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V ARIABLES /* Type Name Temp T[n] Temp Ta Temp Tb HeatFlux Qa HeatFlux Qb PARAMETERS Role Def OUT 0 IN 65 IN 10 OUT 0 OUT 0 Min Max Description */ "Temp. at each node" "Temp. for side a of element" "Temp. for side b of element" "Heat flow rate into side a" "Heat flow rate into side b" Description */ "U-value, ref. Dy” "Inner diameter - DHW tank" "Outside diameter - DHW tank" "Height - DHW tank" "Ambient air temperature" Description */ "Node distance = H/n" /* Supplied parameters */ /* Type HeatCondL Length Length Length Temp Name Role Def U S_P 1 Di S_P 1 Dy S_P 1 H S_P 1 AT S_P 1 Min Max Min Max /* Calculated parameters */ /* Type Name Role Def Length dx C_P 0 MODEL_PARAMETERS /* Type Name Role Def INT n SMP 10 END_MODEL Min Max Description */ 1 BIGINT "Number of nodes" I2 Appendix I – The Transient Two-Dimensional Tank Model /* Energy and temperature equations at side a and b of the element */ Ta = AT; Tb = AT; Qa = U2*PI*((D**2)/4)*(AT-T[1]); Qb = U2*PI*((D**2)/4)*(AT-T[n]); PARAMETER_PROCESSING /* Calculations of constants */ dx := H/n; LINKS /* Type TQ TQ Name a_side b_side Variables */ Ta,POS_IN Qa; Tb,POS_IN Qb;PDF Image | Residential CO2 Heat Pump System for Combined
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CO2 Organic Rankine Cycle Experimenter Platform The supercritical CO2 phase change system is both a heat pump and organic rankine cycle which can be used for those purposes and as a supercritical extractor for advanced subcritical and supercritical extraction technology. Uses include producing nanoparticles, precious metal CO2 extraction, lithium battery recycling, and other applications... More Info
Heat Pumps CO2 ORC Heat Pump System Platform More Info
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