Valhall – Weathering properties and behaviour at sea - In relation to oil spill response - OC2021 A-063

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302006208 - Open

Report

Valhall – Weathering properties and behaviour at sea

In relation to oil spill response

Author(s)

Kristin Rist Sørheim Oddveig M. Bakken

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PROJECT NO. REPORT NO. VERSION

Page 1 of 65

SINTEF Ocean AS Address:

Postboks 4762 Torgarden NO-7465 Trondheim NORWAY

Switchboard: +47 46415000

Enterprise /VAT No:

NO 937 357 370 MVA

Report

Valhall – Weathering properties and behaviour at sea

In relation to oil spill response

REPORT NO.

OC2021 A-063

PROJECT NO.

302006208

VERSION 2.0

DATE 2021-09-14

KEYWORDS:

Weathering;

Valhall crude oil;

Oil spill response

AUTHOR(S)

Kristin Rist Sørheim Oddveig M. Bakken

CLIENT(S) AkerBP ASA

CLIENT’S REF.

Harald Kvernstrøm

NUMBER OF PAGES/APPENDICES:

65 incl. 4 Appendices

CLASSIFICATION Open

CLASSIFICATION THIS PAGE Open

ISBN

978-82-7174-421-2

ABSTRACT

A standardized weathering study has been conducted on Valhall crude oil at 13 °C in 2021. Dispersibility testing on Valhall included the dispersant Dasic Slickgone NS to estimate the viscosity limits and time window for dispersant use. In a previous study on Valhall (Moldestad et al., 2001), the dispersibility limits were based on Corexit 9500A.

The SINTEF Oil Weathering Model (OWM) is used to predict the weathering properties of Valhall at sea. The weathering properties of Valhall are also discussed in relation to oil spill response.

PREPARED BY

Kristin Rist Sørheim

CHECKED BY Per S. Daling

APPROVED BY Andy Booth

Andy Booth (Sep 14, 2021 16:07 GMT+2) Kristin R. Sørheim (Sep 14, 2021 16:09 GMT+2)

Kristin R. Sørheim Per S. Daling (Sep 14, 2021 16:16 GMT+2)Per S. Daling

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Document History

VERSION DATE VERSION DESCRIPTION

1.0 2021-07-12 Draft version for review

2.0 2021-09-14 Final version

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Executive summary

Spilled oils undergo changes when weathered on the sea surface. These changes affect oil behaviour and consequently oil spill preparedness. Oil weathering varies over time and with different environmental conditions. The lifetime of an oil spill at sea depends on the oil's properties, emulsification, release scenario, and environmental conditions (temperature, wind, waves). Natural dispersion and evaporation are the main weathering processes that remove an oil spill from the sea surface. Based on input from the experimental weathering data of the oil, the SINTEF Oil Weathering Model (OWM) has been used to predict the properties of oil as it weathered over time. This summary gives a brief overview of the main changes predicted for Valhall crude oil when weathered on the sea surface.

Compared to many other Norwegian crude oils, this weathering study of Valhall 2021 shows the following properties relevant for the behaviour, if spilled at sea:

• Valhall is a paraffinic crude oil with medium density (0.842 g/mL) with a content of volatile (42 vol

%, 250°C+) that cause a moderate degree of evaporative loss: E.g. after 12 hours the evaporative loss is in the range of 25-35 wt. %.

• The combination of a medium content of wax (4.99 wt.%), asphaltenes (0.04 wt.%), and density, Valhall forms stable water-in-oil emulsions with high water uptake of 70-75 vol .%

• The emulsion formed are expected to be persistent on the sea surface. E.g. the OWM predictions indicate a lifetime at 15 m/s wind speed of 2 days. In calmer weather conditions the lifetime is predicted to be >5 days.

• As much as 65 % of the oil can still remain on the sea surface in very calm weather conditions (2 m/s wind speed) after 5 days, but due to the emulsification the overall volumes the oil has increased with a factor of 1.5 times relative to the volume of oil released.

• In winter conditions, the residue at sea may form semi-solid lumps/material due to the high pour point of the 200 and 250°C+residues (+21 to +24 °C) representing about 3 hours to 2 days weathering at sea.

In summer conditions, a remaining residue may solidify at sea after 2-3 days but expect to be less pronounced than in winter conditions.

Risk of fire /explosion hazard in oil spill response:

If free gas is not associated with an oil release (e.g. surface release of stabilized oil at 1 atm.), the flash point of the oil is the most important parameter when evaluating the potential for fire /explosion hazard. In such cases when the oil is spilled on the sea surface it assumes to reach the ambient water temperature within a short time period. The fire hazard, based on the volatile components from the oil, may be high if the flash point of the oil is below the sea temperature. For Valhall, the flash point is predicted to exceed the sea temperature within the first 15 minutes at wind speeds (10-15 m/s), and within 0.5 hours at lower winds speeds (2-5 m/s).

However, for larger surface release rates, the time for the flash point to exceed the sea temperature can be extended. Moreover, some storage tanks in vessels engaged in oil recovery operations may not be classified to carry liquids with flash points lower than 60 °C. Valhall reaches this limit (60 °C) in 3 hours after a spill at calm wind speed (2 m/s) at summer and 6 hours in winter conditions respective, and more rapidly at higher wind speeds. However, this limit is not considered at relevant for oil recovery vessels with A class certification for transport of liquids (Class I/II, flash point < 60 °C).

A "safety" zone should be established early and downwind from the spill site before any response actions in case of an acute oil spill involving free gas. In a response operation, explosimeters should be utilized to measure concentrations of free gas to minimize the risk for fire and explosion hazard at the spill site.

Effect of adding emulsion breaker:

The emulsions formed were stable but easily released (75-100%) water when adding concentrations (500 and 2000 ppm by weight) of the emulsion breaker (Aerosol OT-SE surfactant). The highest concentration (2000 ppm) was shown to be slightly more effective than 500 ppm. Use of emulsion breaker may effectively be used during an oil spill operation to remove or reduce water from the recovered oil/emulsion which minimizes the storage volume. Emulsion breakers are normally injected at the skimmer head prior to transferring the collected oil/water to storage tanks,

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Mechanical recovery :

The risk for boom leakage in a mechanical recovery operation is more of a concern for low viscous emulsions (lower than 1000 mPa.s) compared to emulsions that are more viscous. Boom leakage is also influenced by other factors such as operational speed and weather conditions. This study shows that the emulsion viscosities of Valhall surpassed 1000 mPa.s about 6-9 hours at 5 m/s wind speed (5 and 15 °C), and about 2-3 hours at 10 m/s wind speed at 5 and 15 °C. Moreover, viscosities larger than 15-20 000 mPa.s are known to reduce the flowability of the oil/emulsion when using traditional weir skimmers. However, Valhall has predicted emulsion viscosities lower than this limit within 5 days weathering at summer and winter conditions.

Chemical dispersion:

Valhall is expected to have potential for chemical dispersion in both winter and summer conditions but overall requires energy in terms of breaking waves and /or artificial energy to enhance the dispersion. The oil was found to be good dispersible with the dispersant Dasic NS (DOR; dispersant-to-oil ratio 1:25) for viscosities

<800 mPa.s, and not (poor) dispersible >8000 mPa.s. In the field, if the viscosity of is reduced dispersible (800-8000 mPa.s), additional energy (e.g. thrusters, Fire Fighting (Fi-Fi) systems or MOB (Man overboard boats) or higher DOR and/or repeated dispersant application may increase dispersant effectiveness.

Solidification of residue at sea:

Increased weathering potentially increases the high pour points to the point of solidification (elastic properties) at the sea surface. Solidification typically arises when the pour point of the oil is 5-15 °C above the seawater temperature. In such cases, if solidified (low emulsified /water free) lumps are observed on the sea surface, a lower dispersant effectiveness is likely.

High-capacity water flushing (mechanical dispersion):

The emulsification is the limiting factor for this strategy. The predicted film thickness is > 0.2-0.3 mm which is the estimated upper limit for effective use of water flushing. Water flushing is therefore not a main response option for Valhall but could be a supplementary method in areas with thin oil films e.g., metallic /rainbow appearance in very calm weather conditions.

Monitoring and remote sensing: Monitoring and remote sensing should be used a support in a response operations for Valhall.

Short summary differences between Valhall 2021 vs. Valhall 2000

Many similarities in physico-chemical properties, but some differences for Valhall 2021:

• Higher evaporative loss of the 200 and 250°C+ residue.

• Higher density of 250°C+ residue

• Lower viscosities of the waterfree residues 200 and 250°C+

Valhall 2021 emulsification:

• Lower kinetics water uptake

• Lower water uptake

• Lower emulsions viscosities Valhall 2021 OWM predictions:

• Higher evaporative loss

• Higher emulsion viscosity mainly due to higher evaporative loss (most impact at winter conditions)

• Higher pour point (most impact in winter conditions)

• Slower water uptake

• Dispersibility limits: The viscosity limit for when the oil sis expected to be good dispersible is higher in 2021, whilst the viscosity limit for when the oil is expected not (poor) dispersible is the same:

>800 mPa.s and < 8000 mPa.s (Valhall 2021) vs. > 400 mPa.s and < 8000 mPa.s (Valhall 2001) Based on the results from the dispersibility testing, mechanical recovery should still be the main response strategy for Valhall followed by dispersant use. Use of dispersants requires breaking waves /artificial energy in very calm sea conditions for being efficient.

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2 Introduction

New oil types, from heavy crude oil to light crude oils and condensates, are continuously coming into production worldwide. Due to large variations in different crude oils’ physical and chemical properties, their behaviour and fate may vary greatly if spilled at sea. For example, the "Braer" accident at the Shetlands (1993) and the "Sea Empress" accident in Wales (1996) have demonstrated how different the fate and behaviour of the crude oils can be when spilled on the sea surface. For that reason, obtaining comprehensive knowledge about the expected behaviour of spilled oil at sea is of great importance. Moreover, the "Deepwater Horizon"

incident in the Gulf of Mexico (2010) clearly showed how the efficacy of the different response techniques changed as the oil weathered and emulsified on the sea surface over a time after the release. These past experiences and other incidents shape the knowledge base and the subsequent refinement of future operative strategies in terms of where, when, and how the mitigation methods should operate during a response operation.

Appendix A describes the general physical and chemical properties and weathering processes of oil spilled on the sea surface.

According to the Norwegian Environment Agency and the Petroleum Safety Authority Norway (Ptil) regulations for petroleum activities (Aktivitetsforskriften §59), the characterization of oils with respect to their weathering properties and fate in the marine environment should be performed for all oils coming into production. SINTEF Ocean has performed a standardized small-scale weathering study on Valhall (2021) at 13 °C. The obtained laboratory data have been used to predict the weathering properties of Valhall by use of the SINTEF Oil Weathering Model (OWM). Information about the Valhall field is given, below (Figure 2-1).

Valhall is a field in the southern part of the Norwegian sector in the North Sea. Block: 2/8. The water depth is 70 metres. Valhall was discovered in 1975, and the initial plan for development and operation (PDO) was approved in 1977.

Production started in 1982.

The Valhall area consists of a field center with five platforms connected by bridges, and four wellhead platforms that are remotely controlled from the field center. The field is powered with electricity from shore.

Valhall produces oil from chalk in the Upper Cretaceous Hod and Tor Formations. Reservoir depth is 2400 metres. The Tor Formation chalk is fine-grained and has good reservoir quality.

Oil and NGL (Natural Gas Liquids) are routed via pipeline to the Ekofisk field and further to Teesside in the UK. Gas is sent via Norpipe to Emden in Germany.

Figure 2-1 https://www.norskpetroleum.no/en/facts/field/valhall/; https://akerbp.com/en/asset/valhall/

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3 Small-scale laboratory testing of Valhall

Description of the oil sample of Valhall for testing and the experimental setup for the small-scale weathering and dispersibility methods are described in Appendix B. Physico-chemical parameters and weathering properties of Valhall from 2021 were compared with a previous study on Valhall from 2000 (Moldestad et al., 2001), this in agreement with AkerBP.

3.1 Gas chromatographic (GC-FID) characterization

The hydrocarbon profile of Valhall was analysed by use of gas chromatography (GC) coupled with Flame Ionization detector (FID). Figure 3-1 illustrates the GC-FID outputs (gas chromatograms) of the fresh oil of Valhall and the corresponding evaporated residues at three different degrees of evaporative loss of volatiles with boiling points 150, 200 and 200°C+ (see Appendix B.2). The loss of low molecular weight (volatiles) compounds (shown towards the left of the chromatogram) at the three temperatures mimics that of natural weathering (evaporative loss at sea) corresponding to approximately 0.5-1-hour, 0.5-1 day and 0.5-1 week of weathering on the sea surface. The GC-FID also provides support for the artificial evaporation of the crude oil by use of distillation.

The gas chromatograms show the n-alkanes as systematic narrow peaks. The first peaks in the chromatogram represent components with the lowest boiling points. Some of the more complex components, such as resins and naphthenes, are shown as a broad and poorly defined bump below the sharp peaks and are often described as the "Unresolved Complex Mixture" (UCM). Heavier compounds such as asphaltenes (> nC40) are not possible to analyze with this technique.

Figure 3-1 shows that Valhall is a typical paraffinic crude oil with a main range of n-alkanes from nC5 to nC30. Valhall from 221 and 2000 also have great similarities in their hydrocarbon profile, as shown in Figure 3-2.

GC/FID is an important tool for oil characterization and for oil spill identification as an initial step. Common screening parameters used for identification, as well as for the degree of biodegradation, are the nC¹⁷/Pristane and nC¹⁸/Phytane ratios. Table 3-1 shows the ratios of Valhall 2021 in comparison with the previous tested Valhall 2000. The ratios show small variations between Valhall 2021 and Valhall 2000, however Valhall 2021 has lower ratios than Valhall 2000 that can be due to some extend biodegradation in the reservoir.

Table 3-1 nC17/Pristane and nC18/Phytane ratios*

Oil name nC17/Pristane nC18/Phytane Valhall 2021 1.8 2.0

Valhall 2000 2.1 2.3

*Ratios > 1 typical for paraffinic oils, ratios < 1 typical for very biodegraded /naphthenic oil.

-: no data obtained

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Figure 3-1 GC-FID chromatograms of fresh sample and evaporated residues of Valhall 2021.

Valhall 2021-880 Fresh

Valhall 2021-880 150˚C+ residue

Valhall 2021-880 250˚C+ residue Valhall 2021-880 200˚C+ residue

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Figure 3-2 GC-FID chromatograms for fresh oils of Valhall 2021 and Valhall 2000. The retention times may differ between the chromatograms due to different temperature programs (relative comparison).

Valhall 2021-880

Valhall 2000-0601

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3.2 Asphaltenes and wax content of the fresh and weathered residues

The content of asphaltenes and wax of Valhall 2021 in comparison with Valhall 2000 are given in Table 3-2.

The Valhall crude oils (2021 and 2000) have both a medium content of wax of the fresh oil (4.99-5.13 wt.%) and low contents of asphaltenes (0.04-0.07 wt.%), in comparison with other Norwegian crude oils.

Table 3-2 Asphaltene ("hard") and wax content of Valhall 2021 vs. Valhall 2000

Oil type Residue Asph*

(wt. %)

Wax (wt. %)

Fresh 0.04 4.99

Valhall 2021 150°C+ 0.05 6.04

200°C+ 0.06 7.03

250°C+ 0.07 7.96

Fresh 0.07 5.13

Valhall 2000 150°C+ 0.08 6.33

200°C+ 0.09 7.22

250°C+ 0.11 8.14

*n-heptane (nC7) precipitation

3.3 Physical properties of the fresh and weathered residues

The physical properties of Valhall 2021 are listed in Table 3-4 in comparison Valhall 2000.

Overall, Valhall 2021 and Valhall 2000 have many similarities in their physical properties, although there are some differences. Valhall 2021 has a slightly higher evaporative loss, higher density and pour point (250°C+) than Valhall 2000. Both oils have low pour point of the fresh oil (-6 °C) that increase rapidly to considerably higher pour points with increasing evaporative loss (+24 and +21 °C for the 250°C+residue). Valhall 2021 has lower viscosities than Valhall 2000, e.g. for the 250°C+residue the viscosity for Valhall 2021 is 2850 mPa.s (10s^-1) vs. 5560 mPa.s for the similar residue for Valhall 2000. However, the viscosity of the emulsions (Figure 3-7) has normally most impact on the behaviour of the spilled oil at sea. The interfacial tension of fresh oil Valhall 2021 is 15 mN/m.

Table 3-3 Physical properties of Valhall 2021 in comparison with Valhall 2000.

Oil type Residue Evap.

(vol. %)

Residue (wt. %)

Density (g/mL)

Flash point (°C)

Pour point (°C)

Visc.

(mPa.s) 13°C (10 s^-1)

Fresh 0 100 0.8422 - -6 21

Valhall 2021 150°C+ 20.9 82.6 0.8783 36.5 9 149

200°C+ 33.3 71.0 0.8962 84.5 21 560

250°C+ 41.6 62.3 0.9087 121 24 2859

Fresh 0 100 0.8413 - -6 82

Valhall 2000 150°C+ 20.2 80.8 0.878 - 9 230

200°C+ 30.2 71.5 0.893 - 15 2160

250°C+ 38.5 63.3 0.905 - 21 5560

-:No data

The True Boiling Point curves (TBP) of Valhall 2021 in comparison with Valhall 2000 are shown in Figure 3-3. Valhall 2021 exbibits a higher distilled cumulative loss than Valhall 2000, that also reflect the higher

evaporative loss of the 150, 200 and 250°C+ residues (Table 3-4), reflecting the evaporative loss at sea.

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Figure 3-3 TBP of Valhall crude oils. TBP of Valhall 2021 from simulated distillation (Simdist GC). TBP of Valhall 2000 from crude assay.

3.4 Viscosity of fresh oil and water-free residues with different shear rates

The viscosity describes the oils' ability to resist gradual deformation by increasing shear, where viscosities of so-called Newtonian oils remain constant independent on the applied shear rate (s^-1) at a given temperature.

The opposite when shear is applied on so-called non-Newtonian oils the viscosity of such oils decreases. The dynamic viscosities (mPa.s) of Valhall 2021 fresh oil and water-free residues are given in Table 3-4 with increasing shear rates (10, 100 and 1000 s^-1) at 13 °C. The fresh oil and the residues 150, 200 and 250°C+ of Valhall 2021 clearly exhibit non-Newtonian behaviour at 13 °C, i.e., viscosities depending on the shear rates.

Non-Newtonian behaviour is also pronounced for the emulsion of Valhall (Figure 3-7).

Table 3-4 Viscosities of fresh oil and residues of Valhall 2021 with increasing shear rates (s^-1) at 13 °C.

Oil type Residue Visc.

(mPa.s) 13°C (10 s^-1)

Visc.

(mPa.s) 13°C (100 s^-1)

Visc.

(mPa.s) 13°C (1000 s^-1)

Fresh 21 17 12

Valhall 2021 150°C+ 149 106 52

200°C+ 560 365 158

250°C+ 2859 949 405

3.5 Emulsifying properties

In general, emulsification is the mixing of seawater droplets into spilled oil at the water’s surface (water-in-oil emulsion), forming a weathered oil residue that often tends to be relatively resistant to other weathering processes such as evaporation, and increases the total volume of oil due to the uptake of water into the oil. The

Boiling points 150°C, 200°C and 250°C+

reflecting evaporative loss at sea

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rotating cylinders method (Mackay and Zagroski, 1982) was used to study the emulsifying properties, and the procedure for maximum water uptake is described in Hokstad et al., 1993 (Appendix B).

3.5.1 Emulsification

Emulsification testing of Valhall 2021 were conducted on the residues of 150°C+, 200°C+ and 250°C+ to produce data for stability, viscosity, maximum water uptake, kinetics, and the effectiveness of the emulsion breaker application. Emulsions of maximum water content after 24 hours rotation are shown in Figure 3-4, below. The figure shows from left to right four emulsions prepared from the residues of 150°C+, 200°C+ and 250°C+, respectively.

Figure 3-4 Rotating cylinders of water-in-oil (w/o) emulsions of Valhall 2021 after 24 hours at 13 °C.

3.5.2 Water uptake

The rate (kinetics) of water content in the water-in-oil (w/o) emulsions as a function of time is tabulated in Table 3-5. The t1/2 values are defined as the time (hours) it takes to incorporate half of the maximum water uptake (vol. %) in 24 hours (rotating time). Valhall 2021 expressed relatively high-water uptakes for all the residues 150°C+, 200°C+ and 250°C+, which ranged from 61 to 85 vol. % (Table 3-5).

Table 3-5 Kinetics (t1/2) for the emulsified residues of Valhall 2021 at 13 °C Mixing

time

150°C+ * (vol. % water)

200°C+ * (vol. % water)

250°C+ * (vol. % water)

Start 0 0 0

5 min 15 7 6

10 min 27 8 6

15 min 32 8 12

30 min 42 29 29

1 hour 49 48 54

2 hours 53 66 64

4 hours 56 74 65

6 hours 59 78 66

24 hours 61 81 67

t ½ 0.26 0.85 0.57

* Depending on weather situation and release rate, the residues are corresponding to approximately 0.5-1-hour, 0.5-1 day and 0.5-1 week of weathering on the sea surface.

150°C+ 200°C+

+

200°C+

++

250°C+

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3.5.3 Efficiency of emulsion breaker and stability of emulsions

In mechanical recovery operations, separating oil from water enables optimal use of available storage (i.e.

facilities/tankers), and the efficiency of this separation can be enhanced by applying emulsion breakers. The effectiveness of the emulsion breaker Aerosol OT-SE surfactant was evaluated on different residues of emulsified Valhall 2021. The choice of emulsion breaker was selected in agreement with Aker BP.

The results show that the emulsified oil volume decreased significantly after treatment with the emulsion breaker in all residues, as water was released from the emulsion (Table 3-6). The emulsions were almost totally broken when adding the emulsion breaker (Aerosol OT-SE). Adding 2000 ppm of the emulsion breaker, relative to the oil was shown to be slightly more efficient to break the emulsion compared with a lower concentration of 500 ppm.

The emulsion stability was studied by quantifying the amount of volume fraction of water released from the emulsion after 24 hours settling time. Valhall 2021 formed stable w/o-emulsions of the 150, 200 and 250°C+

residues, as shown in the first main row of Table 3-6.

Table 3-6 Stability of emulsion and the effectiveness of emulsion breaker at 13 °C of Valhall 2021

Residue Valhall

2021

Emulsion breaker Water-in-oil emulsion (vol. %) at 13 °C

Stability ratio**

% Effect.

(released water) Reference 24 hours

settling *

150ºC+ None 61 61 1.00 0

200ºC+ None 81 81 0.98 20

250ºC+ None 67 66 0.98 20

150ºC+ Aerosol OT-SE 500 ppm 61 9 0.06 94

ppm: parts per million

* Reference: w/o emulsion after 24 hours rotation

*: w/o-emulsion after 24 hours rotation and 24 hours settling.

** Stability ratio of 0 implies a totally unstable emulsion after 24 hours settling; all the water is settled out for 24 hours settling. Stability ratio of 1 implies a totally stable emulsion.

Figure 3-5 (left) shows image of the stable emulsions of Valhall 2021 after 24 hours stand still (150, 200 and 250 °C+). Figure 3-5 (right) illustrates the % effectivity of settling (low values means minor water has been released from the emulsions), and % effectivity of adding emulsion breaker, high values (75-100 %) means that water has effectively been released from the emulsions.

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Figure 3-5 Left: Stable (w/o) emulsions of Valhall 2021 after 24 hours rotating followed by 24 hours stand still (s at 13 °C. Right: % efficiency of settling, and emulsion breaker (EB) on Valhall 2021. High %

effectivity means that water has been released from the emulsion.

3.5.4 Emulsion viscosities

The viscosities of emulsified residues of Valhall 2021 are given in Table 3-7 (including waterfree residues, Table 3-4). The emulsions behave as non-Newtonian fluids due to the increasing degree of weathering (evaporation and water uptake), with higher viscosities at a lower shear rate (10 s^-1) compared to the viscosities measured at higher shear rate (100 s^-1).

Table 3-7 Viscosities waterfree residues and emulsions of Valhall 2021 at 13 °C Residue

Valhall

Water content

Viscosity (mPa.s)

2021 (vol. %) 10 s^-1 100 s^-1

Fresh 0 21 15

150°C+ 0 149 91

200°C+ 0 560 301

250°C+ 0 2859 949

150°C+ 50 528 211

200°C+ 50 1720 637

250°C+ 50 3890 859

150°C+ 75 578 293

200°C+ 75 3011 1013

250°C+ 75 5812 1297

150°C+ 63 588 234

200°C+ 81 1654 549

250°C+ 75 5480 805

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3.6 Chemical dispersibility

The dispersibility testing of Valhall 2021 crude oil included:

• Dosage testing with use of relevant dispersant.

• Systematic testing on weathered /emulsified samples as a basis to predict the time-window for effective application of dispersants.

Screening testing of different dispersants were not performed on Valhall 2021, in agreement with Aker BP. In a previous study (Moldestad et al., 2001), Corexit 9500A was used to estimate the dispersibility (viscosity) limits for dispersant use. In this study, Dasic Slickgone NS was used to estimate dispersibility limits. Dasic Slickgone NS is also the main dispersant agent in NOFO’s stockpile, today. The dispersibility limits (viscosities) are further used as input to the SINTEF Oil Weathering Model (OWM) to predict the time-window for dispersant use.

3.6.1 Dosage testing

Dosage testing at 13 °C was performed using Dasic Slickgone NS on the Valhall 2021 emulsion (200°C+ / 50 vol. %). The dosage test helps to identify optimal design conditions for dispersant use and was performed with dispersant-to-emulsion ratios (DER) of 1:25, 1:50, 1:100 and 1:200, and with no dispersant added. The results are presented in Table 3-8 and Figure 3-6. Pictures from the dosage testing on Valhall 2021 are given in Figure 3-7. The results show a clear dosage dependant effect for the high-energy test (MNS), where DER 1:25 and 1:50 showed the highest effects (87-88%). The MNS test produced formation small, dispersed droplets (< 70 -100 µm) reflecting good dispersion by adding the dispersant to the oil (emulsion), see Figure 3-7. For the low- energy test (IFP), the results indicated negligible effect of adding dispersant to the emulsion, producing larger oil droplets in mm size. This means that breaking waves (> 5 m/s wind speeds) or artificial energy in non- breaking waves (< 5 m/s wind speeds) are necessary to disperse surface emulsion of Valhall. No formation of small oil droplets was observed with no dispersant added to the emulsion of Valhall, as shown in Figure 3-7.

Table 3-8 Dosage testing on 200°C+/50% emulsion of Valhall 2021 at 13 °C.

Dispersant (dispersant-to- emulsion ratio)

% Effectiveness IFP

% Effectiveness MNS

Dasic NS (1:25) 3 87

Dasic NS (1:50) 4 88

Dasic NS (1:100) <0.5 54

Dasic NS (1:200) < 0.5 43

No dispersant - < 0.5

*Emulsion viscosity: 1720 mPa.s (10s^-1)

Figure 3-6 Results from dosage testing with use of Dasic Slickgone NS on Valhall 2021 ( 200°C+/50 vol. emulsion).

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Figure 3-7 MNS high energy test on 200°C+ 50% emulsion. Left: After adding DOR/DER 1:25 Dasic Slickgone NS. Right: No dispersant added showing no effect on the emulsion.

3.6.2 Systematic dispersant testing and dispersibility limits

A dosage ratio of 1:25 (4 wt.%) is commonly used as the standard procedure to establish the time window for dispersant application. The results from the systematic dispersant testing at 13 °C is tabulated in ^{Table 3-9}. At 13 °C the viscosity limit for when the oil-emulsion is not expected to be dispersible expressed as MNS < 5 % was not obtained in the laboratory testing. Therefore, a supplementary test at 5 °C was conducted for the 250°C+ residue to reach higher viscosity and hence lower the dispersant efficiency (Figure 3-10). Figure 3-8 shows the dispersibility limits (viscosities) expressed as a function of % effectiveness.

Table 3-9 Effectiveness of Dasic Slickgone NS on Valhall 2021 at 13 °C

Residue (vol. %) Visc. (10 s⁻¹)

Effectiveness % IFP

Effectiveness % MNS

150°C+ 0 149 68 100

200°C+ 0 560 19 100

250°C+ 0 2859 5 18

150°C+ 50 528 61 100

200°C+ 50 1720 3 87

250°C+ 50 3890 3 28

150°C+ 75 578 66 78

200°C+ 75 3011 8 79

250°C+ 66 5812 n.a n.a

150°C+ 63 588 63 98

200°C+ 81 1654 11 88

250°C+ 75 5480 8 21

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Table 3-10 Effectiveness of Dasic Slickgone NS on Valhall 2021 at 5 °C.

Residue (vol. %) Visc. (10 s⁻¹)

Effectiveness

% IFP

Effectiveness % MNS

250°C+ 50 (37) 8838 n.a 3

250°C+ 75 (51) 10649 n.a n.a

250°C+ mw (62) 11318 n.a n.a

Figure 3-8 Dispersant effectiveness limits on Valhall 2021 at 13 °C.

Valhall 2021 was found to be dispersible for viscosities lower than 800 mPa.s, reflecting > 50 % effectiveness by use of the low energy IFP-test. The upper limit for then Valhall 2021 is not or poor chemically dispersible was estimated to 8000 mPa.s expressed with effectiveness lower than 5 % using the high energy MNS-test.

Reduced dispersibility is expected with viscosities between 800 and 8000 mPa.s and means that the oil is still dispersible but may require additional energy and/or higher dispersant dosage to enhance effective dispersion.

The dispersibility limits are also summarised in Table 3-11.

Table 3-11 Estimated viscosity limits for Visund for use of dispersant and definition of time window.

Dispersibility Criteria for effectiveness (wt. %)

Dispersibility limits based on emulsion viscosity

(mPa.s)

Chemically dispersible IFP > 50 % 800

Not/poor chemically dispersible

MNS < 5 % 8000

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4 Predictions with SINTEF Oil Weathering Model (OWM) 4.1 Description of SINTEF OWM

A systematic stepwise laboratory procedure developed at SINTEF (Daling et al., 1990) was used to isolate and map the various weathering processes that take place when oil is spilled on the sea surface. Laboratory study of Valhall 2021 was conducted at 13 °C, and the analytical data were further used as input to the SINTEF Oil Weathering Model (OWM). The experimental design for the study is described in Appendix B. The input data of Valhall to the SINTEF OWM are given in Appendix C.

The SINTEF OWM relates oil properties to a chosen set of conditions (oil/emulsion film thickness, wind speeds and sea temperature) and predicts the change rate of the oil’s properties on the sea surface with time.

The SINTEF OWM is schematically shown in Figure 4-1. The predictions obtained from the SINTEF OWM are useful tools in the oil spill contingency planning related to the expected behaviour of oil on the sea surface, and to evaluate the time window for operational response strategies in a spill operation. In this report, the presented predictions span a period from 15 minutes to 5 days after an oil spill has occurred. The SINTEF OWM is described in more detail in Johansen (1991), and in the user’s guide for the model.

Figure 4-1 Schematic input data to the SINTEF OWM and the predicted output oil properties.

Oil film thickness

Oils in OWM are categorized as condensate (non-emulsifying oil), low emulsifying oil/condensate, emulsifying oil, heavy bunker fuel or refined distillate. The categorization is based on the experimental results obtained in the laboratory. The terminal film thicknesses vary among these categories based on experimental (field) experience. Valhall is categorized as an emulsifying oil.

Seawater temperature

The prevailing weather conditions greatly influence the weathering rate of oil on the sea surface. Due to the location of the oil field, the prediction seawater temperatures chosen for Valhall 2021 was 5 and 15 °C, reflecting typically winter and summer conditions.

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Wind speed

The relationship between the wind speed and significant wave heights used in the prediction charts obtained from the SINTEF OWM are shown in Table 4-1.

Table 4-1 Relationship between wind speed and significant wave height used in the SINTEF OWM.

Wind speed [m/s] Beaufort wind Wind type Wave height [m]

2 2 Light breeze 0.1 - 0.3

5 3 Gentle to moderate breeze 0.5 - 0.8

10 5 Fresh breeze 1.5 - 2.5

15 6 – 7 Strong breeze 3- 4

4.2 Predictions of Valhall oil weathering properties

A standard surface release was used as a spill scenario. The scenario chosen is not oil field specific but selected to give predictions of the expected weathering properties of the oil based on the experimental data and specified terminal oil film thickness. A standardized scenario will also more easily compare results of weathering properties with other oils.

Input to SINTEF OWM

Oil type: Crude oil

Geographical area: North Sea Terminal oil film thickness: 1 mm

Release rate: 1.33 metric tonnes per min. in 15 min, a total of 20 metric tonnes (80 m³/hour or 1900 m³/day)

Seawater temperatures: 5 and 15 °C

Wind speeds: 2 m/s, 5 m/s, 10 m/s and 15 m/s Predicted properties

• Evaporative loss

• Viscosity

• Flash point

• Pour point

• Mass balance

The predictions are based on 5 days weathering independently if there is not predicted any remining oil within shorter time. The predictions are shown to indicate the weathering properties in cases there are patches or oil left on the surface up to 5 days.

How to use the prediction charts: an example

If the oil has drifted on the sea surface, the following prediction charts could be used to determine the weathering properties of the oil/emulsion. Table 4-2 gives an example of predicted weathering properties for Valhall 2021.

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Table 4-2 Example of weathering properties of Valhall obtained from the OWM predictions after 12 hours of weathering at 2, 5 and 10 m/s wind speed at 15 °C.

Weathering properties 12 hours

15 ˚C 2 m/s

12 hours 15 ˚C 5 m/s

12 hours 15 ˚C 10 m/s

12 hours 15 ˚C 15 m/s

Evaporation, wt. % 28 32 35 37

Flash point, °C 80 95 111 121

Pour Point, °C 18 21 24 26

Water content, vol.% 19 42 69 75

Viscosity, mPa.s * 590 1610 3860 5200

Mass balance / Oil on surface wt.% 72 67 45 11

*mPa.s = cP (mPa.s: SI-standard / cP: Industrial denotation)

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Figure 4-2 Evaporative loss of Valhall 2021 predicted at sea temperatures of 5 and 15 °C.

Property: EVAPORATIVE LOSS Oil Type: VALHALL 2021 Description:

Data Source: Sintef Ocean (2021), Weathering data used

Surface release

Amount/duration of oil spill : 20 metric tons 15.000000minute

OWModel© 13.0

Pred. date: Jul. 06, 2021 2.0

Wind Speed (m/s): 15 Wind Speed (m/s): 10 Wind Speed (m/s): 5 Wind Speed (m/s): 2

Sea surface temperature: 5°C

Evaporated (%)

Hours Days

0.25 0.5 1 2 3 6 9 12 1 2 3 4 5

0 10 20 30 40 50 60 70 80 90 100

Evaporated (%)

Hours Days

0.25 0.5 1 2 3 6 9 12 1 2 3 4 5

0 10 20 30 40 50 60 70 80 90 100

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Figure 4-3 Flash point of Valhall 2021 predicted at sea temperatures of 5 and 15 °C.

Property: FLASH POINT FOR WATER-FREE OIL Oil Type: VALHALL 2021

Description:

Surface release

OWModel© 13.0

Pred. date: Jul. 06, 2021 2.0

No fire hazard

Fire hazard in tankage (<60 °C)

Fire hazard at sea surface (below sea temperature)

Flash Point (°C)

Hours Days

0.25 0.5 1 2 3 6 9 12 1 2 3 4 5

-50 0 50 100 150

Flash Point (°C)

Hours Days

0.25 0.5 1 2 3 6 9 12 1 2 3 4 5

0 50 100 150 200

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Figure 4-4 Pour point of Valhall 2021 predicted at sea temperatures of 5 and 15 °C.

Property: POUR POINT FOR WATER-FREE OIL Oil Type: VALHALL 2021

Description:

Surface release

OWModel© 13.0

Pred. date: Jul. 06, 2021 2.0

Chemically dispersible Reduced chemical dispersibility Poorly / slowly chemically dispersible

Pour Point (°C)

Hours Days

0.25 0.5 1 2 3 6 9 12 1 2 3 4 5

-20 0 20 40

Pour Point (°C)

Hours Days

0.25 0.5 1 2 3 6 9 12 1 2 3 4 5

0 20 40

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Figure 4-5 Water content of Valhall 2021 predicted at sea temperatures of 5 and 15 °C, shear rate 10 s^-1. Property: WATER CONTENT

Oil Type: VALHALL 2021 Description:

Surface release

OWModel© 13.0

Pred. date: Jul. 06, 2021 2.0

Water content (%)

Hours Days

0.25 0.5 1 2 3 6 9 12 1 2 3 4 5

0 20 40 60 80 100

Water content (%)

Hours Days

0.25 0.5 1 2 3 6 9 12 1 2 3 4 5

0 20 40 60 80 100

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Figure 4-6 Viscosity of Valhall 2021 predicted at sea temperatures of 5 and 15 °C, shear rate 10 s^-1. Property: VISCOSITY OF EMULSION

Oil Type: VALHALL 2021 Description:

Surface release

OWModel© 13.0

Pred. date: Jul. 06, 2021 2.0

Chemically dispersible (<800 mPa•s) Reduced chemical dispersibility

Poorly / slowly chemically dispersible (>8,000 mPa•s)

Viscosity (mPa•s)

Hours Days

0.25 0.5 1 2 3 6 9 12 1 2 3 4 5

10 100 1,000 10,000 100,000

Viscosity (mPa•s)

Hours Days

0.25 0.5 1 2 3 6 9 12 1 2 3 4 5

10 100 1,000 10,000 100,000

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Figure 4-7 Predicted mass balance of Valhall 2021predicted 5 °C, wind speeds of 2 and 5 m/s.

Property: MASS BALANCE Oil Type: VALHALL 2021 Description:

Surface release

Release rate/duration: 1.33 metric tons/minute for 15 minute(s)

OWModel© 13.0

Pred. date: Jul. 06, 2021

Evaporated Surface

Naturally dispersed

Temperature: 5°C Wind speed: 2 m/s

Mass (%)

Hours Days

0.25 0.5 1 2 3 6 9 12 1 2 3 4 5

0 20 40 60 80 100

Mass (%)

Hours Days

0.25 0.5 1 2 3 6 9 12 1 2 3 4 5

0 20 40 60 80 100

/ Entrained oil

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Figure 4-8 Predicted mass balance of Valhall 2021 predicted 5 °C, wind speeds of 10 and 15 m/s.

Surface release

OWModel© 13.0

Evaporated Surface

Naturally dispersed

Mass (%)

Hours Days

0.25 0.5 1 2 3 6 9 12 1 2 3 4 5

0 20 40 60 80 100

Mass (%)

Hours Days

0.25 0.5 1 2 3 6 9 12 1 2 3 4 5

0 20 40 60 80 100

/ Entrained oil

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Surface release

OWModel© 13.0

Evaporated Surface

Naturally dispersed

Mass (%)

Hours Days

0.25 0.5 1 2 3 6 9 12 1 2 3 4 5

0 20 40 60 80 100

Mass (%)

Hours Days

0.25 0.5 1 2 3 6 9 12 1 2 3 4 5

0 20 40 60 80 100

/ Entrained oil

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Surface release

OWModel© 13.0

Evaporated Surface

Naturally dispersed

Mass (%)

Hours Days

0.25 0.5 1 2 3 6 9 12 1 2 3 4 5

0 20 40 60 80 100

Mass (%)

Hours Days

0.25 0.5 1 2 3 6 9 12 1 2 3 4 5

0 20 40 60 80 100

/ Entrained oil

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5 Comparison of OWM predictions

Weathering predictions from surface release of Valhall 2021 were compared with predictions of Valhall 2000.

The predictions are based on sea temperature of 15 °C and wind speed of 10 m/s.

5.1 Evaporative loss

Evaporation is one of the natural process that helps removing spilled oil from the sea surface. Valhall 2021 has about 2-5 % higher predicted evaporative loss compared with Valhall 2000 (Figure 5-1). The predicted evaporative loss is within expected range for medium paraffinic crude oils.

Figure 5-1 Predicted evaporative loss at 15 °C and 10 m/s for Valhall 2021 and Valhall 2000.

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5.2 Pour point

The pour point Valhall 2021 and Valhall 2000 are given in Figure 5-2. Valhall 2021 has higher pour points by time than Valhall 2000.

Figure 5-2 Predicted pour point at 15 °C and 5 m/s for Valhall 2021 and Valhall 2000.

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5.3 Water uptake

The water uptakes of the Valhall 2021 and Valhall 2000 are shown in Figure 5-3. Valhall 2021 has a slower rate of water uptake, and reach a slightly lower water uptake 75 vol% than Valhall 2000 (80 vol. %).

Figure 5-3 Predicted water uptake at 15 °C and 5 m/s for Valhall 2021 and Valhall 2000.

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5.4 Viscosity

Figure 5-4 shows the predicted (emulsion) viscosities of Valhall 2021 and Valhall 2000. Valhall 2021 has lower initial viscosity than Valhall 2000 but increases to reach higher viscosities after 4-5 hours. Valhall 2021 may reach viscosity > 8000 mPa.s whilst Valhall about 6000 mPa.s for this scenario. The viscosities of Valhall oils are within the expected range for medium paraffinic crude oils.

Figure 5-4 Predicted (emulsion) viscosity at 15 °C and 5 m/s for Valhall 2021 and Valhall 2000.

Valhall – Weathering properties and behaviour at sea - In relation to oil spill response - OC2021 A-063

Report

Valhall – Weathering properties and behaviour at sea

Report

Valhall – Weathering properties and behaviour at sea

Document History

Table of Contents

Executive summary

2 Introduction

3 Small-scale laboratory testing of Valhall

3.1 Gas chromatographic (GC-FID) characterization

3.2 Asphaltenes and wax content of the fresh and weathered residues

3.3 Physical properties of the fresh and weathered residues

3.4 Viscosity of fresh oil and water-free residues with different shear rates

3.5 Emulsifying properties

3.5.1 Emulsification

3.5.2 Water uptake

3.5.3 Efficiency of emulsion breaker and stability of emulsions

3.5.4 Emulsion viscosities

3.6 Chemical dispersibility

3.6.1 Dosage testing

3.6.2 Systematic dispersant testing and dispersibility limits

4 Predictions with SINTEF Oil Weathering Model (OWM) 4.1 Description of SINTEF OWM

4.2 Predictions of Valhall oil weathering properties

5 Comparison of OWM predictions

5.1 Evaporative loss

5.2 Pour point

5.3 Water uptake

5.4 Viscosity