Better performance and efficiency from Advantages and functions of an open flash

An open flash economizer can be used for both water-cooled and air-cooled compact , and also for split cooling systems. To optimise the cooling output, ENGIE equips all QUANTUM and QUANTUM-G models, as well as the SPECTRUM , with open flash .

Effect Benefits for customer Explanation

INCREASED • Lower investment costs per kilowatt of • Thermodynamic optimisation of the one-step COOLING OUTPUT cooling output (€/kW) cooling circuit through the integration of a mean level with flash extraction, resulting in higher specific evaporation

SMALL • Higher cooling output per m² • The optimum integration of the open flash INSTALLATION AREA of installation area economizer means that the installation dimen- sions of the chiller remain the same

INCREASE IN ENERGY • Lower operating costs at full load • Less technical work is required for the two-step EFFICIENCY (EER value compression process in comparison with the increases by up to 20 %) one-step compression process

HIGHER • Lower operating costs at partial load • The benefits of the economizer affect all ESEER VALUE operating points

OPTIMUM OPERATING • Maximum possible efficiency gain • Open flash economizer is inherently the BEHAVIOUR AT ALL under all operating conditions guaran- thermodynamically optimum solution LOAD LEVELS teed (e. g. changing cooling and heating media ) • Flash gas in saturation state; extraction without superheating • Maximum possible efficiency gain with partial load guaranteed • No efficiency-lowering suction gas superheating, with superheating control required Increased cooling output log p Cooling process in log p h diagram with open flash econo- mizer (Eco) (green) and without economizer (grey). The higher Condensation pressure evaporation enthalpy causes an increase in the cooling out- Medium pressure put. The size of this increase depends on the evaporation and Evaporation pressure condensation temperatures, and on the relationship between Pressure Two-step compression the condensation pressure and the evaporation pressure. with intermediate cooling In general: the higher the pressure ratio, the high- er the proportional gain in output and efficiency. h Evaporation enthalpy without Eco

Evaporation enthalpy with Eco

Comparison between open flash economizer and sub-cooling economizer

Cooling process with open flash economizer Cooling process with sub-cooling economizer and superheating control

Heating medium Heating medium

Condenser Condenser

M Open ash Superheating economizer control Compressor

Subcooler economizer Evaporator M M M

Chilled medium Chilled medium

An open flash economizer is an empty vessel without any The principle of the sub- is that the flow exchanging devices through which a refrigerant flows. from the condenser is divided before it enters the heat ex- In the process, the refrigerant from the condenser is regulated changer. A partial mass flow is regulated and evaporated in by an expansion valve and flows into the open flash econo- the on the secondary side, whereby the mizer. This creates flash gas and the refrigerant. Both main refrigerant flow is sub-cooled on the primary side. The phases occur in the saturation state, which is achieved auto- problem here is: matically at all operating conditions. The liquid refrigerant • A heat exchanger continually experiences exchange and flows into the evaporator and evaporates at increased evap- pressure losses oration enthalpy. The flash gas is extracted via the mean • The evaporating refrigerant must be expelled in a super- pressure connection of the compressor and is compressed heated state to avoid introducing liquid into the compressor to the condensation pressure again. No additional control • Exchange losses and superheating reduce the potential unit is required as the open flash economizer always operates efficiency gains optimally. • Every deviation from fixed setpoints (e. g. due to fluctuating heating and cooling media temperatures or at part loads) reduces the effectiveness

ENGIE Refrigeration GmbH Josephine-Hirner-Strasse 1 & 3 | D-88131 Lindau T + 49 8382 706-1 | F + 49 8382 706-410

[email protected] engie-refrigeration.de