LNG & LPG

LNG (Liquefied Natural Gas) and LPG (Liquefied Petroleum Gas) are two types of gases which are go through a process of liquefaction for transportation and storage purposes. Although similar in their liquid state, they differ significantly in composition, usage, and production methods.

LNG (Liquefied Natural Gas)

LNG is primarily methane (CH4) gas that has been cooled to a temperature of approximately -162 degrees Celsius (-260 degrees Fahrenheit). At this temperature, methane condenses into a liquid form, which takes up about 1/600 th of the volume it occupies as a gas at standard atmospheric temperature and pressure. This significant reduction in volume makes LNG economical to transport over long distances where pipelines are not feasible, such as across oceans. LNG is used mainly for heating and as a fuel for electricity generation and is increasingly used in the transportation sector, especially for ships and heavy-duty vehicles.

LPG (Liquefied Petroleum Gas)

LPG is a mixture of propane (C3H8) and butane (C4H10), gases that are found naturally in crude oil and natural gas. LPG is produced during natural gas processing and oil refining. It is stored and transported in liquid form under moderate pressure, which makes it easier to store and handle compared to LNG. LPG is widely used as a fuel for heating, cooking, and in vehicles. It is also used in industrial applications and is a popular choice for portable cooking and heating equipment in areas not connected to a natural gas network.

Both LNG and LPG play crucial roles in the global energy supply, offering cleaner alternatives to traditional fossil fuels like coal and oil. They contribute significantly to reducing emissions and air pollution in various applications.

Fuelling the Future – Powering the LNG Carriers 1241
Dual-Fuel-Electric LNG Carrier Propulsion 1401
Overview of Alternative Propulsion Systems for the LNG Vessel 1826
The New Generation of Liquefied Natural Gas Carriers – Basic Design Philosophy 1632
Weather-related Economics of Natural Gas Transport for Two Propulsion Plant Configurations 1772
Technical Considerations in the Classing of Vessels Intended to Carry Compressed Natural Gas 1873
Compressed Natural Gas Carriers Applied to Remote Marginal Gas Field Developments 2409
Natural Gas Transportation in the Form of Hydrate Pellets (NGHP) 1827
Wave and Impact Loads in Design of Large and Conventional Liquefied Gas Carriers 1679
Det Norske Veritas Fatigue Analysis of Natural Gas Carriers 1772
Condition Assessment Program for Liquefied Gas Carriers (CAP LNG) 2480
Dynamic Strength Analysis for Membrane Type LNG Containment System Due to Sloshing Impact Load 2066
Coupling Between Liquefied Gas and Vessel’s Motion for Partially Filled Tanks Effect on Seakeeping 1389
Development of the FLNG and FONG for Gas Extraction 1931
Maximising LNG Efficiency Through the Use of Foul Release Coatings 1169
Manning and Operational Standards for the Liquefied Gas Carriers 1752
Planning the Design, Construction and Operation of New LNG Transportation Systems 2072
History and Future Predictions of the Liquefied Natural Gas Shipping 1795
Separation of the Gas Produced in Field from Unnecessary Components 2725
Gas Field Operation Problems and Methods to Deal With Them 1747
Complete Manual for Engineers about Dew Point Reservoirs 2614
Determination of Volumetric Flow Rates of Gas using Orifice Metering System and other Techniques 2047
Perform of Total System Analysis in NG Production Operations 1355
Usage of Natural Gas Compressors in the Gas Production Operations 2061
Performance of the Network of Pipes in Gas Industry 1960
Manual for Engineers to Calculate Amount of Gas in Reservoirs 2141
Best and Most Widely Methods to Perform Necessary Calculations with a Gas 2435
Everything about Natural Gas in Modern Industry 1939
Summary from Researches done with Vessel Simulator Tool (VeSim) 1281
Real Example of Vessel Manoeuvering done with Vessel Simulator (VeSim) 1670
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