Advantages of the CO 2 refrigeration As a refrigerant CO 2 has excellent thermodynamic properties, in terms of good heat-transfer inside an evaporator.

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Presentation transcript:

Advantages of the CO 2 refrigeration As a refrigerant CO 2 has excellent thermodynamic properties, in terms of good heat-transfer inside an evaporator. CO 2 is a good detergent / solvent. It dissolves grease and cleans the inside of the systems where it is used. Using CO 2 as a fluid gives a relatively simple system. The main difference is that the pipes and components used are refrigeration components. On the other hand the pipe sizes are considerably smaller which means a low mass cooling system inside the particle detectors. Lower energy consumption Reduced carbon footprint Smaller pipes Less insulation Smaller pumps More economical operation Lower installation costs Work Package 13 Detectors and Data Acquisition An evaporative bi-phase cooling system based on CO 2 has been chosen as the best option to extract the heat produced by the read-out electronics in the CBM Silicon Tracking System. In the framework of the EU-FP7 project CRISP, the system TRACI (Transportable Refrigeration Apparatus for CO 2 Investigation), developed at NIKHEF/CERN to provide support to the ATLAS and LHCb experiments, is being upgraded at GSI from 100 W to 1 kW cooling power. This system TRACI-XL will be used as a testing device for the CBM application. The I-2PACL principle (Integrated 2 Phase Accumulator Controlled Loop) was created as simplification of the 2PACL systems by using the CO2 line to condensate the gas inside the accumulator instead of using a branched line derived from the condensing unit. This concept is under patent since Friday September 9th, Therefore the control is reduced to one cartridge heater controlled by PLC Siemens Simatic S The size of the control unit is decreased and it allows a wider range of possible operating temperatures from -30 C up to room temperature. I-2PACL concept applied to TRACI-XL Bitzer 2DC-3.F1Y Varispeed: at 30 Hz; Q 0 = 0,55 kW, T0 =-45 C, Tsuction = -30 C, Tc = +35 C, Tsub = 3 K, R404a. at 87 Hz; Q 0 = 1.59 kW, T0 = -45 C, Tsuction = -30 C, Tc = +35 C, Tsub = 3 K, R404a. Bitzer 2DC-3.F1Y Varispeed: at 30 Hz; Q 0 = 0,55 kW, T0 =-45 C, Tsuction = -30 C, Tc = +35 C, Tsub = 3 K, R404a. at 87 Hz; Q 0 = 1.59 kW, T0 = -45 C, Tsuction = -30 C, Tc = +35 C, Tsub = 3 K, R404a. The return line (8-1) contains a bi-phase mixture which is liquefied by the condensing unit named previously below the operating temperature. By controlling the pressure inside an accumulator the evaporation temperature can be fixed. This vessel contains two-phase CO 2 in contact. TRACI-XL Development The heat generated in the read-out electronics is absorbed and extracted by the evaporator capillaries inside the thermal box (5-6). 1.Accumulator 2.Flow meter 3.LEWA Pump (Remote head) 4.LEWA Pump (Flange motor) 5.Heat Exchanger 6.Fire Rod (heater) 7.Control System Box 8.Condensing Unit Platform 9.Compressor 2DC-3.F1Y Varispeed 10.Vacuum Pump --- CO2 (R744)Line --- Rest of the System Pulsation Dampener Calculation -45C -40C -30C J. Sánchez 1, J.M. Heuser 1, C. J. Schmidt 1, A. Lymanets 2, H. R. Schmidt 2 P. Petagna 3, B. Verlaat 3 and L. Zwalinski 3 1 GSI, Darmstadt, Germany; 2 Eberhard Karls University, Tübingen, Germany; 3 CERN, Geneva, Switzerland