System for preparing deeply subcooled liquid oxygen based on mixing of liquid oxygen and liquid nitrogen and then vacuum-pumping
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Solution Overview
Problem
The traditional vacuum-pumping method for deeply subcooling liquid oxygen is energy-intensive due to its low triple point temperature and saturation pressure, limiting its subcooling efficiency and increasing costs, while existing methods like helium bubbling are costly and inefficient.
Innovation Solution
A system that mixes liquid oxygen and liquid nitrogen, leveraging their phase equilibrium to achieve a lower eutectic point temperature and higher saturation pressure, allowing for deeper subcooling of liquid oxygen at lower vacuum-pumping costs, using a secondary and primary subcooler with a vacuum multilayer heat-insulated pipeline and a pumping-out device.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Temperature
If the traditional vacuum-pumping method is used to deeply subcool liquid oxygen to its triple point temperature, then the subcooling degree is improved, but the energy consumption and vacuum-pumping cost increase significantly
Solution Approach 1:
The patent introduces liquid nitrogen as an intermediary cooling medium. Instead of directly vacuum-pumping liquid oxygen to achieve subcooling, the system uses liquid nitrogen (cooled to its triple point) as a heat sink to extract heat from liquid oxygen, achieving the desired subcooling effect with much lower vacuum requirements and energy consumption.
Solution Approach 2:
The patent replaces the mechanical vacuum-pumping process with a thermal heat-exchange process. By substituting the mechanical removal of vapor with a thermal coupling approach using liquid nitrogen, the system achieves subcooling without the high energy costs associated with maintaining deep vacuum conditions.
2Temperature
If liquid nitrogen is evacuated to its triple point to subcool liquid oxygen, then the subcooling efficiency is improved, but the saturation pressure remains too high to achieve deep subcooling below 63.2 K
Solution Approach 1:
The patent applies preliminary cooling to liquid nitrogen, evacuating it to its triple point (63.2 K) first. This pre-cooled liquid nitrogen then serves as an ultra-cold heat sink, enabling liquid oxygen to be cooled below its own triple point temperature through heat exchange, overcoming the pressure limitation.
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 approach enables liquid oxygen to be subcooled to its triple point temperature at a lower cost, maximizing subcooling efficiency by utilizing the cold energy of the gas mixture and reducing the pumping-out device's performance requirements, primarily consuming nitrogen over oxygen.
Implementation Method 1
mixes liquid oxygen and liquid nitrogen, leveraging their phase equilibrium to achieve a lower eutectic point temperature and higher saturation pressure
Implementation Method 2
vacuum-pumping method can subcool the cryogenic working medium to a temperature near the triple point with a readily-available device and low cost
Implementation Method 3
utilizing the cold energy of the gas mixture and reducing the pumping-out device's performance requirements
Data Source
AI summary
A system for preparing subcooled liquid oxygen based on mixing of liquid oxygen and liquid nitrogen and then vacuum-pumping, including atmospheric-pressure saturated liquid nitrogen and oxygen tanks. An inlet of the liquid nitrogen tank communicates with pressurized gas, and an outlet is connected to an inlet a of a secondary subcooler. An inlet of the liquid oxygen tank communicates with the pressurized gas, and a first outlet is connected to an inlet b of the secondary subcooler. An outlet c of the secondary subcooler is connected to an inlet d of a primary subcooler. An outlet e of the primary subcooler is connected to a pumping-out device through a rewarming device. A second outlet of the liquid oxygen tank is connected to an inlet n of the primary subcooler. An outlet o of the primary subcooler is connected to an inlet r of the secondary subcooler.
