solvent discharge valve P, everything so as to keep constantly the apparatus A submerged in the solvent vapours under vacuum and to cause the solvent vapours to be always condensed on the walls thereof and to flow downwardly thereon thereby developing their flooding action according to the plot of Fig. 4, where T1 designates the vapour condensation temperature and T2 designates the average temperature of the apparatus A under treatment. Preferably the solvent used in this case is dearomated eptane which exhibits all of the above mentioned features for performing the washing operation.
- As can be seen from Fig. 4, the temperature T1 is stepwise controlled as a function of the temperature T2 taken over by the apparatus A, i.e. as the temperature T2 of the apparatus A approaches to vapour condensation temperature T1, the latter is increased of a step ΔT, and this operation is repeated until the washing is ended. The box B is further provided with a solvent inlet S. a thermometer V for measuring the solvent vapour temperature and an inert gas source R connected to the box through a valve Z, a non- return safety valve Q calibrated so as to assure that the pressure inside the box B does not exceed the safety values and a drainage tube D for the gravity discharge of the polychlorobiphenyl.
- Once the washing operation is ended it is sufficient to evacuate the box B through the valve P and to condensate the solvent vapours, by recovering all the solvent through the outlet C while the removed PCB is readily discharged through the drainage tube D.
- The inert gas source R during the solvent discharge operation is connected to the box B in order to avoid the air to enter therein, which could give rise to possible combustion of the hot solvent.
- Although the described embodiment shows a washing method with solvent reflux, the same method could be carried out without the top condenser, or it could be otherwise carried out by providing outside the box B a solvent vapour source and then injecting the solvent vapours into the box B following the requirements for performing the washing operation.
- Figs. 2 and 3 diagrammatically show the action of the solvent on the PCB during a liquid phase washing operation and during a vapour phase washing operation, respectively. As can be seen from Fig. 2, the area A is static and therefore there is a poor solvent substitution which, when it is saturated, stops its penetration, whereas in Fig. 3 there is a continuous solvent substitution with resulting higher penetrability into the components of the apparatus to be decontaminated.
- By means of the method according to the invention an automatic washing without the intervention of operators in contact with the PCB occurs. During the full washing cycle all the necessary equipment does not come into contact with PCB and, once the washing operation is ended, it is fully cleaned and decontaminated, with the exception of the lower PCB collecting zone. Furthermore, any possibility of environmental contamination is avoided since the system does not provide circuits for the PCB containing solvent (pumps, pipes, connectors etc.), which could give rise to contamination problems. The washing efficiency is very good since the solvent retains always its dissolving capacity without ever reaching the saturation and moreover the solvent can completely penetrate within interstices also of capillary nature.
- The decontamination operation is extremely quick. It has been experimentally proved on a tipic series of electric transformators that the PCB embedded in the paper or wood or enclosed in too near walls forming the magnetic core or the windings thereof, is very difficult to remove (see plot of Fig. 5, wherein the curve shows the PCB decontamination efficiency with liquid phase solvent, where after about three hours of treatment the decontamination rate is about 40% of PCB) whereas, according to this method, the PCB is almost fully removed in the same time (see Fig. 6 wherein the curve shows that in the same time as in Fig. 5 the PCB has been removed in a very high percentage).
- From tests effectively carried out it has been proved that the amount of PCB remained on a transformator containing 200 Kg of insulating liquid is less than 100 gr.
- Another advantage of this invention is the very low amount of solvent required for the decontamination and easy recovery thereof since it is sufficient an amount less than 1% of the amount required for carrying out the liquid phase washing, which results in a lower cost of solvent recovery, asthis can be recovered by taking advantage of the heat supplied by the heaters by simply evacuating the box once the washing is ended and the PCB has been separated therefrom.
- The so decontaminated apparatus can then be recovered and reused by substituting forthe PCB a usual oil or a silicone oil or a liquid usually employed to this end.
- From the foregoing it will be readily apparent that the method according to this invention permits a decontamination from PCB with very high yields to be obtained, what could not be obtained till now.
Claims (8)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT83830130T ATE22808T1 (en) | 1982-07-02 | 1983-06-23 | METHOD FOR DECONTAMINATION OF ELECTROMECHANICAL DEVICE CONTAMINATED WITH POLYCHLORBIPHENYL. |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
IT2220782 | 1982-07-02 | ||
IT22207/82A IT1157287B (en) | 1982-07-02 | 1982-07-02 | PROCEDURE FOR THE POLLUTION OF ELECTRICAL-MECHANICAL EQUIPMENT FROM POLY-CHLORINE-DIPHENYL |
Publications (3)
Publication Number | Publication Date |
---|---|
EP0098811A1 EP0098811A1 (en) | 1984-01-18 |
EP0098811B1 true EP0098811B1 (en) | 1986-10-15 |
EP0098811B2 EP0098811B2 (en) | 1990-06-13 |
Family
ID=11193047
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP83830130A Expired - Lifetime EP0098811B2 (en) | 1982-07-02 | 1983-06-23 | Method of decontaminating electro-mechanic apparatus from polychlorobiphenyl |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP0098811B2 (en) |
AT (1) | ATE22808T1 (en) |
DE (1) | DE3366842D1 (en) |
IT (1) | IT1157287B (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3714312A1 (en) * | 1987-04-29 | 1988-11-10 | Siemens Ag | Process and device for cleaning electrical devices with an insulating oil in a vessel |
DE3715235A1 (en) * | 1987-05-07 | 1988-11-24 | Micafil Ag | Process and device for extracting oil or polychlorinated biphenyl from impregnated electrical components by means of a solvent, and for distillation of the solvent |
DE4128699A1 (en) * | 1991-08-29 | 1993-03-04 | Peter Warthmann | Process and equipment for solvent degreasing and cleaning - by solvent evapn. and condensn. on goods due to temp. differential, with continuous multistage treatment at increasing solvent pressure and temp. |
DE19515566A1 (en) * | 1995-03-16 | 1996-10-31 | Chugai Ro Kogyo Kaisha Ltd | Cleaning device |
Families Citing this family (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
IT1190411B (en) * | 1985-10-24 | 1988-02-16 | Ecolsir Srl | PROCEDURE FOR THE POLLUTION OF EQUIPMENT OR OTHER MATERIALS CONTAMINATED WITH PCB OR OTHER TOXIC AND HARMFUL SUBSTANCES |
DE3540425A1 (en) * | 1985-11-14 | 1987-05-21 | Transformatoren Union Ag | Process for decontaminating transformers |
EP0270928B1 (en) * | 1986-11-29 | 1992-01-15 | Asea Brown Boveri Aktiengesellschaft | Cleaning method for an insulating part |
US4879004A (en) * | 1987-05-07 | 1989-11-07 | Micafil Ag | Process for the extraction of oil or polychlorinated biphenyl from electrical parts through the use of solvents and for distillation of the solvents |
FR2615763A2 (en) * | 1987-05-27 | 1988-12-02 | Pioch Rene | IMPROVEMENT IN THE CLEANING OF COMPLEX DEVICES ENCLOSED IN A TANK BY ORIENTED VIBRATIONS |
FR2617724B1 (en) * | 1987-07-06 | 1989-11-24 | Vigneron Andre | PROCESS FOR DECONTAMINATION OF ELECTRICAL APPARATUS CONTAINING POLYCHLOROBIPHENYL RESIDUES AND DECONTAMINATION DEVICE |
FR2626582B1 (en) * | 1988-02-03 | 1990-06-22 | Sepulcre Patrick | PROCESS FOR THE REGENERATION OF MINERAL OILS AND SILICONE DIELECTRIC FLUIDS SOILED BY POLYCHLOROBIPHENYLS AND DECONTAMINATION DEVICE |
FR2634674B1 (en) * | 1988-08-01 | 1991-02-22 | Sepulcre Patrick | PROCESS FOR THE RECOVERY OF ELECTRICAL DEVICE COMPONENTS CONTAINING POLYCHLOROBIPHENYL RESIDUES AND TREATMENT DEVICES |
CH676084A5 (en) * | 1988-10-31 | 1990-12-14 | Asea Brown Boveri | |
CN1080147C (en) * | 1995-04-27 | 2002-03-06 | 中外炉工业株式会社 | Cleaning apparatus |
FR2961722B1 (en) | 2010-06-29 | 2013-02-22 | Aprochim | METHOD AND DEVICE FOR DECONTAMINATING POLLUTED MATERIALS |
ITMI20120073A1 (en) * | 2012-01-24 | 2013-07-25 | D E L Co S R L | PROCEDURE AND RELATIVE PLANT FOR THE SAFE AND FAST DECONTAMINATION OF POROUS AND NON-CONTAMINATED PCB MATERIALS |
CN103272797B (en) * | 2013-05-31 | 2016-08-31 | 陈春 | workpiece cleaning method and device |
JP6373331B2 (en) * | 2016-11-24 | 2018-08-15 | 株式会社シー・シー・アイ | Vacuum degreasing and cleaning apparatus and cleaning method thereof |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4008729A (en) * | 1972-07-28 | 1977-02-22 | George Chizinsky | Solvent article cleaner |
US4023983A (en) * | 1975-10-28 | 1977-05-17 | Collins Machinery Corporation | Vapor cleaning system |
-
1982
- 1982-07-02 IT IT22207/82A patent/IT1157287B/en active
-
1983
- 1983-06-23 DE DE8383830130T patent/DE3366842D1/en not_active Expired
- 1983-06-23 EP EP83830130A patent/EP0098811B2/en not_active Expired - Lifetime
- 1983-06-23 AT AT83830130T patent/ATE22808T1/en not_active IP Right Cessation
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3714312A1 (en) * | 1987-04-29 | 1988-11-10 | Siemens Ag | Process and device for cleaning electrical devices with an insulating oil in a vessel |
DE3715235A1 (en) * | 1987-05-07 | 1988-11-24 | Micafil Ag | Process and device for extracting oil or polychlorinated biphenyl from impregnated electrical components by means of a solvent, and for distillation of the solvent |
DE4128699A1 (en) * | 1991-08-29 | 1993-03-04 | Peter Warthmann | Process and equipment for solvent degreasing and cleaning - by solvent evapn. and condensn. on goods due to temp. differential, with continuous multistage treatment at increasing solvent pressure and temp. |
DE19515566A1 (en) * | 1995-03-16 | 1996-10-31 | Chugai Ro Kogyo Kaisha Ltd | Cleaning device |
DE19515566C2 (en) * | 1995-03-16 | 1998-10-08 | Chugai Ro Kogyo Kaisha Ltd | Cleaning device |
Also Published As
Publication number | Publication date |
---|---|
ATE22808T1 (en) | 1986-11-15 |
IT8222207A0 (en) | 1982-07-02 |
EP0098811B2 (en) | 1990-06-13 |
DE3366842D1 (en) | 1986-11-20 |
IT1157287B (en) | 1987-02-11 |
EP0098811A1 (en) | 1984-01-18 |
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