6 Applications & Limitations

6.1   Thermoplastic hose umbilical

Most of the umbilical fabricated to date have used thermoplastic tubes as fluid carriers. Frequently, the electrical conductors are installed separately, but they have been included in some designs, usually termed "electrohydraulic umbilical". Separate control and chemical umbilical were often chosen because of the possible incompatibility between one of the injected chemicals and the hose liner. Such an incompatibility could then result in a chemical attack of the critical element i.e. hydraulic hoses and electric cable insulation with the subsequent loss of control and a total field shutdown. Although chemical compatibility testing was carried out to verify the suitability of the hose liner for transporting the specific chemicals (and alternatives) there was always the risk that an incompatible chemical could be introduced over the field life leading to failure. In addition, the accelerated ageing tests in which the hose liner material is tested with the chemicals at elevated temperatures, although satisfactory, cannot be considered as a fully guaranteed guide to long term deterioration. They are useful in that they will identify most incompatibility problems in a reasonable time.

In the umbilical design, there is a tendency to request duplication of the electrical components, both power and signal. In addition, there is often a requirement to design the umbilical to minimize the cross-sectional area. This may be because of limitations in the I/J tube diameter or handling capacity limitations of transportation or lay vessel reel/carousel.

Power conductors, signal pairs and hydraulic hoses of different diameters and with different elasticity properties are then bundled together using either a planetary machine resulting in a helical lay-up or an alternate clockwise-anticlockwise method known as S-Z. This latter method has a distinct advantage in that it can lay-up longer lengths without joints because of the size limitations of cable drums which can be accommodated on planetary machines.

In addition to the components having different elasticity, the back tensions of each component as they are transferred from the reels or drums to the lay-up machine may be unequal. This residual tension combined with the effects of dynamic forces due to installation vessel motions, the compressive forces due to hydrostatic pressure and potential compression due to the near position in free hanging configuration, may lead to the breaking of electrical cables.

Electro-hydraulic umbilical riser should be designed to withstand dynamic loads induced by FPS. Such umbilical would have a very high degree of radial symmetry and the lay-up angles for all conductor cables and hoses would be high to give the necessary flexibility. They would therefore have a larger diameter and would occupy much more machine time in manufacture than the equivalent static product. As a result, they would be typically 50% more expensive than an umbilical designed for static use.

During the early period of subsea production system implementation (e.g. 80’s), compatibility was not considered to be a major problem, particularly with Polyamide 11, because of its outstanding chemical resistance. Where compatibility evaluations were undertaken, these were performed using dumbbell samples of liner material immersed in the test fluid at elevated temperature (usually 70°C or 100°C). The dumbbell was manufactured nominally 2 mm thick from a sheet of material produced by means of an injection moulding process.

Life prediction was generally based on the half-life principle, whereby the time for the elongation at break to reduce to the 50% level was determined. This prediction that the rate of a chemical reaction doubles for every 10°C rise in temperature, was used to extrapolate the minimum service life at operating temperature.

For example, if a series of tests performed on liner material immersed in a fluid at 70°C shows that it takes 7 months for the elongation at break to reduce to half its original value, the predicted life at 20°C would be extrapolated as shown in Table 6.1, “Prediction life of liner material (50% life improvement for every 10°C reduction)”:

Table 6.1 - Prediction life of liner material (50% life improvement for every 10°C reduction)

Temperature °C

Life (Years/Months)

70

0y 7m

60

1y 2m

50

2y 4m

40

4y 8m

30

9y 4m

20

18y 8m


The increasing use of subsea production systems and increasing offset distances and the need to inject well service chemicals, has resulted in a wider range of control fluids and a proliferation of well service fluids. These fluids tend to be mixtures of chemicals contained within a solvent base. At this time it had been observed that one of the hose liner materials exhibited considerable anisotropic features and, it was felt, that perhaps the dumbbell test method may not necessarily be a realistic test for such materials, particularly, with fluids of a "cocktail" nature.

Whilst recognising the simplicity and low cost features of the dumbbell test, a more elaborate yet simple low cost test was employed to address the anisotropic aspects. Instead of immersing dumbbells in the fluid at ambient pressure, samples of extruded tube were immersed and instead of measuring the elongation at break as a function of time, the burst pressure of the tube was monitored with time.

In order to compare the sample immersion testing with pressurised hose testing, the pressure cycling compatibility test method was developed and consists in filling the hoses with control fluids, which would be subject to pressure cycling at elevated temperatures.

The qualification programme for a standard hydrostatic hose test in accordance with [20] for hoses up to 10,000 psi rated working pressure is as follows:

  • Impulse (200,000 cycles at 135% of rated working pressure at 93°C);

  • Leakage (70% of minimum burst pressure for 5 minutes);

  • Burst (minimum 4 times the rated working pressure);

  • Change in length (±2% at rated working pressure).

Stability of the service fluid is an important consideration and any instability could give rise to localised incompatibility with a hydraulic line.

Stability testing of the service fluid should be undertaken to qualify a fluid and to highlight any potential problem areas. It is understood that API 17F specification (Ref.[4]), "Subsea Control Systems", will include such tests.

The same consideration needs to be given to well service chemicals where separations of products are not uncommon. Where hydraulic lines are installed in a vertical shape, e.g. J-tube, Floating Production System, the potential for separation is greatly increased. The impact of any fluid modifications, however minor, should be fully evaluated before being introduced into a hydraulic line.

Regardless of the materials of construction of a hydraulic line (polymeric, elastomeric or metallic), compatibility testing should be performed with the actual line design to be used in service, in order to minimise the risk of problems arising after manufacture of the umbilical system.

With thermoplastic polyester, the small volumes of additives (lubricant, biocide, etc.) in the control fluid can have a significant effect on the rate of chemical reaction between the fluids and the polymer.

For polymeric hose liners, the rate of increase in chemical reaction is more severe when compared with the historical methods based on dumbbell and tube samples, accelerated without stress.

For polyamide 11, the material would be expected to withstand chemical compatibility and stress ageing. It has been demonstrated that a service life in excess of 20 years for temperature up to 40°C is possible; there are examples of at least 16 years extended service life experience for typical North Sea operational temperatures.

Polymer mechanical properties are shown below in Table 6.2, “Polymer mechanical properties”:

Table 6.2 - Polymer mechanical properties

PROPERTIES

UNITS

ASTM

HDPe

XLPe

Polyamide 11

Thermoplastic

Polyester

Specific gravity

Kg/dm3

D 792

0.946

O.95

1.05

1.22

Tensile strength at break

MPa

D 638

30

30

50

41

Elongation at break

%

D 638

>350

250

350

420

Modulus of elasticity

MPa

D 790

700

800

300

300

Shore hardness

Shore d

 

64

55

63

63

Thermal conductivity

W/m.K

C 177

0.32

0.32

0.33

0.22

Melting point

°C

D 3222

126

N.A.

180

184

Volume resistivity

Ohm/cm

D 257

1014

1014

1011

1013

Electric strength

KV/mm

D 1491

-

-

23

16

Resistance gain 23-C-24h

%

D 570

<0.01

<0.01

0.2

0.2

Resistance to sunlight

  

Good

Good

Good

Good

Resistance to weak acids

 

D 543

Very good

Very good

Very good

Very good

Resistance to strong acids

 

D 543

Accord. to acids

Accord. to acids

Poor

Poor

Resistance to strong bases

 

D 543

Very good

Very good

Good

Fair

Resistance to solvents

 

D 543

Good

Good

Attacked by phenols

Attacked by phenols

Resistance to crude oil without water

  

Up to 60°C

Up to 90°C

Up to 100°C

Good

Resistance to water

  

Up to 60°C

Up to 90°C

Up to 70°C

Poor

Resistance to methanol

  

Up to 60°C

Very Good

Up to 50°C

Poor


For methanol, the following Table 6.3, “Permeation rate of methanol in Polyamide 11 and Thermoplastic Polyester (69 bar)” shows the permeation rates which have been measured for Polyamide 11 (Pa11) and Thermoplastic Polyester at atmospheric pressure:

Table 6.3 - Permeation rate of methanol in Polyamide 11 and Thermoplastic Polyester (69 bar)

Temperature

Permeation rate (g.m2/mm/day)

(°C)

Polyamide 11

Thermoplastic Polyester

50

190

150

40

115

100

23

40

22

4

13.5

5


The permeation rate of methanol in XLPE lining material for internal pressures of 344 bar and 69 bar are presented in the following Table 6.4, “Permeation rate of methanol in XLPE”:

Table 6.4 - Permeation rate of methanol in XLPE

Temperature

Permeation rate (g.m2/mm/day)

(°C)

69 bar (1000 psi)

344 bar (5000 psi)

60

1.35

1.81

20

0.078

1.11

4

0.018

0.079


Remarks : Comparing the permeation at 4°C and 69 bar, of the XLPE to the Polyamide 11, it can be seen that the permeation rate through the XLPE is 750 times less than that of the Polyamide.

6.2   Steel tube umbilical

Subsea requirements have changed considerably over the past 20 years. Deeper waters, longer offsets, higher reservoir pressures and temperatures - combined with an increased use of chemicals for paraffin, hydrate and corrosion control - are too demanding for traditional thermoplastic umbilical and have resulted to the development of steel tube umbilical.

Thermoplastic umbilical cannot sustain operating pressure and temperatures beyond a certain level (e.g. 5000psi, 60°C). Response time is slow due to volumetric expansion. There are also problems relating to fluid contamination and chemical permeation, along with the fact that some umbilical are difficult to clean and keep clean due to the ligamers leeching into the conveyed fluid. Additionally, end fittings are swaged onto plastic hose and are not reliable at high pressure or under the abrasiveness of well control chemicals.

A viable alternative to thermoplastic umbilical is steel tube umbilical, which offers many advantages over plastic materials. Response times increase dramatically. Much higher internal pressures at large diameters (1” at 15,000psi, for example) are achievable. Fluid contamination and chemical permeation are drastically reduced.

Steel tube umbilicals are also easily cleaned and they remain clean. The tubing end fittings are welded, ensuring their integrity under pressure and the corrosiveness of well control chemicals.

Water depths of current interest limit the use of thermoplastic tubes, since they tend to collapse. Metal tubes can be sized for collapse and will not meet a limit until well beyond 10,000 feet (3000 m) for the range of diameter considered for umbilical applications. Metal tube umbilical of reasonable size should not be limited by collapse.

The steel tube umbilical design allows the steel tubes to carry the axial and compressive loads, which eliminates the need for a costly and cumbersome armour wire package that can unravel or "birdcage". The steel tube umbilicals are also lighter and have a smaller outside diameter than the equivalent thermoplastic umbilical while maintaining favourable minimum bend radii and displaying better on bottom stability.

Yet, for all the benefits over conventional thermoplastic systems, the steel tube umbilical is dealing with proven technology, and not a "new" product. Steel tube umbilical evolved from readily familiar pipeline, piping and pressure vessel and flowline bundle-type systems. The end fitting hardware, the J-tube hang-off assembly, bullnose, subsea termination, bend restrictors, bend limiters – all are conventional, field proven equipment systems.

Metal tubes offer advantages including: (1) impermeability to methanol, (2) the abilities to withstand high internal and external pressure, (3) robustness of the tubes without armouring, (4) potential reduction in umbilical cross section complexity and, in some cases, (5) better compatibility with the working fluids. However, there are still engineering considerations that must be addressed regarding metal tube umbilical, such as internal and external corrosion and, in the case of dynamic applications, fatigue performance of tubulars and end terminations and plastic straining during umbilical fabrication and handling.

Furthermore, although fabrication can be accomplished using techniques similar to those for thermoplastic umbilical, the equipment needed are different, in some cases requiring extensive modifications or completely new machinery and thus involving high steel tube umbilical procurement cost.

The following considerations should be addressed in the design of dynamic umbilical:

  • Fatigue life of material;

  • Attachment to the FPS, including design and performance of a bend stiffener;

  • Fatigue and strength of electrical conductors, if used;

  • Wear and abrasion between tubular elements.

Note: Allowing the electrical conductors to move axially, usually by providing lubricants and selecting proper insulation material, is the key to increase their fatigue life.

For dynamic applications the dynamic behaviour and fatigue life of the umbilical are two of the most important characteristics of the design. There are two critical locations that may be deficient in fatigue life and must be examined carefully: the region near the point where the umbilical contacts the seafloor (the “touchdown point or sag-bend radius”) and the hang-off level at FPS. The analysis that is required to assess fatigue life is both complex and time-consuming.

There are two conditions that create fatigue loading: (1) Vortex Induced Vibrations due to current and (2) FPS motions due to wind, wave and current conditions. However, VIV is a minor source of fatigue comparing to FPS motions.

One critical element in the design of a dynamic umbilical is the bend stiffener. This device is an integral part of the top support and serves to limit extreme stresses, due to static offset of the floating production system or strong currents, and reduce the cyclic stresses which contribute to fatigue.

As part of the material selection, the key requirement is maintaining pressure integrity and internal cleanliness for the expected life of the project. Along with the mechanical requirements, the material must resist external corrosion in seawater and mud as well as internal corrosion due to water-based hydraulic fluids and chemical (e.g. methanol).

The tubes within an umbilical are surrounded by seawater. The key parameters of seawater are temperature, oxygen concentration and pH. Another aspect of exterior environment is cathodic protection. Even though it may not be required for the umbilical material, cathodic protection may be required on other parts of the system. It is difficult to isolate these components from the umbilical. In some cases, cathodic protection not properly designed, can lead to hydrogen embrittlement, the degradation of material properties caused when hydrogen is absorbed.

Besides resisting corrosion on the inside, the umbilical material must not significantly change the hydraulic fluid characteristics and in particular the cleanliness of the hydraulic fluid, which must remain near NAS Class 6, since material particle can foul or plug the control valves in the subsea control system.

To meet these conditions, three alternative tube materials were considered:

  1. low-alloy carbon-steel;

  2. super-duplex stainless steel;

  3. titanium alloy.

Each material is further depicted in the following sections. However, it shall be retained that super duplex satisfactorily meets the different requirements and is currently the most selected material. Lean duplex zinc coated has been used in a number of projects in the Gulf of Mexico. Carbon steel difficultly meets the cleanliness requirements and has only be used in a very few cases. Titanium has never been used for umbilical tubes up to now.

6.2.1   Carbon steel:

Carbon steel offer significant cost savings in comparison with other materials but it rusts in seawater. This corrosion can be controlled with coating and/or cathodic protection (CP). Four options are possible: (1) traditional coating and sacrificial anodes, (2) a thermally sprayed aluminium (TSA) coating, (3) aluminium sheathing and (4) Zinc coating. Traditional cathodic protection with sacrificial anodes is not a good option for two reasons. First, it is difficult to make reliable anode connections to the umbilical. Second, attaching sacrificial anodes significantly increases the laying time, and hence the laying cost.

TSA acts both as a barrier coating, as well as a sacrificial anode. These coating have been used in the past, for example as a tendon coating on Conoco's Hutton TLP. There is a significant difference between spraying large diameter pipe and small diameter umbilical tubes. Small diameters decrease the efficiency of the spray process: (most of the sprayed metal does not coat the target and is lost). In addition, it is more difficult to achieve a uniform coating thickness.

The concept of aluminium sheathing is to create an outer aluminium tube around an inner carbon steel tube with a crevice between the two. There would be no metallurgical bond between the aluminium and the steel. To evaluate the aluminium corrosion resistance in seawater, one test specimen had holes drilled through the aluminium sheath, exposing the crevice between the steel and aluminium to seawater. Rapid corrosion of steel tube caused this alternative to be rejected as a means of protecting carbon steel from corrosion in seawater.

The Zinc cladding process was used for the Shell Mensa project (carbon steel tube umbilical) in which the zinc is metallurgically bonded to the substrate. Similarly to TSA, Zinc coating acts as both a barrier coating and a cathodic protection. This option was selected for Mensa as a reasonably economic solution due to the large size and quantity of steel tubes.

Internal corrosion may occur in carbon steel tubes containing either hydraulic fluid or methanol.

Pure, de-oxygenated hydraulic fluid is not corrosive to carbon steel; however, above a small concentration of seawater, pitting can be significant. The pitting of typical steel (e.g. AISI 4140) is a function of the seawater concentration in a typical water-based hydraulic fluid. Successful use of carbon steel requires that the concentration of seawater be kept below 5%. Although seawater may enter the line through negligence, it is more common for seawater to be ingested during coupling. Some have suggested that as much as 1 cm3 of seawater enter each line during coupling.

De-aerated methanol does not promote corrosion in steel. Without oxygen, corrosion rates in pure methanol and other corrosive agents are extremely low, about 0.02 mpy (millimeter per year). At standard temperature and pressure, methanol may contain up to 45ppm dissolved oxygen, whereas water can contain only 5-6 ppm. Consequently, the corrosion rate is greater in aerated methanol. Some tests have reported corrosion rates on the order of 0.1 mpy in 90% methanol 10% water solution saturated with oxygen.

6.2.2   Duplex and Super Duplex Stainless Steel

Duplex and super duplex tubing has been used for umbilical in the North Sea. Duplex steels are composed of two phases, austenite and ferrite, in a roughly 50/50 ratio. In super-duplexes, the key elements providing corrosion resistance are chromium, molybdenum, nitrogen and tungsten (not all super-duplexes contain tungsten).

Two issues are to be considered when evaluating the performance of duplex and super-duplex tubes in seawater: pitting, and hydrogen embrittlement due to cathodic protection.

Although duplex and super duplex materials perform well on standard pitting tests, these materials are susceptible to pitting in natural seawater. Local corrosion rates can be observed after exposing different samples to natural seawater for periods from several months to several years. The benefit of additional molybdenum, nitrogen and tungsten in super-duplex is demonstrated by a decrease in the pitting rate from 22 Cr duplex to 25 Cr duplex. Increased alloying on super-duplex increases the risk of forming s-phase, a third phase with very poor mechanical properties. Care must be taken to prevent the formation of s-phase when welding and heat treating these alloys. Good inspection procedures are also required.

The use of proper welding and inspection procedures overcomes the problem of hydrogen embrittlement of the super-duplex welds.

The good experience with these alloys in the North sea demonstrated their internal corrosion resistance to water based hydraulic fluids, and to methanol.

6.2.3   Titanium alloy

With decreased demand for titanium in military applications, a decrease in titanium prices was anticipated. Consequently, the use of titanium grade 12 tubing can also be considered. Grade 12 titanium is a duplex alloy, consisting of a and b phases. There are two key issues: (1) stress corrosion cracking in methanol (SCC), and (2) resistance to cathodic protection.

Titanium alloys can be susceptible to methanol-induced SCC. The addition of water to methanol can inhibit or prevent this from happening. Based on fracture mechanics tests, the minimum quantity of water required to prevent methanol-SCC in titanium grade 12 is 2%.

Titanium grade 12 tubing in seawater does not require cathodic protection. However, hydrogen embrittlement had been observed in the a phase, such as grade 9. Titanium alloys are susceptible to embrittlement when exposed to cathodic protection, and to use this material, successful mitigation strategies must be adopted.

6.2.4   Summary

Table 6.5 - Material key issues

Material

Key issues

Carbon steel

Corrosion

Duplex and super duplex

  • Pitting

  • Hydrogen embrittlement of the welds

Titanium

  • Stress Corrosion Cracking in methanol

  • Resistance to cathodic protection


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