WO2006026849A1 - Method of foam emulsions well cleanout for gas well - Google Patents

Method of foam emulsions well cleanout for gas well Download PDF

Info

Publication number
WO2006026849A1
WO2006026849A1 PCT/CA2005/001294 CA2005001294W WO2006026849A1 WO 2006026849 A1 WO2006026849 A1 WO 2006026849A1 CA 2005001294 W CA2005001294 W CA 2005001294W WO 2006026849 A1 WO2006026849 A1 WO 2006026849A1
Authority
WO
WIPO (PCT)
Prior art keywords
compressed air
foam
pressure
foaming solution
emulsifier apparatus
Prior art date
Application number
PCT/CA2005/001294
Other languages
French (fr)
Inventor
Al Leduc
Original Assignee
Al Leduc
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=36035870&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=WO2006026849(A1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Al Leduc filed Critical Al Leduc
Publication of WO2006026849A1 publication Critical patent/WO2006026849A1/en
Priority to US11/683,395 priority Critical patent/US7278488B2/en

Links

Classifications

    • EFIXED CONSTRUCTIONS
    • E21EARTH DRILLING; MINING
    • E21BEARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B21/00Methods or apparatus for flushing boreholes, e.g. by use of exhaust air from motor
    • E21B21/14Methods or apparatus for flushing boreholes, e.g. by use of exhaust air from motor using liquids and gases, e.g. foams
    • EFIXED CONSTRUCTIONS
    • E21EARTH DRILLING; MINING
    • E21BEARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B37/00Methods or apparatus for cleaning boreholes or wells

Definitions

  • the present invention relates to a method of well cleanout for a gas well, which uses a foam emulsion as the cleaning medium.
  • An emulsifier apparatus having a compressed air inlet, a foaming solution inlet and a foam outlet, he compressed air inlet is connected to a source of compressed air capable of supplying compressed air to the emulsifier apparatus within a range of selected pressures.
  • the foaming solution is connected to a source of foaming solution capable of supplying foaming solution to the emulsifier apparatus within a range of selected pressures.
  • the foam outlet is connected to a discharge conduit supplying foam to a gas well.
  • the production of foam is initiated out of the foam outlet of the emuisifier apparatus by supplying compressed air to the emuisifier apparatus through the compressed air inlet at a rate of approximately 300 to 400 c.f.m. and at pressures within a range of 175 p.s.i and 375 p.s.i. and foaming solution is supplied to the emuisifier apparatus through the foaming solution inlet at a rate of approximately 10 to 15 litres per minute and at pressures sufficient to overcome internal pressure within the emuisifier apparatus caused by the inflow of compressed air through the compressed air inlet.
  • the pressure of compressed air supplied to the emuisifier apparatus through the compressed air inlet is increased with a corresponding increase in the pressure of foaming solution supplied to the foaming solution inlet until sufficient pressure is generated to force foam exiting the foam outlet along the discharge conduit and down the gas well with an average density of approximately 1 KPA per meter, while monitoring gas well pressure and varying compressed air pressure and foam density to ensure that pressure is always maintained at less than 80% of well pressure.
  • FIGURE 1 is a side view in section of the emuisifier apparatus constructed in accordance with the teachings of the present invention
  • FIGURE 2 is a side plan view of the emuisifier apparatus of FIGURE 1 connected to a well;
  • FIGURE 3 is a perspective view in section of the mixing chamber.
  • FIGURE 1 there is shown an emulsifier apparatus 12 having a compressed air inlet 14, a foaming solution inlet 16 and a foam outlet 18.
  • compressed air inlet 14 is connected to a source of compressed air 20 capable of supplying compressed air to emulsifier apparatus 12 within a range of selected pressures.
  • Foaming solution inlet 16 is connected to a source of foaming solution capable of supplying foaming solution to emulsifier apparatus 12 within a range of selected pressures.
  • source of foaming solution 22 may comprise multiple tank 23 and 25. As depicted, tank 23 is used to hold the foaming agent and tanks 25 are used to hold water necessary for mixing on site to form the foaming solution.
  • Foam outlet 18 is connected to a discharge conduit 24 supplying foam to a gas well 26.
  • a bypass line 27 may be included for the compressed air, in order to provide an option of using compressed air on the gas well without foam.
  • a series of control valves 29 and ball valves 31 allow the user to control the flow of compressed air, foam, and foaming solution through emulsifier apparatus 12.
  • some sections of the piping are flex piping 34 and others are rigid piping 36 to improve the operation. The various sections are joined by unions 38.
  • foam outlet 18 of emulsifier apparatus 12 by supplying compressed air to emulsifier apparatus 12 through compressed air inlet 14 at a rate of approximately 300 to 400 c.f.m. and at pressures within a range of 175 p.s.i and 375 p.s.i.
  • foaming solution is supplied to emulsifier apparatus 12 through foaming solution inlet 16 at a rate of approximately 10 to 15 litres per minute and at pressures sufficient to overcome internal pressure within emulsifier apparatus 12 caused by the inflow of compressed air through the compressed air inlet 14.
  • the pressure of compressed air supplied to emulsifier apparatus 12 through compressed air inlet 14 is increased with a corresponding increase in the pressure of foaming solution supplied to foaming solution inlet 16. This is done until sufficient pressure is generated to force foam exiting foam outlet 18 along discharge conduit 24 and down gas well 26 with an average density of approximately 1 KPA per meter.
  • the gas well pressure is monitored while this happens and the compressed air pressure and foam density are varied to ensure that pressure is always maintained at less than 80% of well pressure.
  • a return tank 28 may also be included to capture the foam after being used in gas well 26.
  • emulsifier apparatus 12 have a series of axially spaced mixing plates 30 having holes
  • Holes 32 in adjacent mixing plates 30 are axially offset to improve emulsification.
  • Plates 30 are held in a casing 40. It is also preferable that emulsifier apparatus 12 operates without the application of heat. It will be understood that the size of the holes and the number of holes plays a role in avoiding shear degradation of the foam. It has been found that a plate diameter of about 12.7 cm with approximately 60 holes having a diameter of about 1.3 cm each is sufficient for the pressures being used to avoid shear degradation.

Abstract

A method of foam emulsion well cleanout for gas well. An emulsifier apparatus is provided having a compressed air inlet, a foaming solution inlet and a foam outlet. He compressed air inlet is connected to a source of compressed air capable of supplying compressed air to the emulsifier apparatus within a range of selected pressures. The foaming solution is connected to a source of foaming solution capable of supplying foaming solution to the emulsifier apparatus within a range of selected pressures. The foam outlet is connected to a discharge conduit supplying foam to a gas well. The production of foam is initiated out of the foam outlet of the emulsifier apparatus by supplying compressed air to the emulsifier apparatus through the compressed air inlet at a rate of approximately 300 to 400 c.f m. and at pressures within a range of 175 p.s.i and 375 p.s.i. and foaming solution is supplied to the emulsifier apparatus through the foaming solution inlet at a rate of approximately 10 to 15 litres per minute and at pressures sufficient to overcome internal pressure within the emulsifier apparatus caused by the inflow of compressed air through the compressed air inlet. The pressure of compressed air supplied to the emulsifier apparatus through the compressed air inlet is increased with a corresponding increase in the pressure of foaming solution supplied to the foaming solution inlet until sufficient pressure is generated to force foam exiting the foam outlet along the discharge conduit and down the gas well with an average density of approximately 1 KPA per meter, while monitoring gas well pressure and varying compressed air pressure and foam density to ensure that pressure is always maintained at less than 80% of well pressure.

Description

TITLE OF THE INVENTION:
Method of foam emulsion well cleanout for gas well
FIELD OF THE INVENTION The present invention relates to a method of well cleanout for a gas well, which uses a foam emulsion as the cleaning medium.
BACKGROUND OF THE INVENTION
All petroleum producing wells drilled in sand formations, eventually become clogged by sand. Foam emulsion well cleanout equipment and procedures were developed for use in oil wells and are not suited for use with gas wells. Oil, particularly heavy oil, can be more than 1000 times the weight of natural gas. The pressure and volume of foam emulsion needed for effective cleaning of an oil well, would hinder rather than aid in the production of natural gas.
All attempts to adapt oil well foam emulsion cleanout methods to gas wells have, to date, proven unsuccessful. There have been so many instances of gas wells being damaged, that the industry is presently pre-mixing foam in tanks and then injecting the foam into the well under carefully controlled pressures. Working with pre-mixed foam does not permit the crew servicing the gas well to react rapidly to changes in pressure by increasing or decreasing the density of the foam.
SUMMARY OF THE INVENTION
What is required is a method of foam emulsion well cleanout for a gas well that will permit an immediate increasing or decreasing of the density of the foam in response to changes in pressure.
According to the present invention there is provided a method of foam emulsion well cleanout for gas well. An emulsifier apparatus is provided having a compressed air inlet, a foaming solution inlet and a foam outlet, he compressed air inlet is connected to a source of compressed air capable of supplying compressed air to the emulsifier apparatus within a range of selected pressures. The foaming solution is connected to a source of foaming solution capable of supplying foaming solution to the emulsifier apparatus within a range of selected pressures. The foam outlet is connected to a discharge conduit supplying foam to a gas well. The production of foam is initiated out of the foam outlet of the emuisifier apparatus by supplying compressed air to the emuisifier apparatus through the compressed air inlet at a rate of approximately 300 to 400 c.f.m. and at pressures within a range of 175 p.s.i and 375 p.s.i. and foaming solution is supplied to the emuisifier apparatus through the foaming solution inlet at a rate of approximately 10 to 15 litres per minute and at pressures sufficient to overcome internal pressure within the emuisifier apparatus caused by the inflow of compressed air through the compressed air inlet. The pressure of compressed air supplied to the emuisifier apparatus through the compressed air inlet is increased with a corresponding increase in the pressure of foaming solution supplied to the foaming solution inlet until sufficient pressure is generated to force foam exiting the foam outlet along the discharge conduit and down the gas well with an average density of approximately 1 KPA per meter, while monitoring gas well pressure and varying compressed air pressure and foam density to ensure that pressure is always maintained at less than 80% of well pressure.
Other advantages will be apparent from the description below.
BRIEF DESCRIPTION OF THE DRAWINGS
These and other features of the invention will become more apparent from the following description in which reference is made to the appended drawings, the drawings are for the purpose of illustration only and are not intended to in any way limit the scope of the invention to the particular embodiment or embodiments shown, wherein: FIGURE 1 is a side view in section of the emuisifier apparatus constructed in accordance with the teachings of the present invention;
FIGURE 2 is a side plan view of the emuisifier apparatus of FIGURE 1 connected to a well; and
FIGURE 3 is a perspective view in section of the mixing chamber.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT
The preferred embodiment, a method of foam emulsion well cleanout for gas will now be described with reference to FIGURES 1 and 2.
Referring now to FIGURE 1, there is shown an emulsifier apparatus 12 having a compressed air inlet 14, a foaming solution inlet 16 and a foam outlet 18. Referring to FIGURE 2, compressed air inlet 14 is connected to a source of compressed air 20 capable of supplying compressed air to emulsifier apparatus 12 within a range of selected pressures. Foaming solution inlet 16 is connected to a source of foaming solution capable of supplying foaming solution to emulsifier apparatus 12 within a range of selected pressures. As shown in FIGURE 2, source of foaming solution 22 may comprise multiple tank 23 and 25. As depicted, tank 23 is used to hold the foaming agent and tanks 25 are used to hold water necessary for mixing on site to form the foaming solution. Foam outlet 18 is connected to a discharge conduit 24 supplying foam to a gas well 26. Referring again to FIGURE 1, a bypass line 27 may be included for the compressed air, in order to provide an option of using compressed air on the gas well without foam. A series of control valves 29 and ball valves 31 allow the user to control the flow of compressed air, foam, and foaming solution through emulsifier apparatus 12. In addition, some sections of the piping are flex piping 34 and others are rigid piping 36 to improve the operation. The various sections are joined by unions 38. Once the above connections are made, the production of foam is initiated out of foam outlet 18 of emulsifier apparatus 12 by supplying compressed air to emulsifier apparatus 12 through compressed air inlet 14 at a rate of approximately 300 to 400 c.f.m. and at pressures within a range of 175 p.s.i and 375 p.s.i. At the same time, foaming solution is supplied to emulsifier apparatus 12 through foaming solution inlet 16 at a rate of approximately 10 to 15 litres per minute and at pressures sufficient to overcome internal pressure within emulsifier apparatus 12 caused by the inflow of compressed air through the compressed air inlet 14. Referring to FIGURE 2, the pressure of compressed air supplied to emulsifier apparatus 12 through compressed air inlet 14 is increased with a corresponding increase in the pressure of foaming solution supplied to foaming solution inlet 16. This is done until sufficient pressure is generated to force foam exiting foam outlet 18 along discharge conduit 24 and down gas well 26 with an average density of approximately 1 KPA per meter. The gas well pressure is monitored while this happens and the compressed air pressure and foam density are varied to ensure that pressure is always maintained at less than 80% of well pressure. A return tank 28 may also be included to capture the foam after being used in gas well 26.
Referring to FIGURE 3 while different designs may be possible, it is preferable that emulsifier apparatus 12 have a series of axially spaced mixing plates 30 having holes
32. Holes 32 in adjacent mixing plates 30 are axially offset to improve emulsification.
Plates 30 are held in a casing 40. It is also preferable that emulsifier apparatus 12 operates without the application of heat. It will be understood that the size of the holes and the number of holes plays a role in avoiding shear degradation of the foam. It has been found that a plate diameter of about 12.7 cm with approximately 60 holes having a diameter of about 1.3 cm each is sufficient for the pressures being used to avoid shear degradation.
In this patent document, the word "comprising" is used in its non-limiting sense to mean that items following the word are included, but items not specifically mentioned are not excluded. A reference to an element by the indefinite article "a" does not exclude the possibility that more than one of the element is present, unless the context clearly requires that there be one and only one of the elements.
It will be apparent to one skilled in the art that modifications may be made to the illustrated embodiment without departing from the spirit and scope of the invention as hereinafter defined in the Claims.

Claims

THE EMBODIMENTS OF THE INVENTION IN WHICH AN EXCLUSIVE PROPERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:
1. A method of foam emulsion well cleanout for gas well, comprising the steps of: providing an emulsifier apparatus having a compressed air inlet, a foaming solution inlet and a foam outlet; connecting the compressed air inlet to a source of compressed air capable of supplying compressed air to the emulsifier apparatus within a range of selected pressures; connecting the foaming solution to a source of foaming solution capable of supplying foaming solution to the emulsifier apparatus within a range of selected pressures; connecting the foam outlet to a discharge conduit supplying foam to a gas well; initiating the production of foam out of the foam outlet of the emulsifier apparatus by supplying compressed air to the emulsifier apparatus through the compressed air inlet at a rate of approximately 300 to 400 c.f.m. and at pressures within a range of 175 p.s.i and 375 p.s.i. and supplying foaming solution to the emulsifier apparatus through the foaming solution inlet at a rate of approximately 10 to 15 litres per minute and at pressures sufficient to overcome internal pressure within, the emulsifier apparatus caused by the inflow of compressed air through the compressed air inlet; increasing the pressure of compressed air supplied to the emulsifier apparatus through the compressed air inlet with a corresponding increase in the pressure of foaming solution supplied to the foaming solution inlet until sufficient pressure is generated to force foam exiting the foam outlet along the discharge conduit and down the gas well with an average density of approximately 1 KPA per meter, while monitoring gas well pressure and varying compressed air pressure and foam density to ensure that pressure is always maintained at less than 80% of well pressure.
2. The method as defined in Claim 1, the emulsifier apparatus operating without the application of heat.
3. The method as defined in Claim 1, the emulsifier apparatus having a series of axially spaced mixing plates having holes, the holes in adjacent mixing plates being axially offset
PCT/CA2005/001294 2004-09-10 2005-08-29 Method of foam emulsions well cleanout for gas well WO2006026849A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US11/683,395 US7278488B2 (en) 2004-09-10 2007-03-07 Method of generating stable foam for oil and gas well cleanouts

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CA2,481,533 2004-09-10
CA002481533A CA2481533C (en) 2004-09-10 2004-09-10 Method of foam emulsion well cleanout for gas well

Related Child Applications (1)

Application Number Title Priority Date Filing Date
US11/683,395 Continuation US7278488B2 (en) 2004-09-10 2007-03-07 Method of generating stable foam for oil and gas well cleanouts

Publications (1)

Publication Number Publication Date
WO2006026849A1 true WO2006026849A1 (en) 2006-03-16

Family

ID=36035870

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CA2005/001294 WO2006026849A1 (en) 2004-09-10 2005-08-29 Method of foam emulsions well cleanout for gas well

Country Status (3)

Country Link
US (1) US7278488B2 (en)
CA (1) CA2481533C (en)
WO (1) WO2006026849A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2601879C1 (en) * 2015-11-09 2016-11-10 Публичное акционерное общество "Татнефть" имени В.Д. Шашина Method of cleaning bottom-hole formation zone of injection wells after hydraulic fracturing

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8056636B1 (en) 2008-03-03 2011-11-15 LP Chemical Service LLC Jet pump with foam generator
US9664009B2 (en) * 2012-04-04 2017-05-30 Weatherford Technologies, LLC Apparatuses, systems, and methods for forming in-situ gel pills to lift liquids from horizontal wells

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1248355A (en) * 1969-03-13 1971-09-29 Chevron Res Method and apparatus for well cleanout
US3662828A (en) * 1970-09-11 1972-05-16 Chevron Res Through tubing well cleanout method using foam
US4913237A (en) * 1989-02-14 1990-04-03 Amoco Corporation Remedial treatment for coal degas wells

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2125245A (en) * 1935-06-28 1938-07-26 Texas Co Emulsion apparatus
US3377139A (en) * 1963-06-21 1968-04-09 Allied Chem Apparatus for preparing low density urea-formaldehyde foams
FR2214037B1 (en) * 1973-01-16 1975-10-31 Schlumberger Ltd
US4213936A (en) * 1978-08-09 1980-07-22 Robert Lodrick Foam generating and spraying apparatus
US4394289A (en) * 1981-07-01 1983-07-19 Brown Lamar W Continuous foam generating system
DE3782044T2 (en) * 1987-04-10 1993-03-25 Chugoku Kayaku MIXER.
US5356565A (en) * 1992-08-26 1994-10-18 Marathon Oil Company In-line foam generator for hydrocarbon recovery applications and its use
US6086052A (en) * 1996-12-03 2000-07-11 Rowe; Carroll G. Foam generating apparatus
US6125761A (en) * 1997-08-07 2000-10-03 Southwest Energy Inc. Zinc oxide inhibited emulsion explosives and method
US6422734B1 (en) * 1999-10-27 2002-07-23 National Gypsum Properties, Llc Static foam generating apparatus and method

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1248355A (en) * 1969-03-13 1971-09-29 Chevron Res Method and apparatus for well cleanout
US3662828A (en) * 1970-09-11 1972-05-16 Chevron Res Through tubing well cleanout method using foam
US4913237A (en) * 1989-02-14 1990-04-03 Amoco Corporation Remedial treatment for coal degas wells

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2601879C1 (en) * 2015-11-09 2016-11-10 Публичное акционерное общество "Татнефть" имени В.Д. Шашина Method of cleaning bottom-hole formation zone of injection wells after hydraulic fracturing

Also Published As

Publication number Publication date
US7278488B2 (en) 2007-10-09
US20070144742A1 (en) 2007-06-28
CA2481533A1 (en) 2006-03-10
CA2481533C (en) 2009-04-21

Similar Documents

Publication Publication Date Title
EP0703830B1 (en) Apparatus for downhole cyclone separation
AU2009256367B2 (en) Multi-point injection system for oilfield operations
CA2591580A1 (en) Simple gas scouring method and apparatus
CA2787510A1 (en) Control valve assembly
NZ575066A (en) Hybrid foam proportioning system
CN102226390A (en) Testing device for deep wells and high-temperature and high-pressure wells
US7278488B2 (en) Method of generating stable foam for oil and gas well cleanouts
WO2017079492A1 (en) Pressure-reducing choke assembly
US20210131410A1 (en) Mobile Pump System
CA2623376A1 (en) Well jet device and the operating method thereof
WO2012135555A2 (en) System and method for reducing pressure fluctuations in an oilfield pumping system
CA2692663C (en) Well jet device
US20090235730A1 (en) Method for cleaning an oil field capillary tube
EP0288106A2 (en) Foamed slurry generator
RU2516093C1 (en) Station for transfer and separation of multiphase mix
US9194216B2 (en) Manipulatable filter system
US20170259091A1 (en) Fire-fighting system
RU126802U1 (en) MULTI-PHASE MIXTURE TRANSMISSION AND SEPARATION STATION
JP2011520050A (en) Injection head for performing the injection filling process
US4126182A (en) Method for decreasing resistance to flow of crude oil up from a well or through a pipeline
US11826716B2 (en) Hydraulic mud shearing system
AU2018252927B2 (en) Inflow device
RU2138696C1 (en) Method of operation of pump ejector well pulse unit
US20240117765A1 (en) Systems, assemblies, and methods for treatment/filtration of intake air flows to a gas turbine engine of a hydraulic fracturing unit
US20240036593A1 (en) Rejected gas recovery in gas oil separation plants

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BW BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE EG ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KM KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NA NG NI NO NZ OM PG PH PL PT RO RU SC SD SE SG SK SL SM SY TJ TM TN TR TT TZ UA UG US UZ VC VN YU ZA ZM ZW

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): GM KE LS MW MZ NA SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LT LU LV MC NL PL PT RO SE SI SK TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG

121 Ep: the epo has been informed by wipo that ep was designated in this application
WWE Wipo information: entry into national phase

Ref document number: 11683395

Country of ref document: US

NENP Non-entry into the national phase

Ref country code: DE

WWP Wipo information: published in national office

Ref document number: 11683395

Country of ref document: US

32PN Ep: public notification in the ep bulletin as address of the adressee cannot be established

Free format text: NOTING OF LOSS OF RIGHTS PURSUANT TO RULE 69(1) EPC (EPO FORM 1205 DATED 01-08-2007)

122 Ep: pct application non-entry in european phase

Ref document number: 05777266

Country of ref document: EP

Kind code of ref document: A1

WWW Wipo information: withdrawn in national office

Ref document number: 5777266

Country of ref document: EP