LNG Container Recondenser Design to Reduce BOG Stratification

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Solution Overview

Problem

Existing methods for boiling-off gas (BOG) recondensation in liquefied natural gas (LNG) storage face inefficiencies due to high nitrogen content in BOG, leading to stratification and incomplete recondensation, as well as the need for cumbersome nozzle designs to enhance surface exchange for effective recondensation.

Innovation Solution

A method and apparatus for BOG recondensation using a recondenser that reintroduces subcooled LNG to directly mix with recondensed gas, minimizing stratification risks and achieving efficient recondensation by optimizing the recondensation process within a separated drum or integrated container setup, with control valves managing gas flow and temperature.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If direct contact recondensation of BOG with LNG is used, then recondensation efficiency is improved, but stratification occurs due to high nitrogen content in BOG

Engineering Contradiction:
Improverecondensation efficiencyVSAvoidstratification
Core Design Contradiction:
ProductivityVSStability of the object's composition

Solution Approach 1:

The recondensation process is divided into two distinct stages: first, pre-cooling BOG in a separate section to reduce its temperature and nitrogen content; second, recondensing the pre-cooled BOG in another section. This segmentation prevents direct mixing of warm BOG with LNG, thereby avoiding stratification while maintaining recondensation efficiency.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

A pre-cooling section acts as an intermediary between the BOG inlet and the main recondensation zone. This intermediate zone allows BOG to be partially condensed and cooled before entering the main LNG contact area, serving as a buffer that prevents the harmful direct mixing of high-nitrogen BOG with stored LNG.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Productivity

If high surface exchange is achieved through complex nozzle designs, then recondensation effectiveness is improved, but device complexity increases

Engineering Contradiction:
Improverecondensation effectivenessVSAvoidnozzle design complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The complex nozzle design is completely removed from the system. Instead of using specialized nozzles to achieve surface exchange, the invention extracts the recondensation function to a separate pre-cooling section where simple direct contact between pre-cooled BOG and LNG occurs, eliminating the need for complex geometries.

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

Instead of using complex nozzles to increase surface area for heat exchange, the invention inverts the approach by using simple direct contact in a separated pre-cooling zone. The high surface exchange is achieved not through nozzle geometry but through the phase change process itself in a simplified configuration.

Inventive Principle:
Principle #13The other way round (Inversion)

3Stress or pressure

If subcooled LNG is injected into container to control pressure, then pressure stabilization is improved, but stratification and flashing risks increase

Engineering Contradiction:
Improvepressure stabilizationVSAvoidstratification and flashing
Core Design Contradiction:
Stress or pressureVSStability of the object's composition

Solution Approach 1:

The system performs preliminary recondensation of BOG in a separate pre-cooling section before the recondensed liquid is injected back into the container. This preliminary action ensures that the liquid returned to the container is already at a stable temperature and composition, preventing stratification and flashing upon injection while maintaining pressure control.

Inventive Principle:
Principle #10Preliminary action

Applied Scientific Principles

This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.

Function Achieved in This Case

The solution effectively reduces stratification and ensures complete recondensation of BOG, minimizing venting and enhancing the composition and temperature match of recondensed liquid with stored LNG, thereby stabilizing container pressure and preventing flashing.

Implementation Method 1

The recondenser has a first inlet for evaporated gas, a second inlet for subcooled liquefied gas and an outlet for recondensed gas

Methodology Applied
Scientific EffectHeat exchange: Heat Exchanger

Implementation Method 2

A method and apparatus for BOG recondensation using a recondenser that reintroduces subcooled LNG to directly mix with recondensed gas

Methodology Applied
Scientific EffectCondensation: Condensation

Implementation Method 3

means for withdrawing liquefied gas from one or more of the at least one container and supplying it to a refrigeration unit for subcooling the liquefied gas

Methodology Applied
Scientific EffectSubcooling: Supercooling

Data Source

PatentEP3658815B1Method and apparatus for storing liquefied gas in and withdrawing evaporated gas from a container
Publication Date: 2023.03.01 CRYOSTAR
  • EP3658815B1 patent drawingFigure 1a
  • EP3658815B1 patent drawingFigure 1b
  • EP3658815B1 patent drawingFigure 1c

AI summary

The present invention relates to a method and an apparatus for storing liquefied gas in at least one insulated container (1) while withdrawing evaporated gas from one or more of the at least one container (1), wherein at least a part of the evaporated gas is supplied to a recondenser (11) and wherein liquefied gas is withdrawn from one or more of the at least one container (1) and at least in part supplied to the recondenser (11) for recondensing the evaporated gas supplied to the recondenser (11) such that recondensed gas is obtained at a recondenser outlet, wherein before supplying the liquefied gas to the recondenser (11), the liquefied gas is subcooled by passing it through a refrigeration unit (8, 9), at least a part of the subcooled liquefied gas being supplied to the recondenser (11), and wherein at least a part of the recondensed gas obtained at the outlet of the recondenser (11) is reintroduced into one or more of the at least one container (1).