Cryogenic Carbon Capture System and Method with Integrated Liquid Natural Gas Vaporizer
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Solution Overview
Problem
Existing systems for integrating cryogenic carbon capture with liquid natural gas vaporization lack efficiency and cost-effectiveness, necessitating improved methods for separating carbon dioxide from flue gases while efficiently vaporizing LNG.
Innovation Solution
A system and method that integrates cryogenic carbon capture with LNG vaporization by using a pre-cool heat exchanger, desublimating heat exchanger, contact liquid heat exchanger, and solid separation device to separate CO2 from a process gas stream, forming a CO2-laden slurry and a CO2-depleted stream, with cooling provided by LNG streams.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Manufacturing precision
If cryogenic carbon capture system is used to separate CO2 from flue gas, then CO2 separation efficiency is improved, but system complexity and operational cost increase
Solution Approach 1:
The patent combines two separate processes - cryogenic CO2 capture and LNG vaporization - into a single integrated system. The CO2 capture system's cold stream is used to vaporize LNG, while the LNG vaporization process provides cooling for the CO2 separation. This merging eliminates the need for separate heating and cooling systems, reducing overall system complexity while maintaining high CO2 separation efficiency.
Solution Approach 2:
The integrated system performs multiple functions simultaneously: it separates CO2 from flue gas, vaporizes LNG, and provides both cooling and heating requirements through a single process flow. The cold stream from the CO2 capture process serves dual purposes by cooling the flue gas and vaporizing the LNG, making the system more versatile and less complex.
2Productivity
If LNG vaporization is performed using external heating, then vaporization effectiveness is improved, but energy cost and operational expense increase
Solution Approach 1:
The patent converts the cold stream that would otherwise be a waste product of the CO2 capture process into a useful resource for vaporizing LNG. Instead of discarding the cold stream or using additional energy to heat the LNG, the system utilizes the temperature differential between the cold stream and the liquid LNG to achieve vaporization, thereby converting a potential disadvantage into a benefit and reducing energy costs.
Solution Approach 2:
The system is designed to be self-sufficient by using its own internal cold stream to vaporize the LNG without requiring external heating sources. The CO2 capture process itself provides the cooling necessary for its operation and simultaneously provides the cold stream needed for LNG vaporization, making the system self-service and reducing operational expenses.
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
Achieves efficient separation of CO2 from flue gases and effective vaporization of LNG, reducing environmental impact and operational costs by optimizing the integration of carbon capture and vaporization processes.
Implementation Method 1
a pre-cool heat exchanger configured to receive and cool a process gas stream so that a cooled process gas stream is formed
Implementation Method 2
The pre-cool heat exchanger is configured to warm the clean process gas stream to provide cooling for the process gas stream
Implementation Method 3
A contact liquid heat exchanger is in fluid communication with the contact liquid inlet of the desublimating heat exchanger and is configured to receive and warm a liquid natural gas stream to provide cooling within the contact liquid heat exchanger
Implementation Method 4
A contact liquid heat exchanger is in fluid communication with the contact liquid inlet of the desublimating heat exchanger and is configured to receive and warm a liquid natural gas stream
Implementation Method 5
The desublimating heat exchanger is configured to contact the cooled process gas stream received from the pre-cool heat exchanger with contact liquid cooled by the contact liquid heat exchanger so that carbon dioxide is absorbed within the contact liquid
Implementation Method 6
A solid separation device is in fluid communication with the contact liquid inlet of the desublimation heat exchanger and is configured to receive the carbon dioxide laden slurry stream from the slurry outlet of the desublimating heat exchanger and to separate the slurry stream into a condensed carbon dioxide stream and a contact liquid stream
Data Source
AI summary
A desublimating heat exchanger receives a cooled process gas stream from a pre-cool heat exchanger and includes a clean gas outlet, a contact liquid inlet and a slurry outlet. A contact liquid heat exchanger communicates with the contact liquid inlet of the desublimation heat exchanger and warms a liquid natural gas stream to provide cooling within the contact liquid heat exchanger. The desublimating heat exchanger contacts the cooled process gas stream with the cooled contact liquid so that carbon dioxide is absorbed within the contact liquid whereby a carbon dioxide laden slurry stream and a carbon dioxide depleted clean process gas stream are formed. The clean process gas stream passes through the clean gas outlet to the pre-cool heat exchanger and the slurry stream passes through the slurry outlet. The pre-cool heat exchanger warms the clean process gas stream to provide cooling for the process gas stream. A solid separation device communicates with the contact inlet of the desublimating heat exchanger and separates the carbon dioxide laden slurry stream from the desublimating heat exchanger into a condensed carbon dioxide stream and a contact liquid stream.


