1 Test of flexible LNG transfer hose with
sub-cooled LN2
As part of the global development of LNG marine transportation, it is
necessary to develop and qualify flexible transfer hoses of LNG between
the Floating Liquefied Natural Gas Plant (FLNG) and the LNG tanker. These
hoses must be tested for mechanical stresses until rupture under a pressure
of 20 to 30 bars. By using sub-cooled LN2 in replacement of LNG, the blast
is reduced during the rupture. The tests are performed at about -190°C at a
pressure up to 30 bars. The rupture of the hose results in instant
de-pressurization to atmospheric pressure. The more the LN2 is sub-cooled,
the lower is the blast caused by evaporation (BLEVE).
Cryogenic Engineering
Cryogenics
Unlike refrigeration by mechanical means where the refrigerant works in a closed circuit, cryogenic
refrigeration is an open-circuit refrigeration with evaporation of the liquid and exhaust of the gas to the
atmosphere. For safety and cost reasons, nitrogen is commonly used, allowing reaching -200°C. In these
applications, liquid nitrogen (LN2) undergoes a phase change (vaporization) by absorbing heat energy. LN2
can be implemented in many areas, most notably food and pharmaceuticals.
In the industry, the LN2 use is competitive for all batch processes where the refrigeration power required is
high and discontinuous. The heat exchange by direct contact between LN2 and the application is not always
possible or desired. The use of LN2 (a very low temperature fluid -180°C to -196°C) must be adapted to
the industrial application requiring temperatures usually in the range of 0°C to -100°C.
This is achieved by interposing between the LN2 and the application an intermediate medium (thermal
processor) maintained at a temperature close to
the temperature required for use. RLD has
developed and realized several types of such
temperature transformers:
•
tube/shell exchangers for liquid or gaseous
coolant
•
aluminum block exchangers
•
heat pipe exchangers
2. Oxygen Vaporizer (6,000 Nm3/h)
To warm up the cryogenic fluid, the only energy used by an atmospheric
vaporizer is heat taken from the ambient air. In the case of pool-like
vaporizers where water is used as intermediate fluid, the objective is
always to use ‘free’ water at room temperature, for example water taken
from the existing network of the plant or ground water. When the
available water does not meet the energy requirement, conventional
heating processes are used. To minimize the energy consumption, it is
important to design vaporizers able to work at low temperatures. RLD
offers vaporizer designs based on different technologies:
•
tube/shell type
•
pool type with exchange tubes arranged in concentric layers along a
vertical axis
3. VCO2 Vaporizer (2,000 kg/h)
In soft drink manufacturing, the CO2 vaporizer plays a dual role:
• Provide the gaseous CO2 introduced into the sparkling water
• Reduce the load of the refrigeration units
The tube/shell type vaporizer is mounted in series in the existing cold
water network of the factory. At a continuous CO2 flow of 2,000 kg/h
the vaporizer provides a cooling capacity of 175 kW (150,000
kcal/hour) at +10°C.
4. Thermal Vacuum Chambers
The components on board satellites are subject to the thermal stresses due
to the cyclical exposure to solar radiations. Tests are performed in Thermal
Vacuum (TV) chambers that simulate the space conditions: a vacuum of
about 10-6 mbar combined with a thermal environment from -180°C to
+200°C. The component to be tested is located on a conductive plate (A) in
the center of radiation screens (B). The temperatures of A and B are
controlled by circulating a thermal fluid cooled down by LN2 and by an
electrically heater. RLD has significantly improved the designs that were
traditionally used to optimize the overall LN2 consumption through the
definition of specific conductive plates, LN2 exchangers, circulators and
screens.