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NET ZERO BASIN Pilot field development 1

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Page 1: Pilot field development

NET ZERO BASINPilot field development

1

Page 2: Pilot field development

● Fully appraised, seven reservoir penetrations, three tested wells, core and fluid samples held by Orcadian, two high quality 3D seismic surveys

● Very high quality sandstone turbidite reservoir, 34% porosity, 2 to 10 darcies of permeability

● Significant oil in place: 263 MMbbls; audited 2P reserve of 79 MMbbls, based on a low salinity polymer flood of the reservoir

● Variable quality oil from 12º to 17º API, 160 cP to 1,200 cP

● Shallow water (c. 80m), 140 kms due East from Aberdeen, c. 40 kms from Gannet et al

2

Pilot field summaryWest East21/27a-6

500m

50 m

Sec

TWT

DataprovidedcourtesyofWesternGeco

5 Reserves Summary

Pilot and Pilot South

Volumetric calculations have been undertaken for the Pilot discovery. A most likely STOIIP for Pilot and Pilot South combined of 263 MMstb was estimated, uncertainty assessments suggested a range of +/-8%. This is a relatively narrow range, and reflects the fact the discovery is well appraised and seismic imaging is of high quality. A hydrocarbon pore thickness map was created as part of the volumetric calculations, see Fig. 5.1.

Fig. 5.1 Hydrocarbon Pore Thickness Map

HCPV

21/27a-6

Pilot Static Model Peer Review 78

Page 3: Pilot field development

Pilot field development plan

3

FPSO WHPJack-upFPP

Page 4: Pilot field development

● Many opportunities to reduce emissions identified

● Integration of aggressive process heat management with high efficiency back-up power generation and electrification has the potential to drive emissions down by over 80%

● Local wind farm power, with highly efficient back-up gas engines, reduces emissions as low as connection to a future grid with half of today’s CO2 intensity

4

A project delivering on the Government’s Net Zero agenda

Kg

CO

2/bb

l

0

5

10

15

20

25

30

35

Typical viscous oil

North Sea 2018

average

Pilot waterflood

Polymer flood

Process & power

generation optimised

Grid from

year 2

Single wind

turbine

Two wind

turbines

21

30

1.42.60.45.9

14.4

24.7

Scope 1 Scope 2 Benchmarks

Estimates from recently submitted CSR Addendum prepared with Crondall Energy. These numbers are CO2e

Shorter field life and lower fluid

handling

FPP wind and wave power unit

Pilot field development

Heat pumps and reciprocating gas

engines

2.3

Page 5: Pilot field development

● Fluid handling requirements massively reduced by using polymer

● Field life significantly shortened with polymer

● Pumping wells and injecting fluid are the key drivers of CO2 emissions

● Polymer boosts recovery so there are more barrels produced in less time and for much less energy

● Polymer use significantly enhances project economics while minimising environmental impacts

5

Why polymer reduces CO2

0

50000

100000

150000

200000

250000

Water Flood

0

50000

100000

150000

200000

250000

Polymer Flood

0

20

40

60

80

100

0 200 400 600 800 1000 1200

Oil R

ecov

ered

, MM

bbls

Water Injected, MMbbls

Polymer Flood

Water Flood

Polymer Flood

Water Flood

Wate

rflo

od

Modeling

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ype

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ave

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idth

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ud

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ich

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ell

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ilit

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etal

.(2

01

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edo

nm

ild

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ater

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mic

rom

od

els.

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esa

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isti

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pt

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ith

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ther

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bli

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the

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app

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met

ho

do

log

yto

that

of

Ria

zet

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20

07

),b

ut

bec

ause

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the

abse

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ve

per

-m

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ents

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eu

sea

3D

qu

asis

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aila

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asis

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he

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ph

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max

imal

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ilin

and

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20

06

;D

on

gan

dB

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00

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edto

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ruct

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etw

ork

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ival

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inte

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smis

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ere

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stru

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ren

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ork

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1,2

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15

1,1

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ore

/th

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rop

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or

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tic

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ula

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use

the

mo

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of

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vat

ne

and

Blu

nt

(20

04

),w

hic

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also

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dto

ver

ify

the

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al-

ity

of

the

gen

erat

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ork

.T

od

oth

is,

we

com

pu

teth

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lary

pre

ssu

rean

dth

ere

lati

ve

per

mea

bil

ity

curv

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mp

are

wit

hex

per

imen

tal

mea

sure

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ts.

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lly

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ew

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ldli

ke

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sem

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rem

ents

mad

eo

nth

esa

mp

les

of

Ex

per

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os.

2,

6,

and

7,

bu

tsu

chd

ata

are

no

tav

aila

ble

,an

dw

eth

eref

ore

use

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tsfr

om

the

lite

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re(O

ren

etal

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99

8).

Av

ery

go

od

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emen

tis

fou

nd

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se to

end

WF

End

WF

End

WF

PV

I = 0

.15

PV

I = 0

.15

0.9

0.8

0.7

0.6

0.5

0.4

0.3

0.8

0.7

0.6

0.5

0.4

0.3

0.8

0.7

0.6

0.5

0.4

0.3

0.2

PV

I = 0

.49

PV

I = 0

.19

PV

I = 0

.58

PV

I = 0

.5

(a)

(b)

(c)

Fig

.4—

Oil

-satu

rati

on

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sat

the

en

do

fw

ate

rflo

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ing

(WF

)an

dd

uri

ng

po

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ing

for

(a)

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men

tN

o.2,(b

)E

xp

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,an

d(c

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xp

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Met

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he

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sect

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ify

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eth

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ult

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nsi

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isco

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tern

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exp

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aco

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nu

um

Dar

cy-t

yp

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on

isn

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rop

riat

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ng

ers

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ow

the

scal

eo

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few

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resi

zes,

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ism

ore

lik

ely

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ev

alid

wh

enfi

ng

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are

gen

erat

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am

acro

sco

pic

scal

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ever

thel

ess,

ver

yfe

wv

alid

atio

nst

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ies

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avai

lab

lein

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re.

Fro

mth

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imag

esat

earl

yti

mes

,th

ev

isco

us

fin

ger

sh

ave

afi

ne

den

dri

tic

asp

ect

and

aty

pic

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idth

of

afe

wm

illi

met

ers.

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eref

ore

,w

ed

on

ot

exp

ect

aD

arcy

-ty

pe

mo

del

toca

ptu

reth

eex

per

i-m

enta

lfi

ng

erin

gp

atte

rns

accu

rate

ly,

bu

tw

ew

ou

ldli

ke

tov

erif

yh

ow

clo

sely

itca

nre

pro

du

ceth

ose

pat

tern

s.In

this

con

tex

t,th

em

ost

rele

van

tst

ud

yis

that

of

Ria

zet

al.

(20

07

),w

her

ese

ver

alex

per

imen

tsw

ere

per

form

edo

na

stro

ng

lyw

ater

-w

etB

erea

core

sam

ple

,fi

rst

tom

easu

rest

ead

y-s

tate

rela

tiv

ep

erm

eab

ilit

yfu

nct

ion

san

dth

ento

mea

sure

satu

rati

on

pro

file

san

do

ilre

-co

ver

yd

uri

ng

un

stea

dy

-sta

ted

isp

lace

men

ts.

Dif

fere

nt

oil

vis

cosi

ties

up

to3

03

cpan

din

ject

ion

rate

su

pto

3cm

3/m

inw

ere

use

dto

iden

-ti

fyth

eo

nse

to

fin

stab

ilit

y,

wh

ich

was

corr

ectl

yp

red

icte

db

yth

eco

nv

enti

on

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arcy

-ty

pe

mo

del

dep

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ent

on

stea

dy

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tere

lati

ve

per

mea

bil

itie

s.H

ow

ever

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eav

erag

esa

tura

tio

np

rofi

les

of

the

un

stab

leex

per

imen

tsco

uld

no

tb

ere

pro

du

ced

exp

lici

tly

by

hig

h-r

eso

lu-

tio

nD

arcy

-ty

pe

sim

ula

tio

ns

mo

del

ing

vis

cou

sfi

ng

ers.

Th

us,

itw

asco

ncl

ud

edth

atth

eco

nti

nu

um

Dar

cy-t

yp

em

od

eld

oes

no

tw

ell

pre

-d

ict

the

flo

wre

gim

ew

ith

full

yd

evel

op

edin

stab

ilit

ies.

InS

har

ma

etal

.(2

01

2),

ano

ther

stu

dy

was

per

form

edo

nm

ild

lyw

ater

-wet

2D

mic

rom

od

els.

Th

eav

erag

esa

tura

tio

np

rofi

les

ob

tain

edfr

om

the

wat

erfl

oo

din

go

fv

isco

us

oil

sw

ere

bet

ter

rep

rod

uce

db

ya

scal

ing

law

dep

end

ent

on

stat

isti

cal

theo

ryra

ther

than

by

aB

uck

ley

-Lev

eret

tp

rofi

le,

bu

tn

oat

tem

pt

was

mad

eto

sim

ula

teth

ed

isp

lace

men

tw

ith

a2

DD

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Production profiles for polymer flood and water flood from Orcadian Energy reservoir simulations; plot of recoverable oil vs. water injected based upon the same simulations.

Page 6: Pilot field development

0

5,000

10,000

15,000

20,000

25,000

Year 1 Year 2 Year 3 Year 4 Year 5 Year 6 Year 7 Year 8 Year 9 Year 10 Year 11

Pow

er d

eman

d kW

Power Demand kW

FPSO Heat pumps Jack-up

WHP-A (South) WHP-B (North) Transfer Pump

0

1

2

3

4

5

6

7

Year 1 Year 2 Year 3 Year 4 Year 5 Year 6 Year 7 Year 8 Year 9 Year 10Year 11

Gas

Dem

and

mm

scf/d

ay

Gas Consumption

Power Generation Average Offloads

0

5,000

10,000

15,000

20,000

25,000

Year 1 Year 2 Year 3 Year 4 Year 5 Year 6 Year 7 Year 8 Year 9 Year 10 Year 11

Pow

er k

W

Energy Sources

FPP Electrical Supplemental heat

Gas Engine power Gas Supplemntal Heat

-3

-2

-1

0

1

2

3

4

5

6

7

Year 1 Year 2 Year 3 Year 4 Year 5 Year 6 Year 7 Year 8 Year 9 Year 10Year 11

Gas

flow

s (m

msc

f/day

) an

d G

as in

Pilo

t Ea

st (

bcf)

Pilot East gas balance

Import gas To Gas storage

6

Emissions, by cause and scope CSR initial polymer scenario

0

2,000

4,000

6,000

8,000

10,000

12,000

14,000

16,000

18,000

20,000

Year 1 Year 2 Year 3 Year 4 Year 5 Year 6 Year 7 Year 8 Year 9Po

wer

dem

and

kW

Power Demand kW

FPSO JACK UP WHP-A (South) WHP-B (North) Fluids Transfer Pump (WHP)

0

2,000

4,000

6,000

8,000

10,000

12,000

14,000

16,000

18,000

20,000

Year 1 Year 2 Year 3 Year 4 Year 5 Year 6 Year 7 Year 8 Year 9

Pow

er d

eman

d kW

Power Demand kW

FPSO JACK UP WHP-A (South) WHP-B (North) Fluids Transfer Pump (WHP)

● Base case from September 2020 CSR submission, focus had been on quantifying rather than driving down emissions (included some worst case assumptions e.g. downhole pump power demands)

● Adoption of polymer flood had reduced both fluid handling and field life

0

2,000

4,000

6,000

8,000

10,000

12,000

14,000

16,000

18,000

20,000

Year 1 Year 2 Year 3 Year 4 Year 5 Year 6 Year 7 Year 8 Year 9

Powe

r dem

and k

W

Power Demand kW

FPSO JACK UP WHP-A (South) WHP-B (North) Fluids Transfer Pump (WHP)

Page 7: Pilot field development

● Industrial heat pumps

● Energy recovery systems

7

Process optimisation

Page 8: Pilot field development

● Wartsila, dual fuel gas reciprocating engines

● “Smart heat recovery” system

8

Power Generation

Page 9: Pilot field development

0

5,000

10,000

15,000

20,000

25,000

Year 1 Year 2 Year 3 Year 4 Year 5 Year 6 Year 7 Year 8 Year 9 Year 10 Year 11

Pow

er d

eman

d kW

Power Demand kW

FPSO Heat pumps Jack-up

WHP-A (South) WHP-B (North) Transfer Pump

0

1

2

3

4

5

6

7

Year 1 Year 2 Year 3 Year 4 Year 5 Year 6 Year 7 Year 8 Year 9 Year 10Year 11

Gas

Dem

and

mm

scf/d

ay

Gas Consumption

Power Generation Average Offloads

0

5,000

10,000

15,000

20,000

25,000

Year 1 Year 2 Year 3 Year 4 Year 5 Year 6 Year 7 Year 8 Year 9 Year 10 Year 11

Pow

er k

W

Energy Sources

FPP Electrical Supplemental heat

Gas Engine power Gas Supplemntal Heat

-3

-2

-1

0

1

2

3

4

5

6

7

Year 1 Year 2 Year 3 Year 4 Year 5 Year 6 Year 7 Year 8 Year 9 Year 10Year 11

Gas

flow

s (m

msc

f/day

) an

d G

as in

Pilo

t Ea

st (

bcf)

Pilot East gas balance

Import gas To Gas storage

9

Emissions, by cause and scope Process optimisations and recips

0

2,000

4,000

6,000

8,000

10,000

12,000

14,000

16,000

18,000

20,000

Year 1 Year 2 Year 3 Year 4 Year 5 Year 6 Year 7 Year 8 Year 9

Pow

er d

eman

d kW

Power Demand kW

FPSO JACK UP WHP-A (South) WHP-B (North) Fluids Transfer Pump (WHP)

● Crondall reshaped process and power generation with the intention of driving down emissions

● The combination of heat pumps and high efficiency generation is the key to reducing emissions

0

2,000

4,000

6,000

8,000

10,000

12,000

14,000

16,000

18,000

20,000

Year 1 Year 2 Year 3 Year 4 Year 5 Year 6 Year 7 Year 8 Year 9Po

wer

dem

and

kW

Power Demand kW

FPSO JACK UP WHP-A (South) WHP-B (North) Fluids Transfer Pump (WHP)

Page 10: Pilot field development

Intro

SYSTEM OVERVIEW

10

• Platform – North Sea design for 15m Hs sites – Panel based semi submersible – Makes use of harbour effect for transfer – Hydrogen energy storage can be accommodated

• Turret Mooring System – Vanes into wave direction • WTG yaws independently

– Multi point catenary mooring system – Disconnectable if required

• Wind Turbine Generator (WTG) – Turbine agnostic – 12 to 15MW (to be assessed)

• Wave Energy Convertor – 4 off, from 500kW to 1MW each (to suit site) – Wave energy converted to motion by absorber – Mechanical motion converted to electricity via oil

hydraulic Power Take Off (PTO) system

Page 11: Pilot field development

11

Emissions, by cause and scope Local wind and wave power

0

5,000

10,000

15,000

20,000

25,000

Year 1 Year 2 Year 3 Year 4 Year 5 Year 6 Year 7 Year 8 Year 9 Year 10 Year 11

Pow

er d

eman

d kW

Power Demand kW

FPSO Heat pumps Jack-up

WHP-A (South) WHP-B (North) Transfer Pump

0

1

2

3

4

5

6

7

Year 1 Year 2 Year 3 Year 4 Year 5 Year 6 Year 7 Year 8 Year 9 Year 10Year 11

Gas

Dem

and

mm

scf/d

ay

Gas Consumption

Power Generation Average Offloads

0

5,000

10,000

15,000

20,000

25,000

Year 1 Year 2 Year 3 Year 4 Year 5 Year 6 Year 7 Year 8 Year 9 Year 10 Year 11

Pow

er k

W

Energy Sources

FPP Electrical Supplemental heat

Gas Engine power Gas Supplemntal Heat

-3

-2

-1

0

1

2

3

4

5

6

7

Year 1 Year 2 Year 3 Year 4 Year 5 Year 6 Year 7 Year 8 Year 9 Year 10Year 11

Gas

flow

s (m

msc

f/day

) an

d G

as in

Pilo

t Ea

st (

bcf)

Pilot East gas balance

Import gas To Gas storage

0

2,000

4,000

6,000

8,000

10,000

12,000

14,000

16,000

18,000

20,000

Year 1 Year 2 Year 3 Year 4 Year 5 Year 6 Year 7 Year 8 Year 9Po

wer

dem

and

kW

Power Demand kW

FPSO JACK UP WHP-A (South) WHP-B (North) Fluids Transfer Pump (WHP)

0

2,000

4,000

6,000

8,000

10,000

12,000

14,000

16,000

18,000

20,000

Year 1 Year 2 Year 3 Year 4 Year 5 Year 6 Year 7 Year 8 Year 9

Pow

er d

eman

d kW

Power Demand kW

FPSO JACK UP WHP-A (South) WHP-B (North) Fluids Transfer Pump (WHP)

● Local renewable power eliminates the need for a gas import pipeline and halves emissions again

● Unit will be a 12MW wind turbine with a 2MW wave power generator from FPP

Page 12: Pilot field development

● To be comparable with this Stanford University dataset, to our Scope 1 & 2 emissions we have added:

● Scope 3 emissions from offshore logistics, oil transportation to the refinery, and polymer production

● Estimates of emissions during the exploration and development phases (done using the Stanford tool)

● Pilot field comparable emissions are 1.4 gCO2eq/MJ with a single wind turbine

12

Comparison with global oil production emissions Viscous oil doesn’t have to mean high emissions

Masnadi et al (2018). Global carbon intensity of crude oil production. Science. 361. 851-853. 10.1126/science.aar6859.

Pilot emissions will lie in the lowest 5% of

global oil production

Page 13: Pilot field development

Auditor: PKF Littlejohn Broker: WH Ireland Banker: Barclays

15 Westferry Circus London E14 4HD

24 Martin Lane, London EC4R 0DR

Level 25, 1 Churchill Place, London, E14 5HP

Lawyer: Hill Dickinson Lawyer: TandonHildebrand Registrar: Neville

The Broadgate Tower, 20 Primrose StreetLondon EC2A 2EW

Labs Atrium, Chalk Farm Rd,London, NW1 8AH

Neville House, Steelpark Road, Halesowen, B62 8HD

Public Relations: Tavistock Competent Person: Sproule Registered Office

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6th Floor 60 Gracechurch Street, London, United Kingdom, EC3V 0HR

Head Office

6th Floor 60 Gracechurch Street, London, United Kingdom, EC3V 0HR

ORCADIAN ENERGY PLC13

Contact Detailsemail: [email protected]

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website: https://orcadian.energy