PURIGAS™ is the package solution for Fuel Gas Supply System(FGSS).
It means PURe and Intelligent GAS storage and supply system.
Although FGSS is the most effective solution for IMO’s SOx,
NOx and GHG emissions restriction, CAPEX and installation space are heavy obstacles
to adapt FGSS solution.
To solve this obstacles, PURIGAS™ has been developed from the accumulated
technology for LNG related equipment and engineering capability of S&SYS and
Samsung Heavy Industries(SHI). As accumulated know-how, PURIGAS ™
will provide the most economical and the most reliable package system to customer.
Reinforcement of regulations for the conservation of the marine atmosphere by IMO, under the UN
1997 MARPOL Protocol : SECAs ( ECAs)
Baltic Sea | Adopted 1997/ into force 2005 |
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North Sea | Adopted 2005/ into force 2006 |
North American coasts | Adopted 2010 / Into force 2012 |
US Caribbean Area | Adopted 2011 /Into force 2011 |
Outside an ECA | Inside an ECA |
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4.5%prior to 1.Jan. 2012 | 1.5%prior to 1.July. 2010 |
3.5%on & after 1.Jan. 2012 | 1.0%on & after 1.Jul. 2010 |
0.5%on & after 1.Jan. 2020 | 0.1%on & after 1.Jan. 2015 |
Existing ECA zones and possible future ECAs
NOx Emission Control Areas (NECA)
Initial IMO strategy on Reduction of GHG emissions from ships
Level of ambition | Timeline |
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Carbon intensity of ships to decline
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Short-term measures: 2018–2023
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Carbon intensity of shipping to decline
GHG emission from shipping to decline
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Mid-term measures: 2023–2030
Long-term measures: > 2050
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By using Natural Gas Instead of MDO, CO2 is reduced about 23% and SOx, NOx and PM are reduced more than 92%.
* Source: Marintek Report from Rolls-Royce DF Engine
NOx
SOx
CO2
Particulates
- Full package for Engineering FGSS and FGSS equipment
- Turn key delivery of FGSS including S&SYS’s own control system (AMS, ICMS, IAS)
- Reliable Engineering based on Reference and site experience in various of FGSS project.
- Post docking operation with N2 , Bunkering operation, Pre-docking operation, Gas trial.
HAZID, HAZOP / FMEA / Cause & Effect / FAT procedure / SAT procedure/ Gas trial procedure FDS(Functional Design Specification) /
Tank preservation procedure/ Operation & Maintenance manual/ Double pipe drawing, etc.
- Strong & Reliable Hardware
- Providing Diagnostic Mimic of Automation System
- Providing Logic Programming Tool for Function & Sequential Flow, Real Time Monitoring
- Easy Maintenance with Search function, Change alarm set value
LNG Storage tank
Bunkering Station
Control & Monitoring system
H.P. Pump Skid
Vaporizer Skid
Engine
Vapor Line: 4 ~ 6” Pipe
IMO Classification of LNG Carriers( IGC Code) | |||
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Independent Tanks (separated from hull structure) | Integrated Tanks (part of hull structure) | ||
Type A | Type B | Type C | Membrane Tank |
* Simple Design * Pο ≤ 0.7 bar * Full secondary barrier |
* Flat Design * Pο ≤ 0.7 bar * Partial secondary barrier |
* Simple Design * Pο ≥ 2 bar * No secondary barrier |
* Simple Design * Pο ≤ 0.7 bar * Full secondary barrier |
Double shell with Vacuum
ISO container (20ft, 40ft)
Single shell with PU
Bi-lobe Tank
Tri-lobe Tank
High Pressure Vaporizer | Low Pressure Vaporizer | ||
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