Extruded aliphatic polyketone permeation barrier for spoolable composite pipes
Spoolable composite pipes for oil and gas flowlines may include an inner extruded tubular liner, a reinforcement layer surrounding the inner extruded tubular liner, and an outer extruded tubular cover surrounding the reinforcement layer. In these spoolable composite pipes, the inner extruded tubular liner may include an aliphatic polyketone. Internally lined pipes for oil and gas flowlines for oil and gas flowlines may include inner extruded tubular liner containing an aliphatic polyketone, and a carbon steel pipe surrounding the inner extruded tubular liner. The spoolable composite pipes and the internally lined pipes may be configured to operate at temperatures of up to about 110° C., and to carry hydrocarbons having an aromatic content of up to about 35% by volume of the total hydrocarbons content.
1. A non-metallic spoolable composite pipe for oil and gas flowlines, comprising:
an inner extruded tubular liner configured to be in direct contact with a fluid comprising hydrocarbons flowing through the spoolable composite pipe;
a polymer reinforcement layer surrounding the inner extruded tubular liner; and
an outer extruded tubular cover surrounding the reinforcement layer;
where the inner extruded tubular liner comprises an aliphatic polyketone having the formula (I)
[[—CH 2 CHR 1 (C═O)—] n [—CH 2 CHR 2 (C═O)—] m ] p , (I)
where R 1 and R 2 are independently from one another the same or different,
where R 1 is selected from the group consisting of hydrogen and an alkyl group, and
where R 2 is an alkyl group, and
where n is less than 0.5 and n+m=1,
where p is an integer between 500 and 5000,
where structural units [—CH 2 CHR 1 (C═O)—] and [—CH 2 CHR 2 (C═O)—], are randomly distributed, blocked or both, and
where the spoolable composite pipe is configured to operate at temperatures of up to about 110° C. and to carry hydrocarbons having an aromatic content of up to about 35% by volume based on the total hydrocarbons content.
2. The non-metallic spoolable composite pipe of claim 1 configured to carry hydrocarbons having an aromatic and cyclo-aliphatic content of up to about 50% by volume of the total hydrocarbons content.
3. The non-metallic spoolable composite pipe of claim 1 configured to operate in a dry gas environment having a hydrogen sulfide partial pressure of up to 10 barg.
4. The non-metallic spoolable composite pipe of claim 1 , where the spoolable composite pipe is configured to operate at temperatures of from about 80° C. to about 110° C.
5. The non-metallic spoolable composite pipe of claim 1 , where the inner extruded tubular liner is a monolayer extruded tube.
6. The non-metallic spoolable composite pipe of claim 1 , where the aliphatic polyketone is co-extruded with one or more thermoplastic polymer to provide the inner extruded tubular liner having a multilayer system comprising an inner aliphatic polyketone layer and a thermoplastic polymer layer surrounding the aliphatic polyketone layer.
7. The non-metallic spoolable composite pipe of claim 1 , where the spoolable composite pipe is unbonded, semi-bonded, or bonded.
8. The non-metallic spoolable composite pipe of claim 1 , where the polymer reinforcement layer comprises a material selected from the group consisting of dry glass fibers, aramid fibers, carbon fibers, steel fibers or strips, glass-reinforced epoxy laminates, and unidirectional thermoplastic composite tapes.
9. The non-metallic spoolable composite pipe of claim 1 , further comprising a bonding layer between the liner and the reinforcement layer.
10. The non-metallic spoolable composite pipe of claim 1 , further comprising a bonding layer between the reinforcement layer and the cover.
11. A method of producing the non-metallic spoolable composite pipe for oil and gas flowlines of claim 1 , the method comprising:
extruding the aliphatic polyketone having the formula (I) to form the inner tubular liner;
forming the polymer reinforcement layer over the inner extruded tubular liner to form the non-metallic spoolable composite pipe; and
providing the outer extruded tubular cover over the thermoplastic-based reinforcement layer.
12. A method of transporting a hydrocarbon fluid having an aromatic content of up to about 35% by volume based on the total hydrocarbons content, the method comprising:
providing the non-metallic spoolable composite pipe for oil and gas flowlines of claim 1 ; and
introducing the hydrocarbon fluid in the non-metallic spoolable composite pipe.
13. An internally lined pipe for oil and gas flowlines, comprising:
an inner extruded tubular liner configured to be in direct contact with a fluid comprising hydrocarbons flowing through the internally lined pipe; and
a carbon steel pipe surrounding the inner extruded tubular liner;
where the inner extruded tubular liner comprises an aliphatic polyketone having the formula (I)
[[—CH 2 CHR 1 (C═O)—] n [—CH 2 CHR 2 (C═O)—] m ] p , (I)
where R 1 and R 2 are independently from one another the same or different,
where R 1 is selected from the group consisting of hydrogen and an alkyl group, and
where R 2 is an alkyl group, and
where n is less than 0.5 and n+m=1,
where p is an integer between 500 and 5000,
where structural units [—CH 2 CHR 1 (C═O)—] and [—CH 2 CHR 2 (C═O)—], are randomly distributed, blocked or both, and
where the internally lined pipe is configured to operate at temperatures of up to about 110° C., and to carry hydrocarbons having an aromatic content of up to about 35% by volume of the total hydrocarbons content.
14. The internally lined pipe of claim 13 configured to carry hydrocarbons having an aromatic and cyclo-aliphatic content of up to about 50% by volume of the total hydrocarbons content.
15. The internally lined pipe of claim 13 configured to operate in a dry gas environment having a hydrogen sulfide partial pressure of up to 10 barg.
16. The internally lined pipe of claim 13 , where the internally lined pipe is configured to operate at temperatures of from about 80° C. to about 110° C.
17. The internally lined pipe of claim 13 , where the internally lined pipe has a permeability of less than about 2×10 −7 cm 3 (STP)·cm/cm 2 ·s·bar when exposed to a dry gas environment comprising hydrogen sulfide, carbon dioxide, and methane.
18. The internally lined pipe of claim 17 , where the dry gas environment comprises about 10% hydrogen sulfide, 10% carbon dioxide, and 80% methane.
19. A method of producing the internally lined pipe for oil and gas flowlines of claim 13 , the method comprising:
extruding the aliphatic polyketone having the formula (I) to form the inner tubular liner; and
internally lining the carbon steel pipe with the inner tubular liner.
20. A method of transporting a hydrocarbon fluid having an aromatic content of up to about 35% by volume based on the total hydrocarbons content, the method comprising:
providing the internally lined pipe for oil and gas flowlines of claim 13 ; and
introducing the hydrocarbon fluid in the internally lined pipe.