Cryogenic Compressor Startup Cooling to Minimize Process Gas Venting

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Solution Overview

Problem

Cryogenic compressors vent process fluid during transient cool-down periods, leading to product loss and increased costs, as existing systems are not designed to operate effectively during this phase without auxiliary cooling.

Innovation Solution

A multi-stage compressor system with inter-stage heat exchangers that circulate a coolant through heat exchangers and cooling jackets to manage fluid temperature during startup, allowing continuous operation without venting by routing fluid through heat exchangers or bypass conduits based on temperature criteria.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Loss of substance

If the compressor is designed to operate during transient cool-down period, then product loss is reduced, but the system complexity increases

Engineering Contradiction:
Improveproduct lossVSAvoidsystem complexity
Core Design Contradiction:
Loss of substanceVSDevice complexity

Solution Approach 1:

The system is divided into multiple functional segments: compression stages, interstage heat exchangers, bypass conduits, and control systems. Each segment operates semi-independently, allowing the compressor to handle both cryogenic and ambient temperature fluids through different pathways, thereby reducing product loss during startup without requiring a completely new system design

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The compressor system is designed with multi-functionality to handle both cryogenic process fluid compression and ambient temperature fluid compression through the same basic infrastructure. The interstage heat exchangers and bypass conduits enable the system to adapt its operation mode based on temperature conditions, eliminating the need for separate auxiliary cooling equipment

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

2Loss of substance

If auxiliary cooling equipment is added to prevent venting during startup, then product loss is reduced, but the device complexity and cost increase

Engineering Contradiction:
Improveproduct lossVSAvoidauxiliary equipment
Core Design Contradiction:
Loss of substanceVSDevice complexity

Solution Approach 1:

The compressor system serves itself during the cool-down period by using its own compression capability to circulate and compress the ambient temperature process fluid. The interstage heat exchangers utilize the compression process itself to gradually cool the system components, eliminating the need for external auxiliary cooling equipment while preventing product venting

Inventive Principle:
Principle #25Self-service

3Productivity

If the compressor operates with ambient temperature fluid during startup, then the system can run without venting, but the fluid temperature must be managed

Engineering Contradiction:
Improvecontinuous operationVSAvoidfluid temperature management
Core Design Contradiction:
ProductivityVSTemperature

Solution Approach 1:

The control system continuously monitors the temperature of the process fluid and the state of system components, dynamically adjusting the operation mode. Based on feedback signals, the controller determines when to route fluid through bypass conduits for ambient temperature compression and when to activate interstage heat exchangers for cooling, enabling continuous operation while maintaining appropriate temperature management

Inventive Principle:
Principle #23Feedback

Solution Approach 2:

The system dynamically transitions between different operational modes during startup: initially compressing ambient temperature fluid through bypass conduits, then gradually incorporating interstage cooling as components cool down, and finally operating in full cryogenic mode. This dynamic adaptation allows continuous operation while managing fluid temperature according to real-time system conditions

Inventive Principle:
Principle #15Dynamics

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

Enables the compressor to operate during the transient cool-down period without venting the process fluid, reducing product loss and associated costs, and accommodating cryogenic fluids without auxiliary cooling equipment.

Implementation Method 1

an interstage heat exchanger between each compression stage through which the process fluid flows

Methodology Applied
Scientific EffectHeat exchange: Heat Exchanger

Implementation Method 2

a first cooling jacket to provide cooling of the fluid in the first compression stage via heat exchange with the first coolant

Methodology Applied
Scientific EffectHeat exchange: Heat Exchanger

Data Source

PatentUS9494281B2Compressor assemblies and methods to minimize venting of a process gas during startup operations
Publication Date: 2016.11.15 AIR PROD & CHEM INC
  • US9494281B2 patent drawing
  • US9494281B2 patent drawing
  • US9494281B2 patent drawing

AI summary

Systems and methods are provided for compressing a cryogenic fluid using a multi-stage compressor. Coolant in a first coolant loop cools cooling jackets of the compression stages and/or inter-stage heat exchangers and warms a pre-compression heat exchanger. The temperature of the coolant in the first heat exchanger is moderated by ambient-air heat exchange. The process fluid is electively cooled by one of the interstage heat exchangers after each of the compression stage if the temperature of the process fluid is above a temperature criterion. This enables the system to operate through a transient period (cool down period) without venting process fluid. The interstage heat exchangers are preferably bypassed when the system reaches steady-state operating temperature.