EP0026906B1 - Procédé de revêtement de tuyaux en métal et utilisation desdits tuyaux - Google Patents
Procédé de revêtement de tuyaux en métal et utilisation desdits tuyaux Download PDFInfo
- Publication number
- EP0026906B1 EP0026906B1 EP80105906A EP80105906A EP0026906B1 EP 0026906 B1 EP0026906 B1 EP 0026906B1 EP 80105906 A EP80105906 A EP 80105906A EP 80105906 A EP80105906 A EP 80105906A EP 0026906 B1 EP0026906 B1 EP 0026906B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- polyethylene
- coating
- melt index
- stage
- tube
- 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
Links
- 238000000576 coating method Methods 0.000 title claims description 48
- 239000011248 coating agent Substances 0.000 title claims description 46
- 238000000034 method Methods 0.000 title claims description 28
- 239000002184 metal Substances 0.000 title claims description 12
- 229910052751 metal Inorganic materials 0.000 title claims description 12
- 239000004698 Polyethylene Substances 0.000 claims description 65
- -1 polyethylene Polymers 0.000 claims description 65
- 229920000573 polyethylene Polymers 0.000 claims description 65
- 239000000843 powder Substances 0.000 claims description 30
- 239000000155 melt Substances 0.000 claims description 21
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 claims description 3
- 229920001577 copolymer Polymers 0.000 claims description 2
- 239000003208 petroleum Substances 0.000 claims description 2
- 229940117958 vinyl acetate Drugs 0.000 claims 1
- 239000010410 layer Substances 0.000 description 48
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 10
- 244000089486 Phragmites australis subsp australis Species 0.000 description 8
- 238000001816 cooling Methods 0.000 description 7
- 238000005260 corrosion Methods 0.000 description 6
- 230000007797 corrosion Effects 0.000 description 6
- 229910052742 iron Inorganic materials 0.000 description 5
- 229910000831 Steel Inorganic materials 0.000 description 4
- 239000002318 adhesion promoter Substances 0.000 description 4
- 239000010959 steel Substances 0.000 description 4
- 239000011247 coating layer Substances 0.000 description 3
- 230000004927 fusion Effects 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 229920000642 polymer Polymers 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 2
- 239000002826 coolant Substances 0.000 description 2
- 229920001519 homopolymer Polymers 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 238000007711 solidification Methods 0.000 description 2
- 230000008023 solidification Effects 0.000 description 2
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- QRUDEWIWKLJBPS-UHFFFAOYSA-N benzotriazole Chemical compound C1=CC=C2N[N][N]C2=C1 QRUDEWIWKLJBPS-UHFFFAOYSA-N 0.000 description 1
- 239000012964 benzotriazole Substances 0.000 description 1
- 230000001427 coherent effect Effects 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000004567 concrete Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 229920006242 ethylene acrylic acid copolymer Polymers 0.000 description 1
- 239000005038 ethylene vinyl acetate Substances 0.000 description 1
- 229920006226 ethylene-acrylic acid Polymers 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000007888 film coating Substances 0.000 description 1
- 238000009501 film coating Methods 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000011346 highly viscous material Substances 0.000 description 1
- 238000007373 indentation Methods 0.000 description 1
- 239000004611 light stabiliser Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229920001684 low density polyethylene Polymers 0.000 description 1
- 239000004702 low-density polyethylene Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229920001179 medium density polyethylene Polymers 0.000 description 1
- 239000004701 medium-density polyethylene Substances 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 1
- 229920002689 polyvinyl acetate Polymers 0.000 description 1
- 239000011118 polyvinyl acetate Substances 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 238000003303 reheating Methods 0.000 description 1
- 239000010801 sewage sludge Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 238000004528 spin coating Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D7/00—Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials
- B05D7/14—Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials to metal, e.g. car bodies
- B05D7/146—Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials to metal, e.g. car bodies to metallic pipes or tubes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D1/00—Processes for applying liquids or other fluent materials
- B05D1/002—Processes for applying liquids or other fluent materials the substrate being rotated
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D2507/00—Polyolefins
- B05D2507/01—Polyethylene
Definitions
- the coating of metal pipes with polyethylene powder is known, the z. B. is applied by Aufriesetn, spin coating or starting on the preheated tube to 300 to 360 ° C.
- the types of polyethylene used in this process have melt indexes (190 ° C / 2.16 kg) of 1.2 to 1.7 g / 1 min.
- the melt index must be higher than in the first-mentioned process because easier melting is essential for coating with powder in order to anchor the applied particles on the surface.
- the coating time for powder is generally about 5 minutes.
- this method has the disadvantage that, although high preheating temperatures are used, adequate corrosion protection due to the application of only one layer is often not achieved.
- Another publication describes a composite pipe made of a polyethylene powder layer welded onto a steel pipe and a polyethylene layer welded to it, which, for. B. in the form of a polyethylene film emerging from an extruder onto the hot sintered polyethylene powder layer.
- the steel tube is z. B. preheated to 150 ° C. At this temperature, however, it is not possible to produce a smooth, coherent layer in a desired required minimum layer thickness of 1.5 to 4 mm.
- a polyethylene layer is applied to a steel pipe, firstly a 0.05 mm thick first layer of an adhesion promoter at a tube temperature about 100 ° C. above the solidification temperature of the adhesion promoter and then the second layer of the adhesion promoter at 20 to Pipe temperature 50 ° C above the solidification temperature, e.g. B. at 140 ° C, is applied.
- the adhesion promoter of the first layer can be applied in powder form or by wrapping it with a film.
- the second layer can be applied by pre-extrusion in the form of a double tube or a double wrapping film.
- the temperature of 140 ° C. is not sufficient for the purposes desired according to the present invention, that is to say for the required minimum layer thickness.
- Another document also discloses coating a steel tube surface with a polyethylene having a higher melt index, e.g. 1 to 1.5 g / 10 min (ASTM-D 1238-53T) and with a lower melt index polyethylene, e.g. B. 0.2 to 0.5 g / 10 min, the second layer being applied to the first coating.
- a polyethylene having a higher melt index e.g. 1 to 1.5 g / 10 min (ASTM-D 1238-53T) and with a lower melt index polyethylene, e.g. B. 0.2 to 0.5 g / 10 min
- Polyethylene powder is used to form both layers. If two layers are applied in the form of powder on top of one another, the surface sometimes leaves something to be desired in terms of their homogeneity and smoothness.
- the subject of the invention is the method defined in claim 1.
- a further possible embodiment of the invention provides according to claims 3 to 5 that first of all a polyethylene powder with a melt index of 1.2 to 1.7 g / 10 min or a strip of polyethylene emerging directly from an extruder with a melt index of at most 1 , 7 g / 10 min (190 ° C / 2.16 kg) on a metal tube, which in the case of powder coating has a temperature of at least 300 ° C and in the case of the coating from the extruder a maximum of 250 ° C, then the coating is allowed to cool to a temperature of about 110 to 170, preferably 110 to 150 ° C and then in a third stage a self-supporting, light-stabilized, light-colored polyethylene film with a melt index of 0.4 to 1.1 g / 10 min at this temperature.
- compounds of the benzotriazole type are suitable as light stabilizers for the light-colored polyethylene film.
- a layer thickness of 1.5 to 4 mm is generally required for adequate corrosion protection. In some cases, the layer thickness can also be more than 4 mm. However, the layer thickness must be at least 1.5 mm, because otherwise there is an excessive cathodic protective current requirement.
- the process according to the invention has the advantage that, in general, compared to known processes, it surprisingly results in energy savings and nevertheless a considerably higher working speed with at least equally good production properties.
- the combination of powder application coating with the tape film coating - in this order mentioned - has succeeded in reducing the energy consumption through targeted temperature control, but at the same time improving the quality of the coating because any pores that occur from the powder coating the film cover is closed by welding.
- the light-colored cover layer provides good protection for the pipes against excessive heating when stored outdoors for long periods under the influence of heat, for example due to sunshine or by laying in strongly heated floor layers.
- the coating of the extruder is also very simple and time-saving without additional equipment.
- the strip emerging from the extruder advantageously has a melt index of at least 0.4 g / 10 min.
- the polyethylene in the powder coating expediently has a particle size of 1 to 600 ⁇ m, preferably 100 to 400 ⁇ m.
- the self-supporting polyethylene film is advantageously in the form of a polyethylene tape, for. B. made of polyethylene with a melt index of 0.1 to 1.2 g / 10 min, applied. It can be applied to a rotating tube. This has the advantage that the tape can be wound automatically. The bandwidth can be varied as desired. It is z. B. at least 20 mm, expediently 10 to 1500 mm. A range of up to about 1 m is generally used.
- the layer thickness of the tapes is usually 100 to 400 microns, preferably 100 to 200 microns.
- the light colored bands are preferably white. However, another color can also be selected as desired, e.g. B. the warning color yellow, but also light orange, light blue, light green or the like. If necessary, the light-colored tapes can also be used to identify the pipes.
- the speed of the coating can vary within wide limits. It depends on the desired layer thickness, the thickness of the tube wall, the length and the diameter of the tube, the outer tube diameter being 50 to 2000 mm, for example.
- z. B about 15 to 45, usually about 30 minutes to cool to 60 ° C.
- the coating of a pipe with a diameter of 400 mm and a layer thickness of 1.5 mm (this is the minimum thickness for adequate corrosion protection) generally requires about 8 to 20, usually about 15 minutes for a 12 m long coating.
- an additional resin in the form of a polymer, e.g. B. polyvinyl acetate, ethylene-vinyl acetate copolymer, ethylene-acrylic acid and / or acrylic ester copolymer, optionally with other comonomers, or other polymers, advantageously in a proportion of 5 to 15, preferably 5 to 10 wt .-%, based on the polyethylene powder.
- a polymer e.g. B. polyvinyl acetate, ethylene-vinyl acetate copolymer, ethylene-acrylic acid and / or acrylic ester copolymer, optionally with other comonomers, or other polymers, advantageously in a proportion of 5 to 15, preferably 5 to 10 wt .-%, based on the polyethylene powder.
- this coating can be carried out by the usual coating methods, by spraying, but preferably by powder coating.
- the same additional resins can also be contained in the polyethylene tape in a proportion of 2 to 5%
- the tubes coated by the method according to the invention are used in a variety of ways. Because of their surface protection, they are especially for laid pipes, e.g. B. in pipelines for the extraction of petroleum, but also of other gaseous, liquid or highly viscous substances, for example natural gas, water, sewage sludge, concrete, waste water, slurries or the like.
- Example 2 The same tube as in Example 1 is used, but with a preheating temperature of 310 ° C.
- the tube is coated with polyethylene powder with a melt index of 1.2 to 1.7 g / 10 min with a layer thickness of 2 mm. After 10 minutes the coating melted smoothly and reached a temperature of 180 ° C. The cooling time to 60 ° C simply by leaving it lying there is 50 minutes.
- Example 2 The same tube as in Example 2 is used, but with a preheating temperature of 360 ° C.
- the tube is covered at this temperature with polyethylene powder having a melt index from 1.2 to 1.7 1 1/2 minutes with a layer thickness of 2 mm.
- the coating melted in the course of 4 minutes and at the same time cooled to 310 ° C. However, reheating is still required for smooth melting. Therefore, after these 4 minutes, the pipe is reheated for one minute. The coating is smooth after this additional minute.
- the cooling time to 60 ° C from the start of the powder coating and without additional cooling is 42 minutes.
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Wood Science & Technology (AREA)
- Laminated Bodies (AREA)
- Application Of Or Painting With Fluid Materials (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Lining Or Joining Of Plastics Or The Like (AREA)
- Protection Of Pipes Against Damage, Friction, And Corrosion (AREA)
Claims (10)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT80105906T ATE4292T1 (de) | 1979-10-05 | 1980-09-30 | Verfahren zur beschichtung von metallrohren und verwendung der rohre. |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19792940388 DE2940388A1 (de) | 1979-10-05 | 1979-10-05 | Verfahren zur beschichtung von metallrohren |
DE2940388 | 1979-10-05 | ||
DE2946459 | 1979-11-17 | ||
DE19792946459 DE2946459A1 (de) | 1979-11-17 | 1979-11-17 | Verfahren zum beschichten von metallrohren |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0026906A1 EP0026906A1 (fr) | 1981-04-15 |
EP0026906B1 true EP0026906B1 (fr) | 1983-07-27 |
Family
ID=25781375
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP80105906A Expired EP0026906B1 (fr) | 1979-10-05 | 1980-09-30 | Procédé de revêtement de tuyaux en métal et utilisation desdits tuyaux |
Country Status (5)
Country | Link |
---|---|
US (1) | USRE31354E (fr) |
EP (1) | EP0026906B1 (fr) |
CA (1) | CA1151017A (fr) |
DE (1) | DE3064429D1 (fr) |
ES (1) | ES495475A0 (fr) |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3101684A1 (de) * | 1981-01-21 | 1982-08-26 | Hoechst Ag, 6000 Frankfurt | "verfahren zur beschichtung von metallrohren und verwendung der nach diesem verfahren hergestellten rohre" |
US4606953A (en) | 1983-06-23 | 1986-08-19 | Nippon Steel Corporation | Polypropylene coated steel pipe |
US5105599A (en) * | 1989-02-24 | 1992-04-21 | Highland Supply Corporation | Means for securing a decorative cover about a flower pot |
DE3444523A1 (de) * | 1984-12-06 | 1986-06-12 | Hoesch Ag, 4600 Dortmund | Metallrohr mit einer korrosions- und stossschutzbeschichtung und verfahren zu seiner herstellung |
US5180531A (en) * | 1988-07-29 | 1993-01-19 | Vartkes Borzakian | Method of forming plastic piling |
US5051285A (en) * | 1988-07-29 | 1991-09-24 | Pillard Products, Inc. | Plastic piling |
US5410856A (en) * | 1988-09-26 | 1995-05-02 | Highland Supply Corporation | Decorative assembly for a floral grouping |
AU668470B2 (en) * | 1993-07-12 | 1996-05-02 | Seaward International, Inc. | Elongated structural member and method and apparatus for making same |
US7882883B2 (en) * | 2007-08-06 | 2011-02-08 | Anderson Kenneth K | Method for making a barrel front for a paintball marker |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1213977B (de) * | 1962-06-22 | 1966-04-07 | Phoenix Rheinrohr Ag | Gegen Spannungsriesse bestaendiger Polyaethylenueberzug auf Metalloberflaechen und Verfahren zur Herstellung eines derartigen Polyaethylenueberzuges |
US3348995A (en) * | 1964-03-09 | 1967-10-24 | American Cast Iron Pipe Co | Method of coating metal surfaces with polyethylene utilizing a polyethylene primer and articles produced thereby |
DE1228052B (de) * | 1965-05-04 | 1966-11-03 | Mannesmann Ag | Verbundrohr und Verfahren zur Herstellung |
DE1629530B1 (de) * | 1966-03-08 | 1972-05-25 | Mannesmann Ag | Verfahren zum Herstellen eines aus einem Stahlrohr mit aeusseren Kunststoffschichten bestehenden Verbundrohres |
GB1407043A (en) * | 1971-09-06 | 1975-09-24 | Sumitomo Metal Ind | Method of manufacturing coated steel pipes |
GB1482528A (en) * | 1973-06-15 | 1977-08-10 | Sumitomo Metal Ind | Process for forming coatings on metal surfaces |
US4211595A (en) * | 1978-10-10 | 1980-07-08 | The Kendall Company | Method of coating pipe |
US4213486A (en) * | 1978-11-06 | 1980-07-22 | The Kendall Company | Coated pipe and process for making same |
DE2852001A1 (de) * | 1978-12-01 | 1980-06-12 | Metallgesellschaft Ag | Verfahren zum ummanteln von rotationssymmetrischen, metallischen formkoerpern |
-
1980
- 1980-09-30 ES ES495475A patent/ES495475A0/es active Granted
- 1980-09-30 EP EP80105906A patent/EP0026906B1/fr not_active Expired
- 1980-09-30 DE DE8080105906T patent/DE3064429D1/de not_active Expired
- 1980-10-03 CA CA000361493A patent/CA1151017A/fr not_active Expired
-
1982
- 1982-09-16 US US06/419,035 patent/USRE31354E/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
CA1151017A (fr) | 1983-08-02 |
ES8106418A1 (es) | 1981-07-01 |
DE3064429D1 (en) | 1983-09-01 |
ES495475A0 (es) | 1981-07-01 |
USRE31354E (en) | 1983-08-23 |
EP0026906A1 (fr) | 1981-04-15 |
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