Search engine for discovering works of Art, research articles, and books related to Art and Culture
ShareThis
Javascript must be enabled to continue!

Methodology to Define Design Motion Criteria for Performance of Floating LNG Process Facilities

View through CrossRef
Abstract This paper proposes a generalized methodology to determine motion criteria for required performance of process facilities using the Abadi Floating LNG (Abadi FLNG) as a sample. The Abadi FLNG is planned to be installed in the Indonesian territory of the Arafura Sea by INPEX Masela, Ltd. Although existing FPSOs all have its own motion criteria fed into topside equipment design, it is known that there is no codified nor comprehensive approach as to how those motion criteria can be specified. Those circumstances could lead to misunderstanding of information among owner, contractors and vendors, and potentially unnecessary cost increase. One of the conventional methods is that the design motion criteria are given as single maximum motion amplitude in the extreme condition for operation. Usually 1 year or 10 year cyclonic condition is adopted as the extreme condition for operation where motion is calculated under assumed wave heading angle with short term prediction manner. In this approach, the wave heading has to be conservatively assumed with some fixed angle, as there is no concurrent environmental data, such as wind, wave, and current, which should be utilized. In addition, the common method to present associated period is not established. For the application to FLNG case, there are some motion sensitive process facilities, such as cryogenic heat exchangers and acid gas absorbers, whose performances degrade with given motion criterion, and the degree of degradation varies with concurrent motion period. To establish the comprehensive motion criteria, FLNG wave heading analysis followed by motion analysis were performed for 10 years time-series concurrent wind, wave, swell and current data including extreme and non-extreme conditions. Calculated motions were incorporated into scatter diagram, which is a table of occurrence probability for motion amplitude and period to develop motion envelope of amplitude and period. This envelope was adopted as design motion criteria of motion sensitive process facilities. This envelope approach to define performace of process facilities due to motion criteria is recommended to other FPSO and FLNG as a generalized approach which has great benefit for clear understanding among owner, contractors and vendors while minimizing unnecessary margins which could have tremendous cost impact particularly for those with motion sensitive floaters. Introduction There are more than 100 FPSOs in operation in the world today. Those FPSOs apply their own design motion criteria to their facilities, however there is no standard method to define those motion criteria. There are two types of design motion criteria. One is design motion criteria for extreme condition, which is applied to all structural design on FPSO. Another one is design motion criteria for operation condition. Under such condition, all topside process facilities are designed to satisfy its full performance. As process facilities performance can be affected by relatively small motion amplitude, both dynamic motion and static inclination are included in design motion criteria for operation condition. In this paper, only dynamic motion of design motion criteria for operation condition are discussed. As for static inclination, equipment fabrication tolerance, equipment installation tolerance, module frame fabrication tolerance, module frame deflection, hull main deck construction tolerance, hull main deck deflection and ballast water control margin are considered.
Title: Methodology to Define Design Motion Criteria for Performance of Floating LNG Process Facilities
Description:
Abstract This paper proposes a generalized methodology to determine motion criteria for required performance of process facilities using the Abadi Floating LNG (Abadi FLNG) as a sample.
The Abadi FLNG is planned to be installed in the Indonesian territory of the Arafura Sea by INPEX Masela, Ltd.
Although existing FPSOs all have its own motion criteria fed into topside equipment design, it is known that there is no codified nor comprehensive approach as to how those motion criteria can be specified.
Those circumstances could lead to misunderstanding of information among owner, contractors and vendors, and potentially unnecessary cost increase.
One of the conventional methods is that the design motion criteria are given as single maximum motion amplitude in the extreme condition for operation.
Usually 1 year or 10 year cyclonic condition is adopted as the extreme condition for operation where motion is calculated under assumed wave heading angle with short term prediction manner.
In this approach, the wave heading has to be conservatively assumed with some fixed angle, as there is no concurrent environmental data, such as wind, wave, and current, which should be utilized.
In addition, the common method to present associated period is not established.
For the application to FLNG case, there are some motion sensitive process facilities, such as cryogenic heat exchangers and acid gas absorbers, whose performances degrade with given motion criterion, and the degree of degradation varies with concurrent motion period.
To establish the comprehensive motion criteria, FLNG wave heading analysis followed by motion analysis were performed for 10 years time-series concurrent wind, wave, swell and current data including extreme and non-extreme conditions.
Calculated motions were incorporated into scatter diagram, which is a table of occurrence probability for motion amplitude and period to develop motion envelope of amplitude and period.
This envelope was adopted as design motion criteria of motion sensitive process facilities.
This envelope approach to define performace of process facilities due to motion criteria is recommended to other FPSO and FLNG as a generalized approach which has great benefit for clear understanding among owner, contractors and vendors while minimizing unnecessary margins which could have tremendous cost impact particularly for those with motion sensitive floaters.
Introduction There are more than 100 FPSOs in operation in the world today.
Those FPSOs apply their own design motion criteria to their facilities, however there is no standard method to define those motion criteria.
There are two types of design motion criteria.
One is design motion criteria for extreme condition, which is applied to all structural design on FPSO.
Another one is design motion criteria for operation condition.
Under such condition, all topside process facilities are designed to satisfy its full performance.
As process facilities performance can be affected by relatively small motion amplitude, both dynamic motion and static inclination are included in design motion criteria for operation condition.
In this paper, only dynamic motion of design motion criteria for operation condition are discussed.
As for static inclination, equipment fabrication tolerance, equipment installation tolerance, module frame fabrication tolerance, module frame deflection, hull main deck construction tolerance, hull main deck deflection and ballast water control margin are considered.

Related Results

LNG Regasification Vessel - The First Offshore LNG Facility
LNG Regasification Vessel - The First Offshore LNG Facility
Abstract Active studies have been made on the offshore LNG receiving terminal by many people around world. Especially in USA, many actual LNG receiving terminal p...
Reimagine LNG – An Overview of the LNG Market Potentially Leading to a Future AFLOAT
Reimagine LNG – An Overview of the LNG Market Potentially Leading to a Future AFLOAT
Objective / Scope LNG has proven its worth, to meet energy demands throughout the globe at scale, whilst providing the cleanest fossil fuel. To complement the eme...
Floating LNG: New Rule Note for the Classification of LNG FPSO
Floating LNG: New Rule Note for the Classification of LNG FPSO
Abstract Offshore LNG terminals are today broadly considered by the industry to respond to the world thirst of energy in a rapid and efficient manner. In order to...
Development of Innovative LNG Production, Transportation, and Regasification System
Development of Innovative LNG Production, Transportation, and Regasification System
Abstract Development of economic means of gas transportation to long distance has been important technical and economic tasks in gas industries. In addition to th...
Trade/Investment in LNG - Asia/Pacific Region
Trade/Investment in LNG - Asia/Pacific Region
History/Growth of LNG Business As the world-wide demand for natural gas grows, so too does the international trade in LNG. The growth in gas demand, which in the ...
LNG Imports Into North America and Implications
LNG Imports Into North America and Implications
Abstract The need for LNG to fill the natural gas supply gap in North America may increase dramatically to 2015 and beyond as natural gas demand increases at rate...
Reviewing the impact of LNG technology advancements on global energy markets
Reviewing the impact of LNG technology advancements on global energy markets
Rapid technological advancements in Liquefied Natural Gas (LNG) have catalyzed a transformative shift in global energy markets. This review delves into the profound impact of LNG t...

Back to Top