EP0098811B1 - Method of decontaminating electro-mechanic apparatus from polychlorobiphenyl - Google Patents

Method of decontaminating electro-mechanic apparatus from polychlorobiphenyl Download PDF

Info

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
Application number
EP83830130A
Other languages
German (de)
French (fr)
Other versions
EP0098811B2 (en
EP0098811A1 (en
Inventor
Aurelio Colombini
Mario Coppo
Vittorio Colombini
Enrico Colombo
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Srl SIREA
Original Assignee
Srl SIREA
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=11193047&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=EP0098811(B1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Srl SIREA filed Critical Srl SIREA
Priority to AT83830130T priority Critical patent/ATE22808T1/en
Publication of EP0098811A1 publication Critical patent/EP0098811A1/en
Publication of EP0098811B1 publication Critical patent/EP0098811B1/en
Application granted granted Critical
Publication of EP0098811B2 publication Critical patent/EP0098811B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B08CLEANING
    • B08BCLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B3/00Cleaning by methods involving the use or presence of liquid or steam
    • B08B3/04Cleaning involving contact with liquid
    • B08B3/08Cleaning involving contact with liquid the liquid having chemical or dissolving effect
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G21/00Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents
    • C10G21/006Refining 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

The method of decontaminating electro-mechanical apparatus from polychlorobyphenyl comprises the steps of: - maintaining the apparatus to be decontaminated submerged in a sealed chamber in vapours of a suitable solvent; and - constantly changing the pressure and temperature of this solvent so as to permit at any time a condensation of the solvent vapours on the surfaces under treatment. The solvent vapours can be produced inside the sealed chamber and, by providing a top condenser, a reflux washing can be obtained, or the vapours can be produced outside the sealed chamber and then injected therein at the required pressure and temperature.

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)

1. Method of decontaminating an electrical or mechanical apparatus contaminated with polychlorobiphenyl using a solvent for polychlorobiphenyl which is chemically inert thereto, characterised 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.
2. Method as claimed in claim 1, characterized in that the solvent vapours are generated in the sealed chamber by associated heating means.
3. Method as claimed in claim 2, characterized in that the solvent vapours are generated by heating means and condensed at the top of the sealed chamber so as to perform a reflux washing of the apparatus.
4. Method as claimed in claim 1, characterized in that the solvent vapours are generated outside the sealed chamber and then injected therein to wash the apparatus.
5. Method as claimed in any one of claims 1-4, characterized in that the solvent is non-toxic and is also compatible with the apparatus materials and has a distillation temperature lower than that of PCB.
6. Method as claimed in any one of claims 1-4, characterized in that the distillation temperature of the solvent is lower than the maximum tem- peratue tolerable by the apparatus to be decontaminated and higher than the room temperature for handling and conservation facility thereof.
7. Method as claimed in any one of the preceding claims, characterized in that dearomated heptane or trichloroethane is employed as solvent.
8. Method as claimed in any one of the preceding claims, characterized in that the temperature of the solvent vapours is increased stepwise as a function of the average temperature of the apparatus to be decontaminated.
EP83830130A 1982-07-02 1983-06-23 Method of decontaminating electro-mechanic apparatus from polychlorobiphenyl Expired - Lifetime EP0098811B2 (en)

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)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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

Cited By (5)

* Cited by examiner, † Cited by third party
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

Similar Documents

Publication Publication Date Title
EP0098811B1 (en) Method of decontaminating electro-mechanic apparatus from polychlorobiphenyl
US4425949A (en) Process for removing undesirable substances from electrical devices
US4443269A (en) Tool decontamination method
US5011542A (en) Method and apparatus for treating objects in a closed vessel with a solvent
US5003143A (en) Microwave sludge drying apparatus and method
US4808319A (en) Method for removing a slime deposit from packing material inside a tower
EP0454873B1 (en) Drying method and apparatus therefor
US4289586A (en) Solvent recovery method
US4483717A (en) Method of removing adsorbent contaminants from electrical apparatus
EP0221028B1 (en) A process for the decontamination of apparatus or other materials contaminated by pcb or other toxic and noxious substances
JP5841579B2 (en) Method for separating and recovering waste liquid containing radionuclides
US4204913A (en) Solvent recovery apparatus
DE4011877A1 (en) Heat pump procedure for distn. and drying - has semiconductor heat pump to evaporate and condense liq. in system which requires little maintenance and can be operated by solar power
US4814021A (en) Apparatus and method for reclassifying electrical apparatus contaminated with PCB
US4790337A (en) Apparatus for removing PCB's from electrical apparatus
US4759710A (en) Apparatus for melting a solder by vapor-phase treatment
EP0109366A1 (en) Method of decontaminating mineral oils and dielectric silicone fluids
EP0321469B1 (en) Reclassification of electrical apparatus contaminated with pcb
RU2187858C1 (en) Process of cleaning of transformer of electric insulation fluid based on polychlorobiphenyl and device for its implementation
EP0976461B1 (en) Method of and apparatus for removing oil from a waste object
US4500363A (en) Method of extracting perchlorethylene from dry cleaner filter cartridges
US4743380A (en) Solvent recovery system
US4913178A (en) Process and apparatus for removing PCB's from electrical apparatus
EP0281680A1 (en) Method of cleaning a spent fuel assembly
JP4295565B2 (en) How to recover hazardous insulating oil

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Designated state(s): AT BE CH DE FR GB LI LU NL SE

17P Request for examination filed

Effective date: 19840704

RAP1 Party data changed (applicant data changed or rights of an application transferred)

Owner name: S.R.L. SIREA

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE CH DE FR GB LI LU NL SE

REF Corresponds to:

Ref document number: 22808

Country of ref document: AT

Date of ref document: 19861115

Kind code of ref document: T

ET Fr: translation filed
REF Corresponds to:

Ref document number: 3366842

Country of ref document: DE

Date of ref document: 19861120

PLBI Opposition filed

Free format text: ORIGINAL CODE: 0009260

26 Opposition filed

Opponent name: MICAFIL AG

Effective date: 19870713

Opponent name: TRANSFORMATOREN UNION AKTIENGESELLSCHAFT

Effective date: 19870710

NLR1 Nl: opposition has been filed with the epo

Opponent name: MICAFIL AG

Opponent name: TRANSFORMATOREN UNION AKTIENGESELLSCHAFT

PLAB Opposition data, opponent's data or that of the opponent's representative modified

Free format text: ORIGINAL CODE: 0009299OPPO

R26 Opposition filed (corrected)

Opponent name: SIEMENS AKTIENGESELLSCHAFT, BERLIN UND MUENCHEN *

Effective date: 19870710

NLXE Nl: other communications concerning ep-patents (part 3 heading xe)

Free format text: IN PAT.BUL.18/87,PAGE 2357:CORR.:SIEMENS AKTIENGESELLSCHAFT

PUAH Patent maintained in amended form

Free format text: ORIGINAL CODE: 0009272

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: PATENT MAINTAINED AS AMENDED

27A Patent maintained in amended form

Effective date: 19900613

AK Designated contracting states

Kind code of ref document: B2

Designated state(s): AT BE CH DE FR GB LI LU NL SE

NLR2 Nl: decision of opposition
ET3 Fr: translation filed ** decision concerning opposition
NLR3 Nl: receipt of modified translations in the netherlands language after an opposition procedure
EPTA Lu: last paid annual fee
EAL Se: european patent in force in sweden

Ref document number: 83830130.7

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: SE

Payment date: 20000508

Year of fee payment: 18

Ref country code: GB

Payment date: 20000508

Year of fee payment: 18

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: AT

Payment date: 20000519

Year of fee payment: 18

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 20000529

Year of fee payment: 18

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: LU

Payment date: 20000605

Year of fee payment: 18

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: CH

Payment date: 20000609

Year of fee payment: 18

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 20000629

Year of fee payment: 18

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: NL

Payment date: 20000630

Year of fee payment: 18

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LU

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20010623

Ref country code: GB

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20010623

Ref country code: AT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20010623

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20010624

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20010630

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20010630

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: BE

Payment date: 20010817

Year of fee payment: 19

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20020101

EUG Se: european patent has lapsed

Ref document number: 83830130.7

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 20010623

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20020228

NLV4 Nl: lapsed or anulled due to non-payment of the annual fee

Effective date: 20020101

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20020403

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: BE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20020630

BERE Be: lapsed

Owner name: S.R.L. *SIREA

Effective date: 20020630