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EP 1 541 710 B1 |
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EUROPEAN PATENT SPECIFICATION |
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Mention of the grant of the patent: |
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04.11.2009 Bulletin 2009/45 |
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Date of filing: 07.12.2004 |
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International Patent Classification (IPC):
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Method for coating tubes
Verfahren zur Beschichtung von Rohren
Procédé de revêtment des tubes
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Designated Contracting States: |
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AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LI LT LU MC NL PL PT RO SE SI
SK TR |
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Priority: |
12.12.2003 FI 20031821
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Date of publication of application: |
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15.06.2005 Bulletin 2005/24 |
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Proprietor: Cupori Group Oy |
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02130 Espoo (FI) |
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Inventor: |
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- Salminen, Aleksi
28800 Pori (FI)
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Representative: Heikkinen, Esko Juhani et al |
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Berggren Oy Ab
P.O. Box 16 00101 Helsinki 00101 Helsinki (FI) |
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References cited: :
EP-A- 0 848 084 DE-A1- 3 800 918 US-A- 5 769 129
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EP-A- 0 851 041 US-A- 2 282 511
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| Note: Within nine months from the publication of the mention of the grant of the European
patent, any person may give notice to the European Patent Office of opposition to
the European patent
granted. Notice of opposition shall be filed in a written reasoned statement. It shall
not be deemed to
have been filed until the opposition fee has been paid. (Art. 99(1) European Patent
Convention).
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[0001] The invention relates to a method according to claim 1 for coating the inner surface
of a tube made of copper or copper alloy.
[0002] Copper tubes are known to be coated internally by tin that provides a cathodic protection
for copper. Specific quality requirements are set for tin-coated tubes with respect
to strength, purity and coating porosity. In chemical tin coating, the process is
known to be distinguished as two or three separate process steps comprising the activation
of the surface to be coated, precoating and the coating step proper with the tin coating.
In the surface activation, the surface to be coated is treated by certain chemicals
in order to make the coating succeed. In the precoating after the activation, the
solution is usually composed of an acidic solution, in which there is dissolved both
a complexing agent participating in the coating reactions, as well as the tin source
proper. The function of the precoating step is to form tin nuclei on the surface to
be coated. In the coating step, a tin coating layer is deposited onto the tin nuclei.
The actual coating step may be carried out either in an acidic or an alkaline solution.
[0003] Chemical tin coating is known to be carried out as an ion-exchange reaction, in which
copper ions are dissolved from the basic metal, and simultaneously on the surface
of the basic metal, from the tin coating solution there is deposited an equivalent
quantity of tin ions on the basis of the tension between the tin coating solution
and copper. An increased quantity of dissolved copper in the solution with respect
to the quantity of tin slows down the ion exchange reaction. Consequently, also according
to the quantity of deposited tin, the solution must from time to time be subjected
to tin source regulation. When the surface of the basic metal is completely coated,
the ion exchange reaction is slowed down and finally stops. If the tin coating becomes
nonhomogeneous during the tin coating process, this may later result in that tin ions
are disengaged for example to household water. The working life of a tin coating solution
can be raised by adding so-called stabilizers into the solution. It is well known
that the tin coating process is carried out in two separate steps, so that the solution
of the first step is only used for transmission, and the solution of the second step
is used for accumulating the tin layer.
[0004] According to the patent
EP0848084, there is known a method for manufacturing a copper tube, according to which the
tin coating of the copper tubes is carried out in two steps, so that the temperature
of the tin coating solution is raised when proceeding to the second tin coating step.
[0005] Further, according to document
US-A-5,769,129 a plating method has been known to coat the inner surface of a copper alloy pipe
with Sn by means of a chemical plating solution. The plating method is carried out
by using Tin(II)-chloride, Thiourea and Tartaric acid as the plating solution which
is caused to flow through the copper pipe. According to document
EP 0 851 041 A1 a coating method for a copper tube is disclosed which method is based on the same
principal to let a chemical tin-solution flow through the pipe. Hereby, method is
divided into two method steps which differ in the temperature of the solution to be
fed through the pipe, respectively. Accordingly, one has to begin with a low temperature
within the range of 35°C - 45°C. which first method step is followed by the second
one using a temperature between 70°C and 85° C at the maximum temperature. At least
it is proposed to alter the temperature during the plating process to realize the
effect of the double-step process.
[0006] The object of the present invention is to introduce a novel solution that is more
advantageous than the prior art for coating the inner wall of a tube made of copper
or copper alloy with a tin layer, particularly so that the coating is carried out
in one coating step.
[0007] The invention is characterized by what is set forth in the characterizing part of
claim 1. Other preferred embodiments of the invention are characterized by what is
set forth in the rest of the claims.
[0008] Remarkable advantages are achieved by the arrangement according to the invention.
By means of the method according to the invention, the tin coating process of the
interior tube wall is made more rapid, and the quantity of used chemicals is remarkably
reduced in comparison with conventional tin coating. By means of the invention, there
is formed a tin layer according to the regulations on the inner surface of a tube
made of copper or copper alloy by carrying out the coating in one coating step, so
that the tin layer is formed as the tin coating solution circulates on the inner tube
surface. The one coating step according to the invention means that the coating solution
is circulated to the inner tube surface at one end of the tube, and it is made to
flow out of the other end of the tube, during which time there is created a tin layer
by means of chemical tin coating according to an ion exchange reaction. Advantageously
the multi-step activation of the inner tube surface, the precoating and the coating
are made to take place by means of one and the same coating solution and essentially
in one coating step, while the coating solution circulates on the inner tube surface.
[0009] The coating solution according to the invention, circulated on the inner tube surface,
includes at least pH adjustment agent, to the extent that the pH of the coating solution
<1, tin source for creating bivalent tin ions (Sn
2+) in the coating solution and complexing agent. According to an embodiment of the
invention, the employed tin source is tin chloride (SnCl
2), and the employed complexing agent is thiourea (NH
2)
2CS, in which case the ratio of the contents of tin chloride and thiourea in the coating
solution is 1:(1-10), preferably, however, 1:4. According to an embodiment of the
invention, the employed pH adjustment agent is hydrochloric acid (HCI). The employed
tin source can be for example tin (II) sulfate or some other tin source, by using
which the tin ion can be made to be present as bivalent (Sn
2+) in the above mentioned coating solution. According to an embodiment of the invention,
the employed pH adjustment agent is sulfuric acid (H
2SO
4). The content of thiourea in the coating solution is 2 - 20 percentages by weight
(w-%), preferably 10 percentages by weight. When the content of thiourea in the coating
solution is relatively low, the tubes are easier to clean after coating.
[0010] In a coating solution according to the invention, the complexing agent participates
in the tin coating reactions as a complexing agent at least by binding free copper
ions in said coating solution. When carrying out the coating in one step by a coating
solution according to the invention, the inner tube surface is also cleaned of possible
impurities that are accumulated on the inner surface in earlier treatments of the
inner tube surface. When using a coating solution according to the invention, the
use of many other chemicals, such as for example stabilizers, can be completely avoided.
When the use of many other chemicals is avoided, the further treatment of the coating
solution is remarkably cheaper. In addition, the when using a coating solution according
to the invention, harmful sedimentation of the solution at high temperatures can be
avoided. The coating reaction time is remarkably shortened at the achieved high temperatures.
Advantageously also when using a coating solution according to the invention, the
solution expenses are reduced, and the time required for preparing the solution remains
short in comparison with the manufacturing of multi-step coating solutions. Likewise,
the use of rinsing waters circulated between various steps can be avoided, and savings
can be achieved in the further treatment expenses of the solution.
[0011] According to the invention, the temperature of the coating solution is adjusted to
be within the range 35 - 100ºC when feeding the coating solution onto the inner tube
surface. By using this temperature, on the inner tube surface there is accumulated
an advantageous tin layer according to the regulations. According to an embodiment
of the invention, the tube is preheated before coating, which further enhances a successful
coating. Preheating can be carried out from outside the tubes, or for instance by
rinsing the inside of the tube by warm water or warm compressed air. According to
the invention, the coating circulates on the inner tube surface for less than 30 minutes.
[0012] According to the invention, the coating is carried out in an oxygen-free atmosphere,
so that the coating solution and the coating equipment are insulated against the effects
of oxygen, for example by arranging them in oxygen-free protective gas and by preventing
the access of oxygen into the coating solution. According to an embodiment of the
invention, oxygen is removed from the coating solution, for instance before coating
or during the coating step, in which case the effects of oxygen contained in the various
ingredients of the solution can be avoided. Thus the oxidation of tin in the solution
is advantageously prevented. Tin oxidation binds tin as a component, which means that
the quantity of free tin ions in the solution is reduced. When the oxidation of tin
is prevented in the tin coating solution, the working age and resistance of the solution
is improved. According to the invention, the stabilizer can thus be advantageously
replaced by various equipment arrangements. The function of the stabilizer is to prevent
the oxidation of tin ions (Sn
2+) in the solution. After coating, the inner tube surface is cleaned of solution residues,
for example by means of rinsing by air and water. The inner surface of the tube to
be coated can be either treated or untreated. According to the invention, the inner
surface of the tube to be coated is oxidized, in which case the tube can be semi-hard
or soft. Advantageously by means of the coating solution according to the invention,
both pickling and coating are carried out in the same coating solution. According
to an embodiment of the invention, the tube to be coated is hard. The tube can also
be pickled. The tube to be coated can be a tube coil, or a straight tube, and can
have a length of even 1,000 meters.
[0013] The invention is described in more detail below with reference to an example.
EXAMPLE
[0014] The following example describes a method according to the present invention for coating
a tube made of copper by a tin layer. According to the example, the tube to be coated
is a semi-hard, straight tube with an oxidized inner surface. The coating for forming
the tin layer can be carried out by feeding the coating solution simultaneously either
onto the inner surfaces of several tubes, or to one tube at a time. Onto the inner
tube surface, there is fed coating solution from a separate solution tank by pressurizing
the coating solution into the tube. According to the example, the coating solution
contains hydrochloric acid (HCI) as the pH adjustment, tin chloride (SnCl
2) as the tin source, and thiourea ((NH
2)
2CS) as the complexing agent. pH adjustment agent is added into pure water to that
extent that the acidity (pH) in the coating solution is below 1, whereafter thiourea
is added so that the content of thiourea in the final coating solution is 10 percentages
by weight. Tin chloride is added to the coating solution to the extent that the ratio
of the tin chloride and thiourea contents in the coating solution is 1:4, i.e. the
quantity of thiourea is 4 times as much as the quantity of tin chloride. In the coating
solution, tin is present in ion form (Sn
2+). According to the example, the temperature of the coating solution is 75 ºC, when
it is fed onto the inner tube surface. The solution tank and the rest of the equipment
are protected so that the access of oxygen into the coating solution is prevented
for example by protective gas. According to the example, oxygen is removed from the
coating solution. The temperature of the coating solution kept in the solution tank
is maintained constant. Before feeding the coating solution in the tube, the tubes
are rinsed by warm liquid. According to the example, the coating solution is fed into
the preheated tube at a turbulent speed. The coating solution circulates on the inner
tube surface for about 20 minutes, during which time a tin layer is formed. The tin
layer grows on the inner surface according to the ion exchange reaction, so that metallic
copper is dissolved from the inner tube surface to the tin coating solution to ions,
and the tin ion contained in the coating solution is deposited on the inner tube surface,
forming a metallic coating. The tin layer is formed as a homogeneous layer with a
thickness of about 1 - 2 micrometers. When the coating solution has circulated from
one end of the tube to the other end, and the tin layer is formed, the tube is emptied
of the coating solution. The tin-coated tubes are cleaned of coating solution residues
for example by rinsing the tubes with water. When necessary, the tin-coated tubes
are dried before their further treatment, such as storage or transport.
[0015] For a man skilled in the art, it is obvious that the various embodiments of the invention
are not restricted to the examples given above, but may vary within the scope of the
appended claims.
1. A method for coating the inner surface of a tube made of copper or copper alloy by
a tin layer, according to which method the tin layer is formed by chemical tin coating,
and the coating solution circulated on the inner tube surface contains at least a
pH adjustment agent to the extent that the pH of the coating solution is < 1, a tin
source for forming bivalent tin ions (Sn2+) in the coating solution, as well as a complexing agent,
characterized in that the inner surface of the tube to be coated is oxidized and that the coating of the
inner tube surface is carried out in one coating step by said coating solution, the
method being arranged in oxygen-free protective gas, wherein the tin layer is formed
as the coating solution having a temperature within the range of 35 - 100°C circulates
on the inner tube surface for less than 30 minutes.
2. A method according to claim 1, characterized in that the employed tin source is tin chloride.
3. A method according to claim 1, characterized in that the employed complexing agent is thiourea.
4. A method according to claim 2 or 3, characterized in that the ratio of the tin chloride and thiourea contents in the coating solution is 1:(1-10)
5. A method according to claim 4, characterized in that the ratio of the tin chloride and thiourea contents in the coating solution is preferably
1:4.
6. A method according to claim 1, characterized in that the employed pH adjustment agent is hydrochloric acid.
7. A method according to claim 1, characterized in that the employed pH adjustment agent is sulfuric acid.
8. A method according to claim 1, characterized in that the employed tin source is tin sulfate.
9. A method according to claim 3, 4 or 5, characterized in that the content of thiourea in the coating solution is 2 - 20 percentages by weight.
10. A method according to claim 9, characterized in that the content of thiourea in the coating solution is preferably 10 percentages by weight.
11. A method according to any of the preceding claims, characterized in that the tube is preheated before coating.
12. A method according to any of the preceding claims, characterized in that the inner tube surface is cleaned after coating.
13. A method according to claim 1 - 12, characterized in that the tube to be coated is semi-hard.
14. A method according to claim 1 - 12, characterized in that the tube to be coated is soft.
15. A method according to claim 1 - 14, characterized in that the tube to be coated is pickled.
1. Verfahren zum Beschichten der Innenfläche eines aus Kupfer oder einer Kupferlegierung
gefertigten Rohres mit einer Zinnschicht, gemäß welchem Verfahren die Zinnschicht
mittels einer chemischen Zinnbeschichtung gebildet wird, und die an der Innenrohrfläche
zirkulierte Beschichtungslöschung zumindest ein pH-Reguliermittel enthält, in dem
Maße, dass der pH der Beschichtungslösung < 1 ist, ferner eine Zinn-Stammquelle zur
Bildung von bivalenten Zinn-Ionen (Sn2+) in der Beschichtungslösung, ferner einen Komplexbildner,
dadurch gekennzeichnet, dass die zu beschichtende Innenfläche des Rohres oxidiert wird und dass die Beschichtung
der Innenrohrfläche in einem einzelnen Beschichtungsschritt mit Hilfe der Beschichtungslösung
ausgeführt wird, wobei das Verfahren in einem sauerstofffreien Schutzgas durchgeführt
wird, und die Zinnschicht gebildet wird, wenn die Beschichtungslösung eine Temperatur
innerhalb des Bereiches von 35 - 100°C hat und auf der Innenrohrfläche für weniger
als 30 Minuten zirkuliert.
2. Verfahren nach Anspruch 1,
dadurch gekennzeichnet, dass die verwendete Zinn-Stammquelle Zinnchlorid ist.
3. Verfahren nach Anspruch 1,
dadurch gekennzeichnet, dass der verwendete Komplexbildner Thiocarbamid ist.
4. Verfahren nach Anspruch 2 oder 3,
dadurch gekennzeichnet, dass das Verhältnis von Zinnchlorid und den Thiocarbamid-Anteilen in der Beschichtungslösung
ist 1 : (1-10).
5. Verfahren nach Anspruch 4,
dadurch gekennzeichnet, dass das Verhältnis von Zinnchlorid und den Thiocarbamid-Bestandteilen in der Beschichtungslösung
vorzugsweise 1 : 4 ist.
6. Verfahren nach Anspruch 1,
dadurch gekennzeichnet, dass das verwendete pH-Reguliermittel Salzsäure ist.
7. Verfahren nach Anspruch 1,
dadurch gekennzeichnet, dass das eingesetzte pH-Reguliermittel Schwefelsäure ist.
8. Verfahren nach Anspruch 1,
dadurch gekennzeichnet, dass die verwendete Zinnstammquelle Zinnsulfat ist.
9. Verfahren nach Anspruch 3, 4 oder 5,
dadurch gekennzeichnet, dass der Anteil an Thiocarbamid in der Beschichtungslösung 2 - 20 Gewichtsprozent beträgt.
10. Verfahren nach Anspruch 9,
dadurch gekennzeichnet, dass der Anteil an Thiocarbamid in der Beschichtungslösung vorzugsweise 10 Gewichtsprozent
beträgt.
11. Verfahren nach einem der vorangehenden Ansprüche,
dadurch gekennzeichnet, dass der Rohr vor dem Beschichten erwärmt wird.
12. Verfahren nach einem der vorangehenden Ansprüche,
dadurch gekennzeichnet, dass die Innenrohrfläche nach dem Beschichten gereinigt wird.
13. Verfahren nach Anspruch 1 - 12,
dadurch gekennzeichnet, dass das zu beschichtende Rohr halbhart ist.
14. Verfahren nach Anspruch 1-12,
dadurch gekennzeichnet, dass das zu beschichtende Rohr weich ist.
15. Verfahren nach Anspruch 1-14,
dadurch gekennzeichnet, dass das zu beschichtende Rohr gebeizt ist.
1. Procédé de revêtement de la surface interne d'un tube constitué de cuivre ou d'un
alliage de cuivre par une couche d'étain, selon lequel la couche d'étain est formée
par un revêtement d'étain chimique, et la solution de revêtement mise en circulation
sur la surface interne du tube contient au moins un agent d'ajustement de pH, dans
la mesure où le pH de la solution de revêtement est inférieur à 1, une source d'étain
pour former des ions d'étain bivalents (Sn2+) dans la solution de revêtement, ainsi qu'un agent complexant,
caractérisé en ce que la surface interne du tube à revêtir est oxydée et que le revêtement de la surface
intérieure du tube est réalisé en une seule étape de revêtement par ladite solution
de revêtement, le procédé étant réalisé dans un gaz protecteur sans oxygène, dans
lequel la couche d'étain est formée lorsque la solution de revêtement ayant une température
comprise dans la gamme de 35 à 100°C, circule sur la surface interne du tube pendant
moins de 30 minutes.
2. Procédé selon la revendication 1, caractérisé en ce que la source d'étain utilisée est le chlorure d'étain.
3. Procédé selon la revendication 1, caractérisé en ce que l'agent complexant utilisé est la thiourée.
4. Procédé selon les revendications 2 ou 3, caractérisé en ce que le rapport entre les teneurs en chlorure d'étain et en thiourée dans la solution
de revêtement sont de 1 : (1-10).
5. Procédé selon la revendication 4, caractérisé en ce que le rapport entre les teneurs en chlorure d'étain et de thiourée dans la solution
de revêtement est de préférence de 1 :4.
6. Procédé selon la revendication 1, caractérisé en ce que l'agent d'ajustement de pH utilisé est l'acide chlorhydrique.
7. Procédé selon la revendication 1, caractérisé en ce que l'agent d'ajustement de pH utilisé est l'acide sulfurique.
8. Procédé selon la revendication 1, caractérisé en ce que la source d'étain utilisée est le sulfate d'étain.
9. Procédé selon les revendications 3, 4 ou 5, caractérisé en ce que la teneur en thiourée dans la solution de revêtement est de 2-20 pour cent en poids.
10. Procédé selon la revendication 9, caractérisé en ce que la teneur en thiourée dans la solution de revêtement est de préférence de 10 pour
cent en poids.
11. Procédé selon l'une quelconque des revendications précédentes, caractérisé en ce que le tube est préchauffé avant revêtement.
12. Procédé selon l'une quelconque des revendications précédentes, caractérisé en ce que la surface intérieure du tube est nettoyée après revêtement.
13. Procédé selon la revendication 1-12, caractérisé en ce que le tube à revêtir est semi-dur.
14. Procédé selon la revendication 1-12, caractérisé en ce que le tube à revêtir est mou.
15. Procédé selon la revendication 1-14, caractérisé en ce que le tube à revêtir est décapé.
REFERENCES CITED IN THE DESCRIPTION
This list of references cited by the applicant is for the reader's convenience only.
It does not form part of the European patent document. Even though great care has
been taken in compiling the references, errors or omissions cannot be excluded and
the EPO disclaims all liability in this regard.
Patent documents cited in the description