CA2293531A1 - Method and device for producing two-component reactive adhesives - Google Patents
Method and device for producing two-component reactive adhesives Download PDFInfo
- Publication number
- CA2293531A1 CA2293531A1 CA002293531A CA2293531A CA2293531A1 CA 2293531 A1 CA2293531 A1 CA 2293531A1 CA 002293531 A CA002293531 A CA 002293531A CA 2293531 A CA2293531 A CA 2293531A CA 2293531 A1 CA2293531 A1 CA 2293531A1
- Authority
- CA
- Canada
- Prior art keywords
- adhesive
- reactive
- component
- liquid
- extruder
- 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.)
- Abandoned
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/002—Methods
- B29B7/007—Methods for continuous mixing
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
- C09J5/00—Adhesive processes in general; Adhesive processes not provided for elsewhere, e.g. relating to primers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/285—Feeding the extrusion material to the extruder
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/78—Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling
- B29C48/80—Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling at the plasticising zone, e.g. by heating cylinders
- B29C48/83—Heating or cooling the cylinders
- B29C48/832—Heating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
- B29C48/07—Flat, e.g. panels
- B29C48/08—Flat, e.g. panels flexible, e.g. films
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/285—Feeding the extrusion material to the extruder
- B29C48/288—Feeding the extrusion material to the extruder in solid form, e.g. powder or granules
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/285—Feeding the extrusion material to the extruder
- B29C48/29—Feeding the extrusion material to the extruder in liquid form
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2105/00—Condition, form or state of moulded material or of the material to be shaped
- B29K2105/0097—Glues or adhesives, e.g. hot melts or thermofusible adhesives
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Adhesives Or Adhesive Processes (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
Abstract
The invention relates to a method and a device for producing reactive adhesives having at least two components, for example adhesives with moistureactivated cross-linking. According to said method at least one non-reactive adhesive component present in solid form, for example a granulate (G), or liquid form (F) and at least one reactive adhesive component present in the form of a solid, for example a granulate (G), or a liquid (F), are used. The two adhesive components are heated by pressure and friction in an endless screw in a specific proportion and mixed to produce the liquid reactive adhesive (K). The liquid reactive adhesive (K) is then applied directly to the area of application (use).
Description
~O 99/51411 PCT/E899/01232 METHOD AND DEVICE FOR PRODUCING TWO-COMPONENT REACTIVE
ADHESIVES
The invention relates to a method of producing at least two-component reactive adhesives, and a device that is subsequently integrated for processing the adhesive, for example a moisture-activated adhesive.
It is known in practice to heat and mix reactive adhesives comprising two or more components, thereby bringing them to a liquid mass, then package them gas-tight in a container, so as to preclude any air humidity;
the vacuum-packed reactive adhesive is then cooled, so it can be stored and transported in solidified form in the container. The desired processing is performed in known pre-melting devices, in which the adhesive is re--melted and then used for the application.
Disadvantages of this process are the relatively-high production costs, possible damage during the transport of the containers carrying the reactive adhesive, and the threat to the durability of the reactive adhesive due to leaks in the packaging over lengthy transport or storage periods. After the container is opened, the surface of the reactive adhesive reacts, and if the adhesive remains exposed for a long period of time, it becomes unusable.
This results in the return of the reactive adhesive, CONH'IR~1TION COpY
which, of course, incurs costs. Reactive adhesive that cannot be processed in its entirety out of a vessel and remains there becomes unusable, The period of durability begins practically at the end of the production process of the reactive adhesive:
this is critical for the optimum use of the reactive adhesive. Tn moisture-activated cross-linking adhesives, the chemical cross-linking reaction is triggered by air humidity, but also by the continuous effect of the temperature during the pre-melting and melting phase until the application.
It is an object of the invention to create a method with which a reactive adhesive is created in a single wozk step from separate components that have an unlimited shelf life, with a processing/application step following immediately afterward, and with which wasted adhesive, and thus additional costs, are avoided.
ACCOrding to the invention, this object is accomplished by the characterizing featurPS of claim 1;
the further method claims describe advantageous modifications of the solution to the object.
A further object lies in the creation of a simple, inexpensively-constructed, economically--operating device, with which ready-to-use reactive adhesives can be produced for the respective application without intermediate - 2 - CONFIRD~IITION COP?
i10 99/51411 PCT/EP99/01232 stations and ~,ritermediate storage.
The device features of claim 6, and advantageous modifications in the other device claims, accomplish this object_ The components of the reactive adhesive are stored separately to prevent premature contact and ensure an unlimited durability and shelf life of the components.
Consequently, the production methods are far s_mpler than before with respect to the individual components.
The adhesive comprises at least one propozticn of the non-reactive component(s), such as functionalized polymers and resin mixtures or others, and at least a second proportion comprising the xeactive component, such as polyisocynates and others.
The two or more Components of the adhesive to be produced ate placed, in solid or liquid form, into an extruder, with at least one component being metered corresponding to the adhesive mix~,ng ratio. The two or more components are mixed in a particular ratio to ons another, which is determined by their chemical structure and the later intended application of the adhesive. The supplied adhesive components are placed into tile extruder and heated through friction and pressure. The friction and pressure suffice to heat the adhesive. The adhesive can be subjected to an additional heating later, when the - 3 - CON~'IRMATZON COPY
WO 99/51111 PCT/$P99/01232 mixing screw of the extruder is re-started and stopped.
The extruder constitutes the pre-melter, which continuously mixes the components, forming them into a usable reactive adhesive that can be processed immediately.
Only as much reactive adhesive is mixed, produced and melted as is required for the respective application. To this point, large quantities have been measured out and must be completely processed. The disadvantage of this is that waste is produced when the required quantity is smaller than the produced quantity, whezeas, i.n the novel method Of the invention, only the desired quantity is produced.
The cleaning process is also extremely simple: The supply of the reactive components) is discontinued, and the other, non-reactive components) is (are) used to rinse the melting systems or application systems.
In the method of producing a two- or multi-companent adhesive (K), at least one adhesive component is used in solid form, such as a granulate (G), or liquid form, and at least one other adhesive component is used in solid form, such as a granulate (G), or in liquid form as a liquid (F). The two adhesive components are heated, in a specific proportional ratio, by pressure and frictian in a conveyor track, and mixed to form the liquid adhesive (K);
ADHESIVES
The invention relates to a method of producing at least two-component reactive adhesives, and a device that is subsequently integrated for processing the adhesive, for example a moisture-activated adhesive.
It is known in practice to heat and mix reactive adhesives comprising two or more components, thereby bringing them to a liquid mass, then package them gas-tight in a container, so as to preclude any air humidity;
the vacuum-packed reactive adhesive is then cooled, so it can be stored and transported in solidified form in the container. The desired processing is performed in known pre-melting devices, in which the adhesive is re--melted and then used for the application.
Disadvantages of this process are the relatively-high production costs, possible damage during the transport of the containers carrying the reactive adhesive, and the threat to the durability of the reactive adhesive due to leaks in the packaging over lengthy transport or storage periods. After the container is opened, the surface of the reactive adhesive reacts, and if the adhesive remains exposed for a long period of time, it becomes unusable.
This results in the return of the reactive adhesive, CONH'IR~1TION COpY
which, of course, incurs costs. Reactive adhesive that cannot be processed in its entirety out of a vessel and remains there becomes unusable, The period of durability begins practically at the end of the production process of the reactive adhesive:
this is critical for the optimum use of the reactive adhesive. Tn moisture-activated cross-linking adhesives, the chemical cross-linking reaction is triggered by air humidity, but also by the continuous effect of the temperature during the pre-melting and melting phase until the application.
It is an object of the invention to create a method with which a reactive adhesive is created in a single wozk step from separate components that have an unlimited shelf life, with a processing/application step following immediately afterward, and with which wasted adhesive, and thus additional costs, are avoided.
ACCOrding to the invention, this object is accomplished by the characterizing featurPS of claim 1;
the further method claims describe advantageous modifications of the solution to the object.
A further object lies in the creation of a simple, inexpensively-constructed, economically--operating device, with which ready-to-use reactive adhesives can be produced for the respective application without intermediate - 2 - CONFIRD~IITION COP?
i10 99/51411 PCT/EP99/01232 stations and ~,ritermediate storage.
The device features of claim 6, and advantageous modifications in the other device claims, accomplish this object_ The components of the reactive adhesive are stored separately to prevent premature contact and ensure an unlimited durability and shelf life of the components.
Consequently, the production methods are far s_mpler than before with respect to the individual components.
The adhesive comprises at least one propozticn of the non-reactive component(s), such as functionalized polymers and resin mixtures or others, and at least a second proportion comprising the xeactive component, such as polyisocynates and others.
The two or more Components of the adhesive to be produced ate placed, in solid or liquid form, into an extruder, with at least one component being metered corresponding to the adhesive mix~,ng ratio. The two or more components are mixed in a particular ratio to ons another, which is determined by their chemical structure and the later intended application of the adhesive. The supplied adhesive components are placed into tile extruder and heated through friction and pressure. The friction and pressure suffice to heat the adhesive. The adhesive can be subjected to an additional heating later, when the - 3 - CON~'IRMATZON COPY
WO 99/51111 PCT/$P99/01232 mixing screw of the extruder is re-started and stopped.
The extruder constitutes the pre-melter, which continuously mixes the components, forming them into a usable reactive adhesive that can be processed immediately.
Only as much reactive adhesive is mixed, produced and melted as is required for the respective application. To this point, large quantities have been measured out and must be completely processed. The disadvantage of this is that waste is produced when the required quantity is smaller than the produced quantity, whezeas, i.n the novel method Of the invention, only the desired quantity is produced.
The cleaning process is also extremely simple: The supply of the reactive components) is discontinued, and the other, non-reactive components) is (are) used to rinse the melting systems or application systems.
In the method of producing a two- or multi-companent adhesive (K), at least one adhesive component is used in solid form, such as a granulate (G), or liquid form, and at least one other adhesive component is used in solid form, such as a granulate (G), or in liquid form as a liquid (F). The two adhesive components are heated, in a specific proportional ratio, by pressure and frictian in a conveyor track, and mixed to form the liquid adhesive (K);
- 4 - GOI~tB'IR~11TION COPY
lf0 99/51411 PCT/EF99/O1Z32 the liquid reactive adhesive (K) is then supplied directly to the application site (processing).
An adhesive component (G/F) is added in a metered quantity to the other adhesive component (G). The one adhesive component is a non-reactive component, and comprises, for example, a granulate (G). The second adhesive component is a reactive component, and is a granulate (G) or a liquid (E); this second component (G/F) is added in a metered quantity to the first adhesive component (G).
The two adhesive components can additionally be mixed while being heated, and/or the completely-liquid reactive adhesive can be kept warm.
The non-reactive component comprises, for example, functionalized polymers and resin mixtures, and the reactive component comprises, for example, polyisocyanates. Other reactive and non-reactive adhesive components can also be used, however.
The method is executed in an extruder (E) that forms a conveyor track, according to the exemplary embodiment shown in the single drawing'figure. This extruder (E) has a mixing and conveying screw (2), which is disposed in a housing (1) and is set into a rotational motion by a motorized drive (3) disposed at one end of the housing.
The extruder (E) includes a filling and feed funnel - 5 - CONL'IRD01TION COP=
IPO 99/51411 pCT/$p99/0123Z
(4) for the non-reactive, solid or liquid component, e.g., a granulate (G), the funnel being seated on the housing (1), and a supply line (S), such as a tubular or hose line, which is provided behind the funnel (9), seen in the S working direction (A) of the extruder. Incorporated inr~
the line is a metering element (6j, preferably a metering pump, for at least one reactive component in solid form, e.g., a granulate (G), or liquid form (F). An adhesive discharge (7) is disposed at the end of the extruder housing (1) opposite the drive (3).
The screw (2) of the extruder (E) forms the pressure and friction element for heating and mixing the adhesive components (G + F). A heating device (8) can be allocated to the extruder (E).
An adhesive dispensing line (9) in the foam of a tubular or hose line can be coupled to the adhesive discharge (7) of the extruder (E), and employed in applying the finished reactive adhesive (K) directly to the processing site.
The length of the extruder (E) is selected to correspond to the chemical structure and the intended application of the adhesive (K) to be produced.
The reactive adhesive (K) is applied by any conventional application system, such as spraying, doctor-blade, roller or nozzle systems.
- CON!'IR1~71TION CORY
lf0 99/51411 PCT/EF99/O1Z32 the liquid reactive adhesive (K) is then supplied directly to the application site (processing).
An adhesive component (G/F) is added in a metered quantity to the other adhesive component (G). The one adhesive component is a non-reactive component, and comprises, for example, a granulate (G). The second adhesive component is a reactive component, and is a granulate (G) or a liquid (E); this second component (G/F) is added in a metered quantity to the first adhesive component (G).
The two adhesive components can additionally be mixed while being heated, and/or the completely-liquid reactive adhesive can be kept warm.
The non-reactive component comprises, for example, functionalized polymers and resin mixtures, and the reactive component comprises, for example, polyisocyanates. Other reactive and non-reactive adhesive components can also be used, however.
The method is executed in an extruder (E) that forms a conveyor track, according to the exemplary embodiment shown in the single drawing'figure. This extruder (E) has a mixing and conveying screw (2), which is disposed in a housing (1) and is set into a rotational motion by a motorized drive (3) disposed at one end of the housing.
The extruder (E) includes a filling and feed funnel - 5 - CONL'IRD01TION COP=
IPO 99/51411 pCT/$p99/0123Z
(4) for the non-reactive, solid or liquid component, e.g., a granulate (G), the funnel being seated on the housing (1), and a supply line (S), such as a tubular or hose line, which is provided behind the funnel (9), seen in the S working direction (A) of the extruder. Incorporated inr~
the line is a metering element (6j, preferably a metering pump, for at least one reactive component in solid form, e.g., a granulate (G), or liquid form (F). An adhesive discharge (7) is disposed at the end of the extruder housing (1) opposite the drive (3).
The screw (2) of the extruder (E) forms the pressure and friction element for heating and mixing the adhesive components (G + F). A heating device (8) can be allocated to the extruder (E).
An adhesive dispensing line (9) in the foam of a tubular or hose line can be coupled to the adhesive discharge (7) of the extruder (E), and employed in applying the finished reactive adhesive (K) directly to the processing site.
The length of the extruder (E) is selected to correspond to the chemical structure and the intended application of the adhesive (K) to be produced.
The reactive adhesive (K) is applied by any conventional application system, such as spraying, doctor-blade, roller or nozzle systems.
- CON!'IR1~71TION CORY
Claims (9)
1. A method of producing at least two-component reactive adhesives, such as moisture-activated cross-linking adhesives, characterized in that at least one non-reactive adhesive component is present in solid form, such as a granulate (G), or in liquid form (F), and at least one other, reactive adhesive component is present in solid form, such as a granulate (G), or a liquid (F), the two adhesive components are heated, in a specific proportional ratio, through pressure and friction in a conveyor track, and mixed to create the liquid reactive adhesive (K), and the liquid reactive adhesive (K) is then applied directly to the application site (processing).
2. The method according to claim 1, characterized in that one adhesive component (G/F) is added in a metered quantity to the other adhesive component (G).
3. The method according to claim 1 or 2, characterized in that the adhesive components pass through the conveyor track for a period of time that corresponds to the chemical structure and the intended application of the reactive adhesive (K) to be produced.
4. The method according to one of claims 1 through 3, characterized in that the two adhesive components are mixed while being heated, and/or the liquid reactive adhesive is kept warm.
5. The method according to one of claims 1 through 4, characterized by the use of at least one non-reactive component comprising functionalized polymers and resin mixtures, and at least one reactive component comprising, for example, polyisocyanates or others.
6, A device for producing an adhesive with the method according to one or more of the foregoing claims, characterized by an extruder (E) that forms a conveyor track and has a filling and feed funnel (4) for the non-reactive solid or liquid component, and at least one supply line (5) with a metering element (6) for at least one reactive component in solid or liquid form, such as a granulate, the line being disposed behind the funnel (4), seen in the working direction (A) of the extruder.
7. The device according to claim 6, characterized in that the motor-driven screw (2) of the extruder (E) forms the pressure and friction element for heating and mixing the adhesive components, and a heating device (8) is allocated to the extruder (E).
8, The device according to claim 6 or 7, characterized in that an adhesive dispensing line (9) leading to the adhesive-processing site can be coupled to the adhesive discharge (7) of the extruder (E).
9. The device according to one of claims 6 through 8, characterized in that the length of the extruder (E) is selected corresponding to the chemical structure and intended application of the reactive adhesive (K).
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE19815203.5 | 1998-04-04 | ||
| DE19815203A DE19815203A1 (en) | 1998-04-04 | 1998-04-04 | Method and device for producing two-component reactive adhesives |
| PCT/EP1999/001232 WO1999051411A1 (en) | 1998-04-04 | 1999-02-26 | Method and device for producing two-component reactive adhesives |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA2293531A1 true CA2293531A1 (en) | 1999-10-14 |
Family
ID=7863642
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002293531A Abandoned CA2293531A1 (en) | 1998-04-04 | 1999-02-26 | Method and device for producing two-component reactive adhesives |
Country Status (9)
| Country | Link |
|---|---|
| EP (1) | EP0986455A1 (en) |
| JP (1) | JP2002511810A (en) |
| KR (1) | KR20010013280A (en) |
| AU (1) | AU2929599A (en) |
| CA (1) | CA2293531A1 (en) |
| DE (1) | DE19815203A1 (en) |
| PL (1) | PL337233A1 (en) |
| TR (1) | TR199902948T1 (en) |
| WO (1) | WO1999051411A1 (en) |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1954214A1 (en) * | 1969-10-28 | 1971-05-06 | Pyton Ag | Continuous mixing of adhesive/rubber compos - itions |
| DE3545899C1 (en) * | 1985-12-23 | 1987-04-23 | Gurit Essex Ag | Method and device for applying an adhesive, sealing, sealing or coating composition comprising at least two components to an object |
| DE3727847A1 (en) * | 1987-08-20 | 1989-03-02 | Fuller H B Co | MELT ADHESIVE AND METHOD FOR ITS PRODUCTION AND PROCESSING |
| DE3883678D1 (en) * | 1987-09-25 | 1993-10-07 | Ciba Geigy | Process for the preparation of a heat-curable, meltable mixture, plant for carrying it out and use in the extruder inlet chamber suitable for the latter. |
| EP0309410B1 (en) * | 1987-09-25 | 1993-09-01 | Ciba-Geigy Ag | Process for the manufacture of a heat-curable, meltable mixture, installation for carrying it out and suitable extruder inlet chamber for use in the latter |
| CA2057948A1 (en) * | 1991-01-11 | 1992-07-12 | James W. Schmitkons | Method and apparatus for metering flow of a two-component dispensing system |
| JPH08258041A (en) * | 1995-03-27 | 1996-10-08 | Matsushita Electric Works Ltd | Method and apparatus for mixing and supplying resin |
-
1998
- 1998-04-04 DE DE19815203A patent/DE19815203A1/en not_active Withdrawn
-
1999
- 1999-02-26 KR KR19997011273A patent/KR20010013280A/en not_active Application Discontinuation
- 1999-02-26 CA CA002293531A patent/CA2293531A1/en not_active Abandoned
- 1999-02-26 PL PL99337233A patent/PL337233A1/en unknown
- 1999-02-26 EP EP99910285A patent/EP0986455A1/en not_active Withdrawn
- 1999-02-26 JP JP54994399A patent/JP2002511810A/en active Pending
- 1999-02-26 WO PCT/EP1999/001232 patent/WO1999051411A1/en not_active Application Discontinuation
- 1999-02-26 TR TR1999/02948T patent/TR199902948T1/en unknown
- 1999-02-26 AU AU29295/99A patent/AU2929599A/en not_active Abandoned
Also Published As
| Publication number | Publication date |
|---|---|
| EP0986455A1 (en) | 2000-03-22 |
| AU2929599A (en) | 1999-10-25 |
| JP2002511810A (en) | 2002-04-16 |
| WO1999051411A1 (en) | 1999-10-14 |
| TR199902948T1 (en) | 2000-06-21 |
| KR20010013280A (en) | 2001-02-26 |
| DE19815203A1 (en) | 1999-10-07 |
| PL337233A1 (en) | 2000-08-14 |
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