Integrated Cold Box Heat Exchanger for Natural Gas Liquid Recovery

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Solution Overview

Problem

Current natural gas liquid recovery systems face inefficiencies in energy consumption and heat recovery due to the lack of effective process integration, particularly in the heating and cooling processes involved in petroleum refining.

Innovation Solution

The implementation of a natural gas liquid recovery system that includes a cold box with a plate-fin heat exchanger and a refrigeration system with a primary and secondary refrigerant loop, utilizing a mixture of hydrocarbons as refrigerants to efficiently transfer heat and condense feed gases, thereby enhancing energy efficiency and reducing utility usage.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Use of energy by moving object

If traditional natural gas liquid recovery systems are used without process integration, then the system structure is simple, but energy consumption is high and heat recovery is inefficient

Engineering Contradiction:
Improveenergy consumptionVSAvoidsystem complexity
Core Design Contradiction:
Use of energy by moving objectVSDevice complexity

Solution Approach 1:

The patent combines multiple heat exchange operations into a single integrated cold box system with plate-fin heat exchangers. The cold box integrates refrigeration cycles, heat recovery, and natural gas liquid separation functions that were previously performed by separate units, thereby reducing energy consumption while managing system complexity through functional integration

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The cold box system performs multiple functions simultaneously: it provides refrigeration for gas cooling, recovers heat from process streams, separates natural gas liquids, and pre-cools feed gas. This multi-functionality reduces the need for separate dedicated equipment, improving energy efficiency without proportionally increasing system complexity

Inventive Principle:
Principle #6Universality (Multi-functionality)

2Loss of energy

If process integration with heat exchange is implemented, then heat recovery is improved and energy efficiency increases, but device complexity increases

Engineering Contradiction:
Improveheat recoveryVSAvoidsystem complexity
Core Design Contradiction:
Loss of energyVSDevice complexity

Solution Approach 1:

Multiple heat exchangers are merged into integrated plate-fin heat exchanger assemblies within the cold box. These consolidated units recover heat from various process streams (refrigerant condensers, gas outlets, liquid outlets) and transfer it to feed gas and other cold streams, maximizing heat recovery while reducing the number of separate heat exchange devices

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The heat exchange network operates continuously to recover heat from all process streams. The integrated cold box system maintains continuous heat transfer between hot and cold streams throughout operation, ensuring that useful heat recovery action is ongoing without interruption, thereby reducing overall energy loss

Inventive Principle:
Principle #20Continuity of useful action

3Ease of operation

If utility streams are used for heating and cooling, then process operations are maintained, but operating costs increase

Engineering Contradiction:
Improveprocess operationVSAvoidutility usage
Core Design Contradiction:
Ease of operationVSUse of energy by stationary object

Solution Approach 1:

The process system serves itself by internally recovering and redistributing heat from process streams. The cold box system uses heat from refrigerant condensation, gas outlet streams, and liquid outlet streams to cool feed gas and other process streams, reducing or eliminating the need for external utility steam and cooling water, thereby reducing operating costs while maintaining process operations

Inventive Principle:
Principle #25Self-service

Solution Approach 2:

Heat that would otherwise be discarded from process streams (refrigerant condenser heat, hot gas outlet heat, hot liquid outlet heat) is recovered and reused to cool feed gas and other cold streams. This recovery and reuse of previously wasted thermal energy reduces utility consumption while keeping the process running efficiently

Inventive Principle:
Principle #34Discarding and recovering

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

This configuration reduces energy consumption, decreases operating costs, and improves heat recovery by effectively integrating heat exchange across various process streams, leading to a more efficient and cost-effective natural gas liquid recovery process.

Implementation Method 1

The cold box is configured to transfer heat from hot fluids in the natural gas liquid recovery system to cold fluids in the natural gas liquid recovery system

Methodology Applied
Scientific EffectHeat transfer: Heat Exchanger

Implementation Method 2

The chill down train can be configured to condense at least a portion of the feed gas in at least one compartment of the cold box

Methodology Applied
Scientific EffectCondensation: Condensation

Implementation Method 3

The separator can be configured to separate the feed gas into a liquid phase and a refined gas phase

Methodology Applied
Scientific EffectPhase change: Phase Change

Implementation Method 4

The refrigeration system includes a first subcooler configured to transfer heat between the primary refrigerant of the primary refrigerant loop and the secondary refrigerant of the secondary refrigerant loop

Methodology Applied
Scientific EffectHeat transfer: Heat Exchanger

Data Source

PatentUS11320196B2Process integration for natural gas liquid recovery
Publication Date: 2022.05.03 SAUDI ARABIAN OIL CO
  • US11320196B2 patent drawing
  • US11320196B2 patent drawing
  • US11320196B2 patent drawing

AI summary

This specification relates to operating industrial facilities, for example, crude oil refining facilities or other industrial facilities that include operating plants that process natural gas or recover natural gas liquids.