Infrastructure Specific Information
SVT does not operate a capacity booking system. Decisions leading to increase or decrease in capacity are anticipated on the basis of forecast throughput, may incur additional cost and (subject to that) are reversible.
|
(a) |
Entry specification (pipeline) |
BS&W True vapour Pressure H |
max 5% vol max 220 psia at 100> |
|
(b) |
Exit specification | - | - |
Stabilized Crude Oil
|
Level |
Test Method | |
| Reid Vapour Pressure, psi | target 10.0 | IP 69 (mod) |
| BS & W vol% | max 0.5 | IP386 (mod) |
| Acidity mgKOH/g | target 0.05 max | - |
| Density at 15oC | to be reported | SVTA 101 |
| Salt Content 1bs/10000bbl | to be reported | IP265 (mod) |
|
TEST |
PROPANE Mole % |
BUTANE Mole % |
METHOD NUMBER |
| Ethane (C2) |
2.0 max |
- |
ASTM D2163 (mod) |
| Propane (C3) |
95.0 min |
3.0 max |
ASTM D2163 (mod) |
| Butanes (iC4 & nC4) |
|
95.0 max |
ASTM D2163 (mod) |
| Butanes & Heavier (C4+) |
2.5 max |
ASTM D2163 (mod) | |
| Pentanes & Heavier (C5+) |
0.5 max |
2.0 max |
ASTM D2163 (mod) |
| Vapour Pressure |
14.34 max |
4.83 max |
ASTM D1838 (mod) |
| Copper Strip |
No. 1 |
No. 1 |
ASTM D4084 (mod) |
| Total Sulphur PPM by Wt |
15.0 max |
15.0 max |
ASTM D4468 (mod) |
| Hydrogen Sulphide (H2S) PPM by vol. |
0.5 max |
0.5 max |
ASTM D4084 (mod) |
| Residue Number (R) |
10.0 max |
10.0 max |
ASTM D2158 |
| Oil Stain Number (O) |
Pass (34.0 max) |
Pass (34.0 max) |
ASTM D2158 |
| Oily Residue PPM by Wt |
20.0 max |
30.0 max |
SVTA 109 |
| Moisture Content |
Pass |
ASTM D2713 (mod) | |
| Free Water Content |
None |
SVTA 108 | |
| Methanol |
to be reported if present |
to be reported if present |
|
| Olefins |
to be reported if present |
to be reported if present |
|
(c) |
Details of primary separation processing facilities | Three stabilisation trains of respective capacity (bbls/day) 350,000, 410,000 and 410,000 (retired) |
|
(d) |
Details of Gas treatment facilities | Fractionation to commercial propane & butane and fuel gas (which is burnt in the onsite poer station) |
|
(e) |
Oil export capacity | 620,000 bbls/day (capacity for export of Brent Blend - can be increased by recommissioning a jetty). |
|
(f) |
Gas compression capacity |
N/A |
|
(g) |
Gas export capcity |
N/A |
|
(h) |
Gas lift capacity |
N/A |
|
(i) |
Produced water handling capacity |
1200 M3/hr |
|
(j) |
Gas Dehydration capacity |
not a bottleneck |
|
(k) |
H2S removal capacity |
N/A (H2S is burnt with fuel gas in power station) |
|
(l) |
Water injection capacity |
N/A |
Modified Sept 07
