GAS

LPG

CTG, annually contributing 50,000 tons of LPG, plays a vital role in the supply chain of this flammable hydrocarbon mixture composed mainly of butane and propane. LPG stands as a significant feedstock for various industrial processes, particularly as a primary input for olefin units.

Comprising two key hydrocarbon gases, butane and propane, LPG serves as a versatile and essential resource across multiple industries. Its flammable nature and adaptable properties make it invaluable for diverse applications, from being a crucial component in petrochemical production, particularly in the creation of olefins, to serving as a fuel for various heating and cooking needs.

CTG’s supply of 50,000 tons of LPG annually is a testament to its robust capacity and role in meeting both domestic and international market demands. This consistent supply aids industries in ensuring the availability of this vital hydrocarbon mixture for their operations, enhancing productivity and supporting various industrial processes

The utilization of LPG as a feed for olefin units underscores its significance in the production of essential materials for the manufacturing sector. CTG’s contribution in providing a substantial quantity of LPG ensures a steady supply chain, benefiting both domestic and international markets, and enabling the seamless continuation of various industrial operations reliant on this versatile resource.

TYPE1

Typical TestUnitSpecificationTest Method
GCISO 7941
C1mol%Max 0.5ISO 7942
C2mol%Max 9ISO 7943
C5mol%Max 2.5ISO 7944
C6+mol%Max 0.4ISO 7945

TYPE2

PropertiesUnitTest MethodResult
Vapour Pressure, Gauge@37.8D eg.CK PaASTM D-1267 or ASTM D-2598420-830 Max
DensityASTM D-1657 or ASTM D-2598Report
Total Sulphur (After Stanched)PPMWASTM D-2784 or ASTM D-324650 Max
Corrosion, Copper Strip 1Hour at 37.8Deg. CASTM D-18381 Max
Free WaterVisual InspectionNone
Odorant (Ethyl Mercaptan) (If Stanched Only)L/1000MT*Smell Test26
Olefin (Required only from complex refinery sources)%MoleASTM D-21635 Max
C2 Hydrocarbons% WeightASTM D-2163I Report
C3 Propane% WeightASTM D-2163Total C3 Saturates 25 30
C4 I-Butane% WeightASTM D-2163Total C4 Saturates 7705
CS and Higher Hydrocarbons% MoleASTM D-21632 Max (Pentenes 0.5 Max)
Residue TestMl/ 100mlASTM D-21580.05 Max
Oil StraineASTM Oe2158Pass
Dienes contents as 1,3 Butadiene’s (Required only from complex refinery sources)% MoleASTM D-21630.5 Max
MON (Motor Octane number)ASTM D-259889 Min

LNG

Liquefied Natural Gas (LNG), a critical energy resource, undergoes a transformation process from its gaseous state into a liquid form. Annually, Creed Trading Group (CTG) contributes a substantial supply of 100,000 tons of LNG to meet the demands of both domestic and international markets.

The production of LNG involves a complex and precise conversion process. Natural gas is cooled to extremely low temperatures, typically around -162 degrees Celsius (-260 degrees Fahrenheit), converting it into a liquid state. This liquefaction process reduces the volume of natural gas by about 600 times, making it more efficient and cost-effective to transport over long distances.

CTG’s annual supply of 100,000 tons of LNG plays a pivotal role in meeting energy demands globally. LNG serves as a versatile energy source with diverse applications across various industries. It serves as a clean-burning fuel for power generation, heating, and industrial purposes, offering a more environmentally friendly alternative to traditional fossil fuels.

The supply of LNG by CTG serves as a cornerstone for both domestic and foreign markets, supporting energy-intensive industries and enhancing the energy security of regions reliant on this resource. Its widespread use in various sectors underscores its importance in contributing to a more sustainable and efficient energy landscape.

By providing a consistent and substantial supply of LNG, CTG plays a significant role in meeting the energy needs of diverse industries, contributing to economic growth, and promoting a more environmentally conscious approach to energy consumption and production.

1 Methane CH4% Mol91.1300
2Ethane:C2H6% Mol6.1100
3Propane:C3H8% Mol2.1600
4lso Butane :1- C4H10% Mol0.3100
5N·Butane :nC4H10% Mol0.2600
6lso Pentane:iC5H12% Mal0.0000
7N·Petane:nC5H12% Mol0.0000
8N-Hexane:nC6H14% Mal0.0000
9Nitrogen :N2% Mal0.0300
10Oxygen 02% Mol0.0000
11Carbon Dioxide :C02% Mol0.0000
12Hydrogen Sulphur.H2Smg/m3<0.2
13Total Sulphur: Smg/m3<0.2
14Hydrocarbon Ana:lys1s Method = ISO 6974
15H2S &Total Sulphur Analysis Method ASTM 06667& ISO 1973 Average Liquid Temp Prior to Discharge ·c -159.10 Average Density @ Observed Temp (Calculated) Kg/m3 451.79
16Calorific Value Minimum 36.4 MJ/m3 Maximum 40.9 MJ/m3