Heather oil field

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Heather oil field
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Location of Heather oil field
CountryUnited Kingdom
Regionnorthern North Sea
Location/block2/5
Offshore/onshoreOffshore
Coordinates 60°57′13″N00°56′23″E / 60.95361°N 0.93972°E / 60.95361; 0.93972
OperatorsUnionoil, Unocal, DNO, Lundin, Enquest
OwnerSee text
Field history
Discovery1973
Start of production1978
Peak of production1982
Production
Recoverable oil (million tonnes)14.1
Producing formationsJurassic sandstone

The Heather oil field is a significant crude oil producing field in the UK sector of the northern North Sea, 458 km north-north-east of Aberdeen. Production of oil started in 1978 and ceased in 2019. The Heather Alpha installation is currently (2021) undergoing decommissioning.

Contents

The field

The Heather oil field is located in Block 2/5 of the UK North Sea. It is named after the plant that grows extensively on Scottish moors. [1] The Heather field was discovered in December 1973 and comprises a middle Jurassic sandstone at a depth of 9,800 to 11,750 feet (2,9873 to 3,581 m). [2] The reservoir and its fluids had the following characteristics: [2]

Heather reservoir fluids
ParameterValue
Porosity1.7-19.3 %
Water saturation21.4-56.3 %
API gravity 35°API
Gas Oil Ratio 650 standard cubic feet/barrel
Sulfur content0.7 %
Recoverable reserves90-120 million barrels, 14.1 million tonnes

Owners and operators

The initial owners of the field were a consortium comprising Unionoil Company of Great Britain (31.25%), Texaco North Sea UK Ltd (31.25%), Tenneco Great Britain Ltd (31.25%), and DNO (UK) Ltd. (6.25%). The field was operated by Unionoil Company of Great Britain. [2] In 1994 the owners were BG Great Britain Limited (31.25%), Texaco Exploration Ltd (31.25%), Unocal Britain Ltd (31.25%), and DNO (Heather Oilfield) Ltd (6.25%). The operator was Unocal. [1] In 1999 DNO became the operator, then Lundin from 2008, and finally Enquest. [3]

Development

The field was developed by a single integrated drilling, production and accommodation platform: Heather Alpha (Heather A). The principal design data of the Heather A platform is given in the following table. [2]

Heather A platform design
InstallationHeather A
Coordinates60°57’13”N 00°56’23”E
Water depth, metres143
Fabrication substructureMcDermott, Ardersier
Topsides designMcDermott
Topside weight, tonnes22,000
FunctionDrilling, production, accommodation
Accommodation (crew)180
TypeSteel jacket
Legs8
Piles24
Well slots40
Throughput oil, barrels per day (bpd)60,000
Water injection, bpd100,000
Platform installedJune 1977
Production startOctober 1978
Oil production toNinian Central
Gas production toUsed onboard for gas lift and fuel gas

Processing

The wellhead fluids flowed via the production manifold to the 3-phase Production Separator which operated at 65 psi (448 kPa). [4] From the Separator oil was routed to another 3-phase Production Separator operating at a lower pressure of 35 psi (241 kPa). Oil then flowed to the crude booster pumps, through oil metering then by 32 km 16-inch pipeline to Ninian Central and thence to Sullom Voe. Produced water from the separators was treated by hydrocylones and a compact flotation unit (CFU) to remove oil prior to overboard discharge. Vapour from the Production Separators was compressed, dried by TEG (triethylene glycol) and further compressed to 325 psi (2,241 kPa) for use as fuel gas and up to 1,480 psi (10,204 kPa) for gas lift. [4] In 1985 a connection was made to the Western leg gas pipeline, a 6-inch pipeline imported gas into Heather to augment gas supplies. [1] Import gas flowed to an Import Gas Knockout Drum, through metering and to an Import Gas Heater. [4]

The oil production profile for Heather A (in 1000s barrels per year) in the early operating period is shown in the graph: [2]

The fluid handling capability of the Heather facilities in its latter years was as follows: [5]

Heather A processing capability
FacilityCapacity
Crude oil30,000 bbls/day
Gas compression54 MMSCFD (million standard cubic feet per day)
Dehydration54 MMSCFD
Gas lift54 MMSCFD
Produced water50,000 bbl/day
Water injection70,000 bbl/day

Broom oil field

Fluids from the Broom oil field in Block 2/4a were routed into Heather for treatment and export to Ninian Central. [6] The Broom field is located 7 km from Heather. The field development comprised four gas-lifted production wells and two water injection wells. Lift gas and injection water were supplied from Heather A. Production from Broom started in 2004. [6]

Decommissioning

Following a fire on Heather A in October 2019 and the shutdown of the platform [7] Enquest decided to decommission the platform. [8] This was principally due to the low oil price environment during the coronavirus pandemic. [8] The topsides will be removed for onshore recycling and disposal. [9] The removal of the jacket will be the subject off a further plan. [9]

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References

  1. 1 2 3 Department of Trade and Industry (1994). The Energy Report. London: HMSO. pp. 56 and map 6. ISBN   0115153802.
  2. 1 2 3 4 5 Oilfield Publications Limited (1985). The North Sea Platform Guide. Ledbury: Oilfield Publications Limited. pp. 284–89.
  3. ↑ A Barrel Full (2015). "Heather oil and gas field". abarrelfull. Retrieved 17 October 2021.
  4. 1 2 3 Heather A Process Flow Diagrams, Lundin, undated
  5. ↑ Enquest (March 2019). "Heather Platform High Level Capacity Information" (PDF). enquest.com. Retrieved 17 October 2021.
  6. 1 2 "Ithaca Energy Non Operated Assets The Broom Field". www.ithacaenergy.com. Retrieved 17 October 2021.
  7. ↑ "Enquests Thistle and Heather platforms still shut production to resume in 2020". Offshore Energy. October 2019. Retrieved 17 October 2021.
  8. 1 2 "Enquest files decom plans for Heather topsides". offshore-energy.biz. 12 April 2021. Retrieved 17 October 2021.
  9. 1 2 "Heather Alpha Platform Topsides decommissioning Programme" (PDF). www.enquest.com. Retrieved 17 October 2021.
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