Objectives Finished Cooling Towers and Adiabatic Humidifiers Cooling Cycles Refrigerants
Air Washer Sprays liquid water into air stream Typically, air leaves system at lower temperature and higher humidity than it enters
Schematic
Air Washers/Evaporative Coolers Heat and mass transfer is mutually compensating Can evaluate based on temperature drop, humidification, or comparison to other energy exchangers
Cooling Tower Similar to an evaporative cooler, but the purpose is often to cool water Widely used for heat rejection in HVAC systems Also used to reject industrial process heat
Cooling Tower
Solution Can get from Stevens diagram (page 272) Can also be used to determine Minimum water temperature Volume of tower required Can be evaluated as a heat exchanger by conducting NTU analysis
Real World Concerns We need to know mass transfer coefficients They are not typically known for a specific direct-contact device Vary widely depending on packing material, tower design, mass flow rates of water and air, etc. In reality, experiments are typically done for a particular application Some correlations are in Section 10.5 in your book Use with caution
Summary Heat rejection is often accomplished with devices that have direct contact between air and water Evaporative cooling Can construct analysis of these devices Requires parameters which need to be measured for a specific system
Vapor Compression Cycle Expansion Valve
Efficiency First Law Second law Coefficient of performance, COP COP = useful refrigerating effect/net energy supplied COP = qr/wnet Second law Refrigerating efficiency, ηR ηR = COP/COPrev Comparison to ideal reversible cycle
Carnot Cycle No cycle can have a higher COP All reversible cycles operating at the same temperatures (T0, TR) will have the same COP For constant temp processes dq = Tds COP = TR/(T0 – TR)
Real Cycles Assume no heat transfer or potential or kinetic energy transfer in expansion valve COP = (h3-h2)/(h4-h3) Compressor displacement = mv3
Example R-22 condensing temp of 30 °C (86F) and evaporating temp of 0°C (32 F) Determine qcarnot wcarnot Diminished qR and excess w for real cycle caused by throttling and superheat horn ηR
Comparison Between Single-Stage and Carnot Cycles Figure 3.6
Subcooling and Superheating Refrigerant may be subcooled in condenser or in liquid line Temperature goes below saturation temperature Refrigerant may be superheated in evaporator or in vapor (suction) line Temperature goes above saturation temperature
Two stage systems
Multistage Compression Cycles Combine multiple cycles to improve efficiency Prevents excessive compressor discharge temperature Allows low evaporating temperatures (cryogenics)
What are desirable properties of refrigerants? Pressure and boiling point Critical temperature Latent heat of vaporization Heat transfer properties Viscosity Stability
In Adition…. Toxicity Flammability Ozone-depletion Greenhouse potential Cost Leak detection Oil solubility Water solubility
Refrigerants What does R-12 mean? ASHRAE classifications From right to left ← # fluorine atoms # hydrogen atoms +1 # C atoms – 1 (omit if zero) # C=C double bonds (omit if zero) B at end means bromine instead of chlorine a or b at end means different isomer (b is generally less symmetric)
Refrigerant Conventions Mixtures show mass fractions Zeotropic mixtures Change composition/saturation temperature as they change phase at a constant pressure 400 series (if commercialized) Azeotropic mixtures Behaves as a monolithic substance Composition stays same as phase changes 500 series (if commercialized)
More Refrigerant Arcana Organic refrigerants – 600 series Inorganic refrigerants 700 + molecular weight
Inorganic Refrigerants Ammonia (R717) Boiling point? Critical temp = 271 °F Freezing temp = -108 °F Latent heat of vaporization? Small compressors and linesets Excellent heat transfer capabilities Not particularly flammable But…
Carbon Dioxide (R744) Recent ASHRAE papers Evaluation of carbon dioxide as R-22 substitute for residential air-conditioning Brown, J. Steven (Department of Mechanical Engineering, Catholic University of America); Kim, Yongchan; Domanski, Piotr A. Source: ASHRAE Transactions, v 108 PART 2, 2002, p 954-963 Abstract: This paper compares the performance of CO2 and R-22 in residential air-conditioning applications using semi-theoretical vapor compression and transcritical cycle models. The simulated R-22 system had a conventional component configuration, while the CO2 system also included a liquid-line/suction-line heat exchanger. The CO2 evaporator and gas cooler were microchannel heat exchangers originally designed for CO2. The R-22 heat exchangers employed the same microchannel heat exchangers as CO2 with the difference that we modified the refrigerant passages to obtain reasonable pressure drops. The study covers several heat exchanger sizes. The R-22 system had a significantly better coefficient of performance (COP) than the CO2 system when equivalent heat exchangers were used in the CO2 and R-22 systems, which indicates that the better transport properties and compressor isentropic efficiency of CO2 did not compensate for the thermodynamic disadvantage of the transcritical cycle in comfort cooling applications. An entropy generation analysis showed that the CO2 evaporator operated with fewer irreversibilities than did the R-22 evaporator. However, the CO2 gas cooler and expansion device generated more entropy than their R-22 counterparts and were mainly responsible for the low COP of the CO2 system. (33 refs.) Cheap, non-toxic, non-flammable Critical temp? Huge operating pressures Often no phase change
Water (R718) Two main disadvantages? ASHRAE Handbook of Fundamentals Ch. 20
Water in refrigerant Water + Halocarbon Refrigerant = (strong) acids or bases Corrosion Solubility Free water freezes on expansion valves Use a dryer (desiccant) Keep the system dry during installation/maintenance
Oil Miscible refrigerants (11,12, 21,113) High enough velocity to limit deposition Especially in evaporator Immiscible refrigerants (717,744,13,14) Use a separator to keep oil contained in compressor Intermediate (22, 114)
The Moral of the Story No ideal refrigerants Always compromising on one or more criteria Should be able to look up properties and analyze good candidates for refrigeration cycles