Ccc Machinery Custom Coated Flowline Products

7/23/2019 Ccc Machinery Custom Coated Flowline Products

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Custom CoatedFlowline Products



Page 1

INDEX

1. Custom-Made Flowline Products with Internal Coating …………………

2. Examples of Custom Fabricated Products by CCC Machinery ………..... Page 3

3. Reasons to Coat Pipe Internally ………………………..……………………… Page 5

4. Cost Comparison ………........................………………..……………………… Page 5

5. Examples of Coated vs. Uncoated Internal Surfaces ….…………….…… Page 6

6. Examples of Coated Flowline Products ..……..……………………………… Page 7

7. Calculation of Hydraulic Efficiency ……….…………………………………… Page 8

8. The Effects of Internal Coating in Monetary Terms …….………………… Page 9

9. Different Coatings for Different Applications ………….…………………… Page 10

10. Summary …………………………………………………..………………………… Page 12

11. End User References ..…………………………………..………………………… Page 14

12. Contact ……………………………………………………..………………………… Page 15



Page 2

1. CUSTOM

-M ADE

FLOWLINE

PRODUCTS WITH

INTERNAL

COATING

CCC Machinery fabricates and internally coats pipes, fittings and spools according to customer s’ designs and specifications without any limitations to size, shape or design and according to theapplicable international oil industry standards.

Scope of Products

line pipedrill pipeOCTGfittingsspools

manifoldsflanged connectionssleeves for welded connections

These custom-made flowline products can be internally coated with a choice of Tuboscope Vetco’s liquid and powder applied plastic coating products, which are highly resistant to chemical andmechanical corrosion, thereby providing an unsurpassed longevity to drilling and flowline components.

Our flowline products also offer an economical and flexible method for field construction, tie-in’ s,terminations, modifications, and repair of internally coated lines, as they are designed for connectionby welding (in combination with Thru-Kote TM UB Sleeves) or with flanges.

A great number of upstream and downstream end-users in the oil, gas and water producing industriesworldwide have come to appreciate the the cost-saving and production-increasing properties of our

internally coated products.



Page 3

2. E XAMPLES OF

CUSTOM

F ABRICATED

PRODUCTS BY

CCC M

ACHINERY

Manifold design by Saudi Aramco / KOC Joint Operations (Kuwait) for fabrication and internal coating by CCC Machinery

U-sections after welding Manifold header after welding

Manifold header after sandblasting and prior to coating Coated internal surface of pipe section



Page 4

Manifold components being packed for shipment to Kuwait

Manifold after assembly at customer’s site in Kuwait

We supply the following certificates together with all our fabricated products:

Mills’ Test Certificates for bare pipe, fittings, flanges etc. issued by manufacturersWelding Procedure Specification (WPS)Procedure Qualification Record (PQR)Welder’s Performance Qualifications (WPQ)Radiographic Examination Reports

Visual Weld Inspection ReportsDesign drawingsCoating Inspection Certificates issued by Vetco Coating GmbH

Adhesion Test Report issued by Vetco Coating GmbHInspection Certificates for coating raw material issued by Akzo NobelThird party Inspection Certificate issued by customer’s prescribed inspection company X-ray images are kept on file by us for a period of minimum 5 years from date of test certificate

and are made available to the customer upon request



Page 5

3. R EASONS TO

COAT

PIPE

INTERNALLY

protect against CORROSION

increase PRODUCTION R ATES

improve H YDRAULIC EFFICIENCY by flow improvement

control DEPOSITION of paraffin, asphaltene & scale

minimize TUBING WEAR by erosion & abrasion

mechanical damage

improve FLUID PURITY

reduce COSTS through extended tubular life less maintenance less workovers less fishing lower production costs lower purchasing investment compared to higher grade steel alloys (see comparison below)

4. COST COMPARISON

Steel Alloy Cost Factor

Carbon Steel bareCarbon Steel with Internal CoatingStainless Steel 316LStainless Steel 904LInconel 625Incoloy 825

100% (base cost)150 - 200%600%900%1800%2200%



Page 6

5. E XAMPLES OF

COATED VS

. U

NCOATEDI

NTERNALS

URFACES

BaSO4 ScaleNon adhering BaSO4 Scale in an internal coated pipe, easy to remove/clean and easy to decontaminate.

Calcium Carbonate ScaleScale deposits in uncoated pipe. No scale deposits found in a coated pipe.

Salt IncrustationSalt blocking after 5 hours in a non internally coated pipe. No salt incrustation after 336 hours in internally coated pipe.

The difference between coated and uncoated pipe.



Page 7

6. E XAMPLES OF

COATED

FLOWLINE

PRODUCTS

Coatings forDrill PipeTubing and Down Hole-AccessoriesCasings

ValvesLine Pipe & Flow LinesSpools and Fittings

Custom Coating

Line Pipe Coating

Jointing system UB Sleeve for internal coated line pipe



Page 8

7. C ALCULATION OF

H YDRAULIC

EFFICIENCY

(B ARE VS

. C

OATED28"

L

INEP

IPE)

Base Data

• OD pipe: 28"• ID pipe: 27.25" (WT 0.375") = 692.15 mm• Length of Pipe String: 100 km, no geodetic difference• Gas Pressure: Scenario a) 8.0 MPa

Scenario b) 6.4 MPa• Medium: natural gas (rich on methane) at 20 °C• Density ρ: 0,78 kg/m³ at 0.1 Δ p 013 MPa absolute pressure

at 8.1 MPa: 58.74 Kg/m³ (ρ = p / R x T)

at 6.5 MPa: 41.14 Kg/m³, (absolute pressure)• Dynamic Viscosity: 11.1 x 10^-6 pas at 0.1013 MPa absolute pressure,

gas constant, R, at 20°C: 470.38 j/kg k• Kinematic Viscosity: ν = η x R x T / p

ν = 11.1 x 10^-6 x 470.38 x 293.15 / (p+1) x 10^5ν = 0.1889 x 10^-6 m²/s at 8.0 MPaν = 0.2355 x 10^-6 m²/s at 6.4 MPa

• Velocity of Medium: 10 m/s

Scenario a) 8,0 MPa B ARE PIPE - pressure 8,0 MPa COATED PIPE - pressure 8,5 MPa

Roughness Factor, k 0,08 mm (80 microns) 0,005 mm (5 microns)

Reynolds No.RE = v x ID / ν

RE = 10 x 0,69215 / 0,1889 x 10^-6= 36.641.080

RE = 10 x 0,69215 / 0,1889 x 10^-6= 36.641.080

Factor ID / k = 8.651,8 = 138 4300acc. to Nomogram ofPrandtl-Colebrookfriction factor λR

λR = 0.0122 λR = 0.0085

Pressure Loss Δ p = ρ /2 x v² x λR x L/ID

Δ p = 58,74/2 x 10² x 0,0122 x 100000/0,69215 Δ p = 5.176.826 Pa ~ 52 bar (5,2 MPa)


52 bar pressure loss (uncoated) 36 bar pressure loss (internally coated)

Conclusion: Flow Improvement with Coating = 30,8%

Scenario b) 6,4 MPa B ARE PIPE - pressure 6,4 MPa COATED PIPE - pressure 6,5 MPa

Roughness Factor, k 0,08 mm (80 microns) 0,005 mm (5 microns)

Reynolds No.RE = v x ID / ν

RE = 10 x 0,69215 / 0,2355 x 10^-6= 29.390.658

RE = 10 x 0,69215 / 0,2355 x 10^-6= 29.390.658

Factor ID / k = 8651,8 = 138 4300acc. to Nomogram ofPrandtl-Colebrookfriction factor λR

λR = 0,0124 λR = 0,087

Pressure Loss Δ p = ρ /2 x v² x λR x L/ID


Δ p = 41,14/2 x 10² x 0,087 x 100000/0,69215 Δ p = 2 585 552 Pa ~ 26 bar (2,6 MPa)

37 bar pressure loss (uncoated) 26 bar pressure loss (internally coated)

Conclusion: Flow Improvement with Coating = 29,8%



Page 9

8. THE

EFFECTS OF

INTERNAL

COATING IN

MONETARY

TERMS

Effects of Internally Coated Tubing

Lower Flowing PressuresLower Abandonment PressureLower Injection Pressure

Accelerated Revenues from Increased ProductionProtection from CorrosionProtection from mechanical damageProtection from stimulation

Gas Production Field Results

Coating: TK-236Reservoir Pressure: 2,500psiWellhead Pressure: 1,500 psiTubing Size: 5 ½” 13CR Coating Roughness: < 5 microns (after 10 years)Gas Capacity Coated Pipe: 1.88 million m3 per dayGas Capacity Bare Pipe: 1.64 million m3 per day

The operator realizes a 15% increase in production capacity with internal coating.

Gas Production Field Results Cost of Coating vs. Increased Revenues

0

10

20

30

40

50

60

70

80

G a s R a t e M M C F D

A B C D E

W e l l s

Bare Coate d

$0

$200.000

$400.000

$600.000

$800.000

$1.000.00

0

$1.200.00

0

$1.400.00

0

A B C D E



Page 10

9. DIFFERENT

COATINGS FOR

DIFFERENT

APPLICATIONS

Tuboscope Vetco Coating Product Line

Coating TypeTemperature

°F °CPrincipal Service

TK-2 Phenolic(liquid)

400° 204° Oil Production, Water injection, Co2 and organic acidresistance.

TK-7 Modified Phenolic(liquid)

400° 204° Sour gas and oil to 300 °F, oil, gas and Co2 to 400 °F

TK-21 Epoxy Polyamide(liquid)

150° 66° Water, crude oil, mild caustic, mild hydrocarbons.

TK-15 Modified Novolac(powder)

300° 149° Oil, natural gas, fresh and salt water,sweetcorrosion(Co2), mild H2S, and alkaline service.

TK-33 Urethane(liquid)

225° 107° Paraffin and scale prevention.

TK-34 Modified Ep-Phenolic(liquid/powder)

* * Drill Pipe

TK-69 Epoxy mod. Phenolic(liquid/powder)

250° 121° Oil, fresh and salt water, Co2 acids, causticcompletion fluids, and gases in miscible injectionsystems.

TK-70 Epoxy (powder) 175° 79° Oil, fresh and salt water handling service. Excellent instimulation acids.

TK-99 Polyamide(nylon powder)

225° 107° High flexible coating for line pipe and tubing in oil,fresh and saltwater service.

TK-216 Modified Ep-Phenolic(powder)

200° 95° Surface and subsurface, water handling systems,crude oil, mild caustic and mineral acids, anddisposal wells.

TK-236 Modified Novolac(powder)

400° 200° High pressure, sweet and sour oil/gas wells, andtertiary oil recovery systems.

Coating Chemistry

Chemistry Characteristics

Epoxy Temperature limit 225ºF (95°C), the amount of flexibility and temperatureresistance are inversely related. Inherently have a fair amount of chemical

resistance.

Phenolic Temperature limit 400ºF (204°C), high abrasion and temperatureresistance along with good chemical resistance. Can be brittle.

Epoxy Phenolic Temperature limit 250ºF, produce a middle of the road coating with goodflexibility, temperature resistance, and chemical resistance.

Novolac(Phenol /Epoxy/Cresol)

Temperature limit 400ºF (204°C), excellent chemical resistance in acid andalkaline environments, temperature resistance close to a phenolic, andflexibility similar to a phenolic.

Nylon Temperature limit 225ºF (95°C), a thermoplastic, excellent flexibility andabrasion resistance with very good chemical resistance.



Page 11

Polymeric Coating Systems for Down Hole Applications

Liquid applied, baked onPowder applied, baked on

Factors determining Coating Selection

EnvironmentsPressureTemperatureph level

VelocitiesWell/Line design

Well treatments

Types of Downhole Corrosion

Chemical corrosion: CO2, H2S, Cl, Oxygen, WaterMechanical corrosion: SCC, Erosion, FatigueElectro-chemical, Galvanic corrosion

Coating Performance Influenced by

Pipe quality

Pipe handling systemsPipe running proceduresConnection systemsWell intervention and wire line workDesign of wire line equipment

Primary Factors Influencing Flow Inside Pipe

Velocity of medium Viscosity of mediumGeometry of pipeRoughness of pipe surface

Primary Considerations When Selecting Internal Coatings

Compatibility with service environment Applicator procedures & quality programPipe handling practicesProduction practicesMechanical properties of coating

Are formulator, coating manufacturer & applicator unified?



Page 12

10. SUMMARY

IMPROVEMENT OF TUBING EFFICIENCY BY ELIMINATION OF INTERNAL CORROSION AND/OR SCALING

To a great extent, the profitability of production and injection wells depends on the lifetime of the used tubing string. Thereplacement of a tubing string always creates additional costs for buying new tubes, for workover services, the inspection andtransportation of pipe. Also, lost production has to be considered as a major cost item.

Taking above facts into consideration it is easy to conclude the following:

The extension of the operational time between workovers means to be the key function regarding the profitability of theproduction and/or injection well.

Among several possibilities such as the utilization of corrosion inhibitors or the utilization of high alloy steel, internal coating oftubular has proven to be successful in practice:

Coating + inhibitorsCoating + high alloy steel

Almost all types of corrosion which appear in connection with oil production and water injection today, can be fought byapplication of Tuboscope's internal powder coating systems.

Types of Corrosion:

CO2-CorrosionH2S-Corrosion (up to 30% H2S content)Oxygen CorrosionBacterial CorrosionSaltwater Corrosion

Following the latest materials and application techniques, new internal coatings had been developed which can be utilized at

temperatures up to 200°C with a totally holiday free surface. Even gas pressures > 500 bar inside the production tubular withrapid decompressions will not create any problem to Tuboscope Vetco's internal coating systems today.

Most of the tubing connections in use - which admittedly represent critical areas inside the string with regard to thehomogeneity of the internal coating - can reliably be coated according to Tuboscope's Coating's Procedures and Tuboscope'sSOP. With some caution during the trip-in (using Stabbing Guides) these critical areas remain holiday-free even afterinstallation.

OTHER ADVANTAGES OF INTERNAL COATING SYSTEMS

Among its major task to prevent corrosion, the internal coating provides other advantages, i.e. prevention of scale built-up andimprovement of volumetric performance.

Paraffin, carbonate deposits and salt scale as well as deposits of radioactivity containing materials can be delayed up to three to

four times if using internally coated pipe. This can be achieved because of the very smooth coating surface of < 5 µm. This verylow surface roughness also leads to a tremendous improvement of the hydraulic conditions (volumetric efficiency), which worksout very positively with higher production respectively injection rates. Production increase of > 20 % is achieved.

From time to time most production wells need to be stimulated with acid. Also for this type of work the coating will protect thetubing string effectively. The best results for the extension of the operational time of a production well will be achieved if inaddition to the coated tubing all other components used forproduction and injection are coated, i.e. packers, pup joints, subs, tubing hanger etc. Other downhole equipment in contactwith corrosive fluids should be coated as well.

Above ground the gathering lines, valves etc. should be coated to prevent corrosion.



Page 13

Example: CORROSION PROTECTION AND IMPROVED HYDRAULIC EFFICIENCY OF DRILL PIPE

Internally coated drill pipe are increasingly used since more than three decades. As a passive corrosion protection the coating isacting as a barrier to avoid direct contact between the steel pipe and the corrosive medium (fluid/gases etc.), thus avoidingcorrosion.

Drilling:Today's used drilling fluids can be classified as 'non corrosive' up to 'extremely corrosive'. Since within the lifetime of a drillstring the utilization will be for all different environments, possible corrosion caused by aggressive muds have to be considered.

Testing and Stimulation:Downhole tests as well as stimulation services very often initiate extremely corrosive environments. Especially CO2 and H2S areinfluencing the corrosion rate. Acids used for stimulation purposes in connection with high bottom hole temperatures lead tohigh corrosion rates although stimulation periods are relatively short.

Storage of Drill Pipe:

Practically all drill pipes remain in storage for shorter resp. longer periods. This can happen directly at the rig site or at the pipeyard. During this time the uncoated internal drill pipe surface very often is subject to the so-called rack corrosion. Left drillingfluid, oxygen and condensate are generating a corrosive environment especially attacking the internal surface of drill pipe.

ADVANTAGES OF INTERNAL COATING

Corrosion ProtectionPrimarily corrosion within drill pipe is starting as a type of pitting corrosion. Due to cyclical stresses as encountered in drillingany given section of the drill pipe in operation is permanently under tensile stress (weight of the string), internal respectivelyexternal pressure (mud system) and under alternate compressive and tensile stresses due to the deviation of the hole beingdrilled, the corrosion pittings develop into transversal cracks (notch effect). This phenomenon, which is called “stress corrosioncracking”, is developing perpendicular to the main stress direction. Although the transversal cracks inside a drill pipe generallydevelop over the entire length, a certain preference for the end areas is found in practice due to the change in cross sectionalareas. Washouts and/or ruptures predominantly up to one meter behind the upsets are known in the drilling industry.

With today's application of internally coated drill pipe the internal corrosion can be controlled. Without internal corrosion nonotch effect can occur.

Stress corrosion cracking with all consequences such as washouts and/or pipe ruptures does not represent a problem anymoreif drilling companies uses internally coated drill pipe. Even wireline cuts which may develop after some time in service -especially within the tool joint and upset areas - do not limit the positive performance of internal coatings.

Hydraulic EfficiencyOne major advantage of internally coated drill pipe is found in the improved hydraulic efficiency. Effected by the very smooth(glossy) internal surface of the drill pipe, the pressure drop can be reduced considerably inside the drill string. This results ineither energy savings during drilling or (more probably) in a higher drilling speed since a higher pressure is available at the bit.

Energy savings of > 9 % and betterCirculation rates of > 14 % can be achieved

An additional positive effect is the reduction in scale build-up achieved by the glossy and smooth internal surface. Moreover, thecleaning of internally coated pipe is much easier and more efficient.

SummaryToday more than 90% of the western world drill pipe are internally plastic coated providing a less risk drilling operation, anincreased life time and energy savings while drilling. It is standard to the drilling industry to day to utilize coated drill pipe evenduring harsh drilling environments.

Corrosion mitigation costs are reduced by extending life of down hole tubular goods.

Lower descaling costs and longer production schedules.

Increased production in high volume wells or smaller pipe sizes can be utilized.

Greater mud velocities in drilling or reduced pump maintenance by reduction of pressure.

Eliminates contamination of a reservoir with corrosion products during water flooding.



Page 14

11. END USER R EFERENCES

The following customers are using coated industrial items for the oilfield, drinking water, waste water and sewage, as well asfor the mining industry.Coated items are: pipes, pipe spools, fittings, flanges, valves (ball valves, gate valves, check valves) etc. coated with fusionbonded powder coatings or thermal cured liquid phenolics.

Customer Country Customer Country

ADNOC (Abu Dhabi National Oil Co.) United Arab Emirates Mobil Germany

Agip Congo Mokveld Valves Netherlands

Aker Subsea Norway NAM B.V. (Nederl. Aardolie Maatsch.) Netherlands

Al-Furat Shell Syria NIGC Iran

AMOCO Scotland NOC Libya

AMOCO Gabon Normec Oilfield Products Germany

ARAMCO Saudi Arabia OMV AG Austria

Baker Hughes Inteq Germany Orbit Valve Italy

Baker Oil Tools Germany Petro Valve Italy

BEB Erdgas und Erdöl GmbH Germany Preussag AG Germany

Bjorge Offshore Norway Raimondi Italy

BP (British Petroleum) North Sea Ring-O-Valve Italy

BP Expro (Britoil) United Kingdom RMA Germany

BRDR Christensens Haner A/S Denmark Ruhrgas AG Germany

CONOCO Scotland RWE Germany

CONOCO North Sea SDT Valve FranceConoco (UK) Ltd. United Kingdom Shell Expro North Sea

DEA Mineralöl AG (formerly Texaco) Germany Shell Expro Scotland

DEE (Deilmann Erdöl Erdga GmbH) Germany Solber & Andersen Norway

Dong Denmark Sonatrach Algeria

EA Mineralöl AG Germany Sonatrach Algeria

EDECO Netherlands Statoil Norway

EE Caledonia (formerly Occidental Petrol.) Scotland Sun Oil Scotland

Elf Acquitaine France TOMEK (Total Oil Marine Aberdeen) North Sea

Frames Process Systems Netherlands Tormene SpA Italy

Gaz de France France UNOCAL Netherlands

Gazprom Russia VAG GermanyHaugesund Mek. Verkst Norway Vitas Srl Italy

KOC (Kuwait Oil Company) Kuwait Waha Libya

Kvaerner Subsea Contr. Norway Wintershall AG Germany

Marathon Oil United Kingdom Zueitina Libya

Please contact us if any detailed field reports from the existing end users are required.



Page 15

12. CONTACT

Company Residence Postal Address

CCC Machinery GmbHTubular DivisionPalmaille 67D-22767 HamburgGermany

CCC Machinery GmbHTubular DivisionPO Box 50 10 40D-22710 HamburgGermany

Name Title / Function Direct Tel. E-mail

Detlev Wahl Managing Director +49 40 38022 7401 [email protected]

Sabine Kürtz Assistant +49 40 38022 7402 [email protected]

Ekkehard M. Ebert Director Tubular Div. +49 40 38022 7454 [email protected]

Björn Laubscher Area Manager Sales +49 40 38022 7453 [email protected]

Mohamed Drahmoune Area Manager Sales +49 40 38022 7452 [email protected]

Jorge Alejandro Prado Area Manager Sales +49 40 38022 7429 [email protected]

Niklas Hemptenmacher Area Manager Sales +49 40 38022 7456 [email protected]

Christian Wille Order Processing +49 40 38022 7476 [email protected]

Fax Number Tubular Division +49 40 38022 7444

VAT Registration Number DE 812668979

Company Registration Number HRB 77678

Ccc Machinery Custom Coated Flowline Products

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