Refrigeration 101 (PDF)

Total Page:16

File Type:pdf, Size:1020Kb

Refrigeration 101 (PDF) Refrigeration 101 Rusty Walker, Corporate Trainer Hill PHOENIX Compressor Basic Evaporator Condenser / Refrigeration Receiver Cycle Expansion Device Vapor Compression Cycle The MOVEMENT Cooling by the of HEAT from a removal of heat place where it is not wa nted to a place where it is unobjectionable How Heat is Removed What is heat? A form of energy What is cold? Absences of heat. How does heat High heat to low heat flow? Does cold NO flow? How is heat British Thermal Unit (BTU) measured? Heat is a form of energy and is measured British in BTU’s. Thermal Unit (BTU) A BTU is the quantity of heat required to raise the tempp,erature, of one p ound of water, one degree Fahrenheit. 1. Heat flows from high energy levels to a lower energy level. 1 2. Heat will n ot fl ow wi th out a 2 temperature difference 3 3. The greater the temperature difference, the faster the energy will flow. Radiation HtHeat Flows Three Ways Convection Conduction Conduction The transfer of heat Example: from molecule to Heating one end of molecule through a copper tube , will a substance by cause the other chain collision end to get hot. Convection Heat transfer by the Example: movement of •Convection oven molecules from •Forced air furnace one place to another. Radiation The transfer of heat Example: by passing from a Sunlight – goes source to an through a window absorbent surface without heating the without heating glass but heats the the space in su rface in the room between. it is shinning on. Temperature Temperature indicates the average velocity of the molecules of a substance. As the heat energy in a substance increases, it’ s molecules vibrate more intensely A thermometer measures the iiintensity of this vibrat ion. Thermometers do not measure heat, they measure the effect of heat. Temperature Animation The amount of heat (measured in BTU’s) required to raise one pound of a substance one degree Fahrenheit. Specific Heat Temp Rise (Deg F) Substance (BTU/LB/Deg F) (From 1 BTU Addition) Water (Liquid) 1.00 1.00 Ice 0.50 2.00 Steam 0480.48 2082.08 Aluminum 0.22 4.54 Brass 0.09 11.11 Physical State of a Substance Gas Adding heat Changing the energy in any of state of a the three states substance will Liquid will increase the require a larger temperature. quantity of heat energy. Solid Heat Energy There are two types of Heat 1. 2. Energy Sensible Heat Latent Heat 1. Is the energy of molecular motion 1 2. Causes a change in temperature, with 2 No change in state. 3. Sensible heat causes an increase in 3 molecular motion. 4 4. The addition or removal of sensible heat is measurable with a thermometer 1. Is the energy of molecular separation and arrangement. 1 2. Causes a ch an ge in state, whil e tteehere 2 is no change In temperature. 3 3. It can not be measured with a thermometer. Mechanical refrigeration The majority of heat is The majority of the works by changing the removed from the absorbed heat is state of the refrigerant. temperature controlled removed from the space as the refrigerant refrigeration system in absorbs heat when it the condenser as the changes state from a refrigerant changes liquid to a gas in the state from a gas back to evaporator. a liquid. Vapor Compression Cycle Example (Deg. F.) ( Deg. C.) 970 BTU’sNo are requiredmeasurable to changetemperature the water 250 to Latentsteam.Boilingchange Heat Water MeasurableSensibleSteam 212 100 200 tttHeatemperature 152 change 180MblMSiblSenseasura BTUibl’s e blare e 100 Liquid Heat Energy is addddded to requiredtemperatureHeat to reach Boiling 50 change 32 °F. (0°C) Water (liquid) 32 0 Point 25 100 200 400 600 800 1000 1100 1200 BTU’s The temperature Add Heat = Liquid to Vapor (Vaporization) at which a substance will change state from a liquid to a vapor or a vapor to a Remove Heat = Vapor to Liquid liquid (()Condensation) At a temperature Addition of Heat = Boiling equal to it’s boiling point or condidensing point, a substance can be both vapor and Removal Heat = Condensing liquid. 100% Liquid, no vapor present At a temperature blbelow i’it’s bo iling point, a substance is: 1lb. Of water @ 200o F. What is the state of water? - Sub-cooled liquid - Sub-cooled by 12o F. 100% vapor, no liquid present At a temperature above it’s boiling point, a substance is: 1lb. Of water @ 220o F. What is the state of water? - Super heated vapor (steam) - Super heated by 8o F. Example (Deg. F.) ( Deg. C.) A mixt ure of vapor 250 Temperature at 212 ° F. (100°C) Sensible = Saturatedand liquid. Mixture Temperature100MeasurableSteam % vapor Above 212 100 Heat212° F. (100°C) = 200 Su-temThereppperheatedperature is Va nopor 152 liquid.change Temperature100 % liquid below 100 212 °F. (100°C) = Saturation Temperature of Water -ThereSub-cooled isLiquid no is 212 °F. (100°C) at Sea Leve l 50 vapor. (0 PSIG / 14.7 PSIA) 32 0 25 100 200 400 600 800 1000 1100 1200 BTU’s Pressure: Defined as a force per unit of area PSI Bars KPA How does pressure flow? High To Low What would happen if you take Refrigerant flows two refrigerant from the tank tanks, one with with refrigerant to refrigerant and the the tank that is in other in a vacuum a vacuum, until and connect a the pressures hose between equalize. them? As the pressure on a substance increases, boiling temperature will increase. As pressure decreases, boiling temperature will also decrease. Pressure and boiling temperature follow each other At the boiling point we have both Liquid and Vapor . As the pressure increases, saturation temperature will increase. As pressure decreases, saturation temperature will also decrease. Pressure and boiling temperature follow each other At the saturation temperature we have a saturated mixture (both liquid and vapor are present). Atmospheric Pressure • At Sea Level, the atmospheric pressure on our bodies is 14.7 PSIA. • A column of air, one inch square and 60 miles high weighs 14.7 pounds. Pressure Scales Gauge Scale Absolute Scale ATMOSPHERE 0 PSIG 14.7 PSIA (Pressure @ Sea Level) 0 in Hg 29.92 in Hg Hg is the symbol for Mercury. VACUUM 29. 92 in Hg 0 in Hg Compound Gauge Gauge Scale: Positive Pressure Scale Vacuum Scale (Reference Only!) Vacuum Gauge Absolute Pressure in microns of Hg. Mercury Barometer Vacuum Atmospheric Pressure at Sea Level Column of mercury supporte77606d bcmy mm atmospheric29.92 in pressure. Hg 1 inch of Hg =25,400 microns Mercury A medium to move heat A substance that absorbs heat by evaporating at low temperatures What is a and pressures. refrigerant? And ggpives up heat by condensing at high temperatures and pressures Refrigerants No Longer Available R‐12 CFC R‐11 CFC R‐500 CFC R‐502 CFC • 100% Ozone • 100% Ozone • 66% Ozone • 28% Ozone depletion depletion depletion depletion potential • Used in • Used in • Used in • Used in centrifugals 50hz deep freezers every thing • Med. Temp • Med. - Low • Low. Temp • Med. – Low Te m p temp. Production Production Production Production ceased in 1995 ceased in 1995 ceased in 1995 ceased in 1995 RefrigerantsCurrently in Use R22HCFC RR134aHFC R507HFC 404AHFC • • 5% Ozone • 0% Ozone • 0% Ozone 0% Ozone depletion depletion depletion depletion • potential • Used in • Used in Used in • Used in auto A/C freezers deep freezers • every thing • Med. - Low •Low Temp Med. – Low • Med. – Low Te m p Te m p temp. Production phase out Replaced R-12 Replaced R-502 Compressor Refrigeration Evaporator Condenser / System Receiver Components Expansion Device Compressors Compressors Additional Compressor Types Example Mechanical Center Condensers CdCondensers Air Cooled Water Cooled Tube and fin Shell and tube Plate Evaporative Superheated Sub-cooled Vapor In Liquid Out Evaporative Plate Metering Device TXV and Electronic Evaporators Display Case Evaporators WalkWalk--InIn Evaporators Plate to Plate Heat Exchanger Questions.
Recommended publications
  • Energy Analysis and Carbon Saving Potential of a Complex Heating
    European Journal of Sustainable Development Research 2019, 3(1), em0067 ISSN: 2542-4742 Energy Analysis and Carbon Saving Potential of a Complex Heating System with Solar Assisted Heat Pump and Phase Change Material (PCM) Thermal Storage in Different Climatic Conditions Uroš Stritih 1*, Eva Zavrl 1, Halime Omur Paksoy 2 1 University of Ljubljana, SLOVENIA 2 Çukurova Üniversitesi, TURKEY *Corresponding Author: [email protected] Citation: Stritih, U., Zavrl, E. and Paksoy, H. O. (2019). Energy Analysis and Carbon Saving Potential of a Complex Heating System with Solar Assisted Heat Pump and Phase Change Material (PCM) Thermal Storage in Different Climatic Conditions. European Journal of Sustainable Development Research, 3(1), em0067. https://doi.org/10.20897/ejosdr/3930 Published: February 6, 2019 ABSTRACT Building sector still consumes 40% of total energy consumption. Therefore, an improved heating system with Solar Assisted Heat Pump (SAHP) was introduced in order to minimse the energy consumption of the fossil fuels and to lower the carbon dioxide emissions occurring from combustion. An energy analysis of the complex heating system for heating of buildings, consisting of solar collectors (SC), latent heat storage tank (LHS) and heat pump (HP) was performed. The analysis was made for the heating season within the time from October to March for different climatic conditions. These climatic conditions were defined using test reference years (TRY) for cities: Adana, Ljubljana, Rome and Stockholm. The energy analysis was performed using a mathematical model which allowed hourly dynamics calculation of losses and gains for a given system. In Adana, Rome and Ljubljana, it was found that the system could cover 80% of energy from the sun and the heat pump coefficient of performance (COP) reached 5.7.
    [Show full text]
  • Solar Heating and Cooling & Solar Air-Conditioning Position Paper
    Task 53 New Generation Solar Cooling & Heating Systems (PV or solar thermally driven systems) Solar Heating and Cooling & Solar Air-Conditioning Position Paper November 2018 Contents Executive Summary ............................................................. 3 Introduction and Relevance ................................................ 4 Status of the Technology/Industry ...................................... 5 Technical maturity and basic successful rules for design .............. 7 Energy performance for PV and Solar thermally driven systems ... 8 Economic viability and environmental benefits .............................. 9 Market status .................................................................................... 9 Potential ............................................................................. 10 Technical potential ......................................................................... 10 Costs and economics ..................................................................... 11 Market opportunities ...................................................................... 12 Current Barriers ................................................................. 12 Actions Needed .................................................................. 13 This document was prepared by Daniel Neyer1,2 and Daniel Mugnier3 with support by Alexander Thür2, Roberto Fedrizzi4 and Pedro G. Vicente Quiles5. 1 daniel neyer brainworks, Oberradin 50, 6700 Bludenz, Austria 2 University of Innsbruck, Technikerstr. 13, 6020 Innsbruck, Austria
    [Show full text]
  • Chapter 8 and 9 – Energy Balances
    CBE2124, Levicky Chapter 8 and 9 – Energy Balances Reference States . Recall that enthalpy and internal energy are always defined relative to a reference state (Chapter 7). When solving energy balance problems, it is therefore necessary to define a reference state for each chemical species in the energy balance (the reference state may be predefined if a tabulated set of data is used such as the steam tables). Example . Suppose water vapor at 300 oC and 5 bar is chosen as a reference state at which Hˆ is defined to be zero. Relative to this state, what is the specific enthalpy of liquid water at 75 oC and 1 bar? What is the specific internal energy of liquid water at 75 oC and 1 bar? (Use Table B. 7). Calculating changes in enthalpy and internal energy. Hˆ and Uˆ are state functions , meaning that their values only depend on the state of the system, and not on the path taken to arrive at that state. IMPORTANT : Given a state A (as characterized by a set of variables such as pressure, temperature, composition) and a state B, the change in enthalpy of the system as it passes from A to B can be calculated along any path that leads from A to B, whether or not the path is the one actually followed. Example . 18 g of liquid water freezes to 18 g of ice while the temperature is held constant at 0 oC and the pressure is held constant at 1 atm. The enthalpy change for the process is measured to be ∆ Hˆ = - 6.01 kJ.
    [Show full text]
  • Ammonia As a Refrigerant
    1791 Tullie Circle, NE. Atlanta, Georgia 30329-2305, USA www.ashrae.org ASHRAE Position Document on Ammonia as a Refrigerant Approved by ASHRAE Board of Directors February 1, 2017 Expires February 1, 2020 ASHRAE S H A P I N G T O M O R R O W ’ S B U I L T E N V I R O N M E N T T O D A Y © 2017 ASHRAE (www.ashrae.org). For personal use only. Additional reproduction, distribution, or transmission in either print or digital form is not permitted without ASHRAE’s prior written permission. COMMITTEE ROSTER The ASHRAE Position Document on “Ammonia as a Refrigerant” was developed by the Society’s Refrigeration Committee. Position Document Committee formed on January 8, 2016 with Dave Rule as its chair. Dave Rule, Chair Georgi Kazachki IIAR Dayton Phoenix Group Alexandria, VA, USA Dayton, OH, USA Ray Cole Richard Royal Axiom Engineers, Inc. Walmart Monterey, CA, USA Bentonville, Arkansas, USA Dan Dettmers Greg Scrivener IRC, University of Wisconsin Cold Dynamics Madison, WI, USA Meadow Lake, SK, Canada Derek Hamilton Azane Inc. San Francisco, CA, USA Other contributors: M. Kent Anderson Caleb Nelson Consultant Azane, Inc. Bethesda, MD, USA Missoula, MT, USA Cognizant Committees The chairperson of Refrigerant Committee also served as ex-officio members: Karim Amrane REF Committee AHRI Bethesda, MD, USA i © 2017 ASHRAE (www.ashrae.org). For personal use only. Additional reproduction, distribution, or transmission in either print or digital form is not permitted without ASHRAE’s prior written permission. HISTORY of REVISION / REAFFIRMATION / WITHDRAWAL
    [Show full text]
  • Heat Transfer in Flat-Plate Solar Air-Heating Collectors
    Advanced Computational Methods in Heat Transfer VI, C.A. Brebbia & B. Sunden (Editors) © 2000 WIT Press, www.witpress.com, ISBN 1-85312-818-X Heat transfer in flat-plate solar air-heating collectors Y. Nassar & E. Sergievsky Abstract All energy systems involve processes of heat transfer. Solar energy is obviously a field where heat transfer plays crucial role. Solar collector represents a heat exchanger, in which receive solar radiation, transform it to heat and transfer this heat to the working fluid in the collector's channel The radiation and convection heat transfer processes inside the collectors depend on the temperatures of the collector components and on the hydrodynamic characteristics of the working fluid. Economically, solar energy systems are at best marginal in most cases. In order to realize the potential of solar energy, a combination of better design and performance and of environmental considerations would be necessary. This paper describes the thermal behavior of several types of flat-plate solar air-heating collectors. 1 Introduction Nowadays the problem of utilization of solar energy is very important. By economic estimations, for the regions of annual incident solar radiation not less than 4300 MJ/m^ pear a year (i.e. lower 60 latitude), it will be possible to cover - by using an effective flat-plate solar collector- up to 25% energy demand in hot water supply systems and up to 75% in space heating systems. Solar collector is the main element of any thermal solar system. Besides of large number of scientific publications, on the problem of solar energy utilization, for today there is no common satisfactory technique to evaluate the thermal behaviors of solar systems, especially the local characteristics of the solar collector.
    [Show full text]
  • A Comprehensive Review of Thermal Energy Storage
    sustainability Review A Comprehensive Review of Thermal Energy Storage Ioan Sarbu * ID and Calin Sebarchievici Department of Building Services Engineering, Polytechnic University of Timisoara, Piata Victoriei, No. 2A, 300006 Timisoara, Romania; [email protected] * Correspondence: [email protected]; Tel.: +40-256-403-991; Fax: +40-256-403-987 Received: 7 December 2017; Accepted: 10 January 2018; Published: 14 January 2018 Abstract: Thermal energy storage (TES) is a technology that stocks thermal energy by heating or cooling a storage medium so that the stored energy can be used at a later time for heating and cooling applications and power generation. TES systems are used particularly in buildings and in industrial processes. This paper is focused on TES technologies that provide a way of valorizing solar heat and reducing the energy demand of buildings. The principles of several energy storage methods and calculation of storage capacities are described. Sensible heat storage technologies, including water tank, underground, and packed-bed storage methods, are briefly reviewed. Additionally, latent-heat storage systems associated with phase-change materials for use in solar heating/cooling of buildings, solar water heating, heat-pump systems, and concentrating solar power plants as well as thermo-chemical storage are discussed. Finally, cool thermal energy storage is also briefly reviewed and outstanding information on the performance and costs of TES systems are included. Keywords: storage system; phase-change materials; chemical storage; cold storage; performance 1. Introduction Recent projections predict that the primary energy consumption will rise by 48% in 2040 [1]. On the other hand, the depletion of fossil resources in addition to their negative impact on the environment has accelerated the shift toward sustainable energy sources.
    [Show full text]
  • (Vocs) in Asian and North American Pollution Plumes During INTEX-B: Identification of Specific Chinese Air Mass Tracers
    Atmos. Chem. Phys., 9, 5371–5388, 2009 www.atmos-chem-phys.net/9/5371/2009/ Atmospheric © Author(s) 2009. This work is distributed under Chemistry the Creative Commons Attribution 3.0 License. and Physics Characterization of volatile organic compounds (VOCs) in Asian and north American pollution plumes during INTEX-B: identification of specific Chinese air mass tracers B. Barletta1, S. Meinardi1, I. J. Simpson1, E. L. Atlas2, A. J. Beyersdorf3, A. K. Baker4, N. J. Blake1, M. Yang1, J. R. Midyett1, B. J. Novak1, R. J. McKeachie1, H. E. Fuelberg5, G. W. Sachse3, M. A. Avery3, T. Campos6, A. J. Weinheimer6, F. S. Rowland1, and D. R. Blake1 1University of California, Irvine, 531 Rowland Hall, Irvine 92697 CA, USA 2University of Miami, RSMAS/MAC, 4600 Rickenbacker Causeway, Miami, 33149 FL, USA 3NASA Langley Research Center, Hampton, 23681 VA, USA 4Max Plank Institute, Atmospheric Chemistry Dept., Johannes-Joachim-Becherweg 27, 55128 Mainz, Germany 5Florida State University, Department of Meteorology, Tallahassee Florida 32306-4520, USA 6NCAR, 1850 Table Mesa Drive, Boulder, 80305 CO, USA Received: 9 March 2009 – Published in Atmos. Chem. Phys. Discuss.: 24 March 2009 Revised: 16 June 2009 – Accepted: 17 June 2009 – Published: 30 July 2009 Abstract. We present results from the Intercontinental 1 Introduction Chemical Transport Experiment – Phase B (INTEX-B) air- craft mission conducted in spring 2006. By analyzing the The Intercontinental Chemical Transport Experiment – mixing ratios of volatile organic compounds (VOCs) mea- Phase B (INTEX-B) aircraft experiment was conducted in sured during the second part of the field campaign, to- the spring of 2006. Its broad objective was to understand gether with kinematic back trajectories, we were able to the behavior of trace gases and aerosols on transcontinental identify five plumes originating from China, four plumes and intercontinental scales, and their impact on air quality from other Asian regions, and three plumes from the United and climate (an overview of the INTEX-B campaign can be States.
    [Show full text]
  • Investigating Absorption Refrigerator Fires (Part I)
    Orion P. Keifer Peter D. Layson Charles A. Wensley Investigating Absorption Refrigerator Fires (Part I) ATLANTIC BEACH, FLORIDA—In today’s recreational vehicles (RV), the then expels it when perco- most common refrigerator uses absorption refrigeration technology, lated in the boiler. It is this primarily because this type of system can operate on multiple sources action of the water which of power, including propane when electrical power is unavailable. makes the ammonia flow. These refrigerators have been under intense scrutiny in recent years The hydrogen in the re- due to numerous reported fires, apparently starting in the area of the frigeration coil maintains absorption refrigerator. Both the Dometic Corporation and Norcold a positive pressure of ap- Incorporated, two manufacturers of RV refrigerators, have been re- proximately 300-375 PSI quired by the National Highway and Traffic Safety Administration (2.07-2.59 MPa) when (NHTSA) to recall certain models of refrigerators which have been not in operation and, due identified as capable of failing in a fire mode. In summary, the three to its low partial pressure, NHTSA recalls indicate a fatigue crack may develop in the boiler tube promotes the evaporation of the cooling unit which may release sufficient pressurized flammable of the liquid ammonia. It coolant solution into an area where an ignition source is present. The should be noted that unlike NHTSA Recall Campaign ID Numbers are 06E076000 for Dometic conventional refrigeration (926,877 affected units), and 02E019000 (28,144 affected units) and systems which extensively 02E045000 (8,419 affected units) for Norcold. use copper due to its high thermal conductivity, the Applications Engineering Group, Inc.
    [Show full text]
  • Solar Air-Conditioning and Refrigeration - Achievements and Challenges
    Solar air-conditioning and refrigeration - achievements and challenges Hans-Martin Henning Fraunhofer-Institut für Solare Energiesysteme ISE, Freiburg/Germany EuroSun 2010 September 28 – October 2, 2010 Graz - AUSTRIA © Fraunhofer ISE Outline Components and systems Achievements Solar thermal versus PV? Challenges and conclusion © Fraunhofer ISE Components and systems Achievements Solar thermal versus PV? Challenges and conclusion © Fraunhofer ISE Overall approach to energy efficient buildings Assure indoor comfort with a minimum energy demand 1. Reduction of energy demand Building envelope; ventilation 2. Use of heat sinks (sources) in Ground; outside air (T, x) the environment directly or indirectly; storage mass 3. Efficient conversion chains HVAC; combined heat, (minimize exergy losses) (cooling) & power (CH(C)P); networks; auxiliary energy 4. (Fractional) covering of the Solar thermal; PV; (biomass) remaining demand using renewable energies © Fraunhofer ISE Solar thermal cooling - basic principle Basic systems categories Closed cycles (chillers): chilled water Open sorption cycles: direct treatment of fresh air (temperature, humidity) © Fraunhofer ISE Open cycles – desiccant air handling units Solid sorption Liquid sorption Desiccant wheels Packed bed Coated heat exchangers Plate heat exchanger Silica gel or LiCl-matrix, future zeolite LiCl-solution: Thermochemical storage possible ECOS (Fraunhofer ISE) in TASK 38 © Fraunhofer ISE Closed cycles – water chillers or ice production Liquid sorption: Ammonia-water or Water-LiBr (single-effect or double-effect) Solid sorption: silica gel – water, zeolite-water Ejector systems Thermo-mechanical systems Turbo Expander/Compressor AC-Sun, Denmark in TASK 38 © Fraunhofer ISE System overview Driving Collector type System type temperature Low Open cycle: direct air treatment (60-90°C) Closed cycle: high temperature cooling system (e.g.
    [Show full text]
  • Psychrometrics Outline
    Psychrometrics Outline • What is psychrometrics? • Psychrometrics in daily life and food industry • Psychrometric chart – Dry bulb temperature, wet bulb temperature, absolute humidity, relative humidity, specific volume, enthalpy – Dew point temperature • Mixing two streams of air • Heating of air and using it to dry a product 2 Psychrometrics • Psychrometrics is the study of properties of mixtures of air and water vapor • Water vapor – Superheated steam (unsaturated steam) at low pressure – Superheated steam tables are on page 817 of textbook – Properties of dry air are on page 818 of textbook – Psychrometric charts are on page 819 & 820 of textbook • What are these properties of interest and why do we need to know these properties? 3 Psychrometrics in Daily Life • Sea breeze and land breeze – When and why do we get them? • How do thunderstorms, hurricanes, and tornadoes form? • What are dew, fog, mist, and frost and when do they form? • When and why does the windshield of a car fog up? – How do you de-fog it? Is it better to blow hot air or cold air? Why? • Why do you feel dry in a heated room? – Is the moisture content of hot air lower than that of cold air? • How does a fan provide relief from sweating? • How does an air conditioner provide relief from sweating? • When does a soda can “sweat”? • When and why do we “see” our breath? • Do sailboats perform better at high or low relative humidity? Key factors: Temperature, Pressure, and Moisture Content of Air 4 Do Sailboats Perform Better at low or High RH? • Does dry air or moist air provide more thrust against the sail? • Which is denser – humid air or dry air? – Avogadro’s law: At the same temperature and pressure, the no.
    [Show full text]
  • Cryogenicscryogenics Forfor Particleparticle Acceleratorsaccelerators Ph
    CryogenicsCryogenics forfor particleparticle acceleratorsaccelerators Ph. Lebrun CAS Course in General Accelerator Physics Divonne-les-Bains, 23-27 February 2009 Contents • Low temperatures and liquefied gases • Cryogenics in accelerators • Properties of fluids • Heat transfer & thermal insulation • Cryogenic distribution & cooling schemes • Refrigeration & liquefaction Contents • Low temperatures and liquefied gases ••• CryogenicsCryogenicsCryogenics ininin acceleratorsacceleratorsaccelerators ••• PropertiesPropertiesProperties ofofof fluidsfluidsfluids ••• HeatHeatHeat transfertransfertransfer &&& thermalthermalthermal insulationinsulationinsulation ••• CryogenicCryogenicCryogenic distributiondistributiondistribution &&& coolingcoolingcooling schemesschemesschemes ••• RefrigerationRefrigerationRefrigeration &&& liquefactionliquefactionliquefaction • cryogenics, that branch of physics which deals with the production of very low temperatures and their effects on matter Oxford English Dictionary 2nd edition, Oxford University Press (1989) • cryogenics, the science and technology of temperatures below 120 K New International Dictionary of Refrigeration 3rd edition, IIF-IIR Paris (1975) Characteristic temperatures of cryogens Triple point Normal boiling Critical Cryogen [K] point [K] point [K] Methane 90.7 111.6 190.5 Oxygen 54.4 90.2 154.6 Argon 83.8 87.3 150.9 Nitrogen 63.1 77.3 126.2 Neon 24.6 27.1 44.4 Hydrogen 13.8 20.4 33.2 Helium 2.2 (*) 4.2 5.2 (*): λ Point Densification, liquefaction & separation of gases LNG Rocket fuels LIN & LOX 130 000 m3 LNG carrier with double hull Ariane 5 25 t LHY, 130 t LOX Air separation by cryogenic distillation Up to 4500 t/day LOX What is a low temperature? • The entropy of a thermodynamical system in a macrostate corresponding to a multiplicity W of microstates is S = kB ln W • Adding reversibly heat dQ to the system results in a change of its entropy dS with a proportionality factor T T = dQ/dS ⇒ high temperature: heating produces small entropy change ⇒ low temperature: heating produces large entropy change L.
    [Show full text]
  • Refrigerant Selection and Cycle Development for a High Temperature Vapor Compression Heat Pump
    Refrigerant Selection and Cycle Development for a High Temperature Vapor Compression Heat Pump Heinz Moisia*, Renè Riebererb aResearch Assistant, Institute of Thermal Engineering, Graz University of Technology, Inffeldgasse 25/B, 8010 Graz, Austria bAssociate Professor, Institute of Thermal Engineering, Graz University of Technology, Inffeldgasse 25/B, 8010 Graz, Austria Abstract Different technological challenges have to be met in the course of the development of a high temperature vapor compression heat pump. In certain points of operation, high temperature refrigerants can show condensation during the compression which may lead to compressor damage. As a consequence, high suction gas superheat up to 20 K can be necessary. Furthermore high compressor outlet temperatures caused by high heat sink outlet temperatures (approx. 110 °C) and high pressure ratios can lead to problems with the compressor lubricant. In order to meet these challenges different refrigerant and cycle configurations have been investigated by means of simulation. Thermodynamic properties as well as legal and availability aspects have been considered for the refrigerant selection. The focus of the cycle configurations has been set on the realization of the required suction gas superheat. Therefore the possibility of an internal heat exchanger and a suction gas cooled compressor has been investigated. The simulation results showed a COP increase of up to +11 % due to the fact that the main part of the suction gas superheat has not been provided in the evaporator. Furthermore, the effect of increased subcooling has been investigated for a single stage cycle with internal heat exchanger. The results showed a COP of 3.4 with a subcooling of 25 K at a temperature lift of approximately 60 K for the refrigerant R600 (n-butane).
    [Show full text]