Supersonic LNG Chiller Using Recycled Cold Gas Instead of Cold Boxes

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Solution Overview

Problem

Traditional LNG producing systems are costly and large due to the use of cold boxes with nitrogen or mixed refrigerants, which are inefficient and expensive for cooling natural gas.

Innovation Solution

A system utilizing a supersonic chiller and heat exchanger configuration to cool and liquefy natural gas, eliminating the need for a traditional cold box by recycling chilled gaseous natural gas to provide the necessary cooling, thereby reducing system size and complexity.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Temperature

If a traditional cold box with nitrogen or mixed refrigerants is used to cool natural gas, then the natural gas can be liquefied, but the system size and cost increase significantly

Engineering Contradiction:
Improvenatural gas cooling temperatureVSAvoidcold box size
Core Design Contradiction:
TemperatureVSVolume of stationary object

Solution Approach 1:

The patent extracts and eliminates the traditional cold box component from the LNG system by using a supersonic chiller instead. The supersonic chiller uses expansion nozzles to directly cool the natural gas stream through isentropic expansion, removing the need for separate refrigerant circulation systems and cold box infrastructure.

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The patent replaces the mechanical refrigerant circulation system (compressors, heat exchangers, expansion valves) with a supersonic expansion-based cooling system. The supersonic chiller uses high-velocity gas flow through expansion nozzles to achieve cooling through kinetic energy conversion and isentropic expansion, eliminating complex mechanical refrigeration equipment.

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

2Temperature

If a traditional cold box with nitrogen or mixed refrigerants is used to cool natural gas, then the natural gas can be liquefied, but the system cost increases

Engineering Contradiction:
Improvenatural gas cooling temperatureVSAvoidsystem cost
Core Design Contradiction:
TemperatureVSEase of manufacture

Solution Approach 1:

The patent extracts and eliminates the traditional cold box component from the LNG system by using a supersonic chiller instead. The supersonic chiller uses expansion nozzles to directly cool the natural gas stream through isentropic expansion, removing the need for separate refrigerant circulation systems and cold box infrastructure.

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The patent replaces the mechanical refrigerant circulation system (compressors, heat exchangers, expansion valves) with a supersonic expansion-based cooling system. The supersonic chiller uses high-velocity gas flow through expansion nozzles to achieve cooling through kinetic energy conversion and isentropic expansion, eliminating complex mechanical refrigeration equipment.

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

3Temperature

If nitrogen or mixed refrigerants are used in the cold box, then cooling capacity is achieved, but system complexity increases

Engineering Contradiction:
Improvecooling capacityVSAvoidsystem complexity
Core Design Contradiction:
TemperatureVSDevice complexity

Solution Approach 1:

The patent extracts and eliminates the traditional cold box component from the LNG system by using a supersonic chiller instead. The supersonic chiller uses expansion nozzles to directly cool the natural gas stream through isentropic expansion, removing the need for separate refrigerant circulation systems and cold box infrastructure.

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The patent replaces the mechanical refrigerant circulation system (compressors, heat exchangers, expansion valves) with a supersonic expansion-based cooling system. The supersonic chiller uses high-velocity gas flow through expansion nozzles to achieve cooling through kinetic energy conversion and isentropic expansion, eliminating complex mechanical refrigeration equipment.

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

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 system effectively produces liquefied natural gas with a smaller, more efficient design, reducing costs and improving operational efficiency by utilizing the recycled cold energy from the chilled gaseous natural gas stream.

Implementation Method 1

a supersonic chiller configured to chill the cooled natural gas stream to a production temperature to produce the LNG and output a chilled gaseous natural gas stream

Methodology Applied
Scientific EffectSupersonic expansion: De Laval Nozzle

Implementation Method 2

The compressed fluid is passed in succession through three counterflow heat exchangers to be further cooled and then expanded in a nearly isentropic expansion nozzle

Methodology Applied
Scientific EffectIsentropic expansion: Adiabatic Cooling

Implementation Method 3

the compressed natural gas stream is cooled together with the feed natural gas stream by heat exchanging with the chilled gaseous natural gas stream

Methodology Applied
Scientific EffectHeat exchange: Heat Exchanger

Data Source

PatentEP3479037B1System and method for producing liquefied natural gas
Publication Date: 2024.02.14 BAKER HUGHES OILFIELD OPERATIONS LLC
  • EP3479037B1 patent drawingFigure 1
  • EP3479037B1 patent drawingFigure 2
  • EP3479037B1 patent drawingFigure 3

AI summary

A system, and a method for producing liquefied natural gas are provided. The system includes a heat exchanger, a first supersonic chiller, and a compression unit. The heat exchanger is for cooling a feed natural gas stream to obtain a cooled natural gas stream. The first supersonic chiller is for chilling the cooled natural gas stream to produce liquefied natural gas and output at least a portion of chilled gaseous natural gas to the heat exchanger to be heated to obtain a heated natural gas stream. The compression unit is for compressing the heated natural gas stream from the heat exchanger and providing a compressed natural gas stream to the heat exchanger to be cooled together with the feed natural gas stream by heat exchanging with the at least a portion of the chilled gaseous natural gas.