Freon™ 22 (R-22) Refrigerant
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Effect of Insulations on Cop in Vapor Compression Refrigeration System
International Journal of Mechanical Engineering and Technology (IJMET) Volume 10, Issue 01, January 2019, pp. 1201-1208, Article ID: IJMET_10_01_122 Available online at http://www.iaeme.com/ijmet/issues.asp?JType=IJMET&VType=10&IType= 01 ISSN Print: 0976-6340 and ISSN Online: 0976-6359 © IAEME Publication Scopus Indexed EFFECT OF INSULATIONS ON COP IN VAPOR COMPRESSION REFRIGERATION SYSTEM Anusha Peyyala Assistant Professor P V P Siddhartha Institute of Technology, Research Scholar, Acharya Nagarjuna University, India. Dr N V V S Sudheer Associate Professor, R V R & J C College of Engineering, Guntur India ABSTRACT In this project, experimentation is done on Vapour Compression Refrigeration System [VCRS] as the COP is high for this system and it is the present trend of the HVAC in the domestic industry. This study presents investigation of best suited refrigerant and insulation combination for gas pipeline and liquid pipeline of a split air conditioning system. Analysis are performed for R22-Chlorodiflouromethane, a HydroChloroFlouro Carbon refrigerant, which has been using in the present world that cause both global warming and ozone layer depletion and R410a, mixture of di- flouromethane and pentaflouroethane, a Hydroflouro carbon refrigerant, which is future of HVAC which reduces the effect of ozone layer depletion [ODP] and Global Warming Potential [GWP].For these two refrigerants, we had found out the best insulation suitable as insulation also affects the COP of air conditioner, which has been observed from the literature. Minimizing the temperature of refrigerant in suction line helps condensing unit work more effectively intern the system performance increases. This reduces the overall power required for working of air conditioner, thereby reducing the maintenance cost of system. -
New and Improved Infrared Absorption Cross Sections for Chlorodifluoromethane (HCFC-22)
Atmos. Meas. Tech., 9, 2593–2601, 2016 www.atmos-meas-tech.net/9/2593/2016/ doi:10.5194/amt-9-2593-2016 © Author(s) 2016. CC Attribution 3.0 License. New and improved infrared absorption cross sections for chlorodifluoromethane (HCFC-22) Jeremy J. Harrison1,2 1Department of Physics and Astronomy, University of Leicester, University Road, Leicester, LE1 7RH, UK 2National Centre for Earth Observation, University of Leicester, University Road, Leicester, LE1 7RH, UK Correspondence to: Jeremy J. Harrison ([email protected]) Received: 10 December 2015 – Published in Atmos. Meas. Tech. Discuss.: 18 January 2016 Revised: 3 May 2016 – Accepted: 6 May 2016 – Published: 17 June 2016 Abstract. The most widely used hydrochlorofluorocarbon 1 Introduction (HCFC) commercially since the 1930s has been chloro- difluoromethane, or HCFC-22, which has the undesirable The consumer appetite for safe household refrigeration led effect of depleting stratospheric ozone. As this molecule to the commercialisation in the 1930s of dichlorodifluo- is currently being phased out under the Montreal Pro- romethane, or CFC-12, a non-flammable and non-toxic re- tocol, monitoring its concentration profiles using infrared frigerant (Myers, 2007). Within the next few decades, other sounders crucially requires accurate laboratory spectroscopic chemically related refrigerants were additionally commer- data. This work describes new high-resolution infrared ab- cialised, including chlorodifluoromethane, or a hydrochlo- sorption cross sections of chlorodifluoromethane over the rofluorocarbon known as HCFC-22, which found use in a spectral range 730–1380 cm−1, determined from spectra wide array of applications such as air conditioners, chillers, recorded using a high-resolution Fourier transform spectrom- and refrigeration for food retail and industrial processes. -
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 -
SAFETY DATA SHEET Chlorodifluoromethane (R 22) Issue Date: 16.01.2013 Version: 1.0 SDS No.: 000010021746 Last Revised Date: 18.06.2015 1/15
SAFETY DATA SHEET Chlorodifluoromethane (R 22) Issue Date: 16.01.2013 Version: 1.0 SDS No.: 000010021746 Last revised date: 18.06.2015 1/15 SECTION 1: Identification of the substance/mixture and of the company/undertaking 1.1 Product identifier Product name: Chlorodifluoromethane (R 22) Trade name: Gasart 503 R22 Additional identification Chemical name: Chlorodifluoromethane Chemical formula: CHClF2 INDEX No. - CAS-No. 75-45-6 EC No. 200-871-9 REACH Registration No. 01-2119517587-31 1.2 Relevant identified uses of the substance or mixture and uses advised against Identified uses: Industrial and professional. Perform risk assessment prior to use. Refrigerant. Using gas alone or in mixtures for the calibration of analysis equipment. Using gas as feedstock in chemical processes. Formulation of mixtures with gas in pressure receptacles. Uses advised against Consumer use. 1.3 Details of the supplier of the safety data sheet Supplier Linde Gas GmbH Telephone: +43 50 4273 Carl-von-Linde-Platz 1 A-4651 Stadl-Paura E-mail: [email protected] 1.4 Emergency telephone number: Emergency number Linde: + 43 50 4273 (during business hours), Poisoning Information Center: +43 1 406 43 43 SDS_AT - 000010021746 SAFETY DATA SHEET Chlorodifluoromethane (R 22) Issue Date: 16.01.2013 Version: 1.0 SDS No.: 000010021746 Last revised date: 18.06.2015 2/15 SECTION 2: Hazards identification 2.1 Classification of the substance or mixture Classification according to Directive 67/548/EEC or 1999/45/EC as amended. N; R59 The full text for all R-phrases is displayed in section 16. Classification according to Regulation (EC) No 1272/2008 as amended. -
UNITED STATES PATENT of FICE 2,640,086 PROCESS for SEPARATING HYDROGEN FLUORIDE from CHLORODFLUORO METHANE Robert H
Patented May 26, 1953 2,640,086 UNITED STATES PATENT of FICE 2,640,086 PROCESS FOR SEPARATING HYDROGEN FLUORIDE FROM CHLORODFLUORO METHANE Robert H. Baldwin, Chadds Ford, Pa., assignor to E. H. du Pont de Nemours and Company, Wi inington, Del, a corporation of Delaware No Drawing. Application December 15, 1951, Serial No. 261,929 9 Claims. (C. 260-653) 2 This invention relates to a process for Sep These objects are accomplished essentially by arating hydrogen fluoride from monochlorodi Subjecting a mixture of hydrogen fluoride and fluoronethane, and more particularly, separat Inonochlorodifluoromethane in the liquid phase ing these components from the reaction mixture to temperatures below 0° C., preferably at about obtained in the fluorination of chloroform with -30° C. to -50° C., at either atmospheric or hydrogen fluoride, Super-atmospheric pressures, together with from In the fluorination of chloroform in the prest about 0.25 mol to about 2.5 mols of chloroform ence Of a Catalyst, a reaction mixture is pro per mol of chlorodifluoronethane contained in duced which consists essentially of HCl, HF, the mixture and separating an upper layer rich CHCIF2, CHCl2F, CHCls, and CHF3. A method O in HF from a lower organic layer. The proceSS of Separating these components is disclosed in is operative with mixtures containing up to 77% U. S. Patent No. 2,450,414 which involves sep by weight of HF. arating the components by a special fractional It has been found that chloroform is substan distillation under appropriate temperatures and tially immiscible With EIF at temperatures be pressures. -
(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. -
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). -
CYCLE D-HX: NIST Vapor Compression Cycle Model Accounting for Refrigerant Thermodynamic and Transport Properties
NIST Technical Note 1974 CYCLE_D-HX: NIST Vapor Compression Cycle Model Accounting for Refrigerant Thermodynamic and Transport Properties Version 1.0 User’s Guide J.S. Brown R. Brignoli P.A. Domanski This publication is available free of charge from: https://doi.org/10.6028/NIST.TN.1974 NIST Technical Note 1974 CYCLE_D-HX: NIST Vapor Compression Cycle Model Accounting for Refrigerant Thermodynamic and Transport Properties Version 1.0 User’s Guide J.S. Brown The Catholic University of America R. Brignoli P.A. Domanski Engineering Laboratory National Institute of Standards and Technology This publication is available free of charge from: https://doi.org/10.6028/NIST.TN.1974 December 2017 U.S. Department of Commerce Wilbur L. Ross, Jr., Secretary National Institute of Standards and Technology Walter Copan, NIST Director and Under Secretary of Commerce for Standards and Technology This software package was developed by the National Institute of Standards and Technology (NIST), is not subject to copyright protection, and is in the public domain. It can be used freely provided that any derivative works bear some notice that they are derived from it. NIST used its best efforts to provide a high-quality software package and to select modeling methods and correlations based on sound scientific judgement. However, NIST assumes neither responsibility nor liability for any damage arising out of or relating to the use of CYCLE_D-HX. The software is provided “AS IS”; NIST makes NO GUARANTIES and NO WARRANTIES OF ANY TYPE, expressed or implied, including NO WARRANTY OF MERCHANTABILITY OR FITNESS FOR A PARTICULAR PURPOSE. -
Factors Affecting Indoor Air Quality
Factors Affecting Indoor Air Quality The indoor environment in any building the categories that follow. The examples is a result of the interaction between the given for each category are not intended to site, climate, building system (original be a complete list. 2 design and later modifications in the Sources Outside Building structure and mechanical systems), con- struction techniques, contaminant sources Contaminated outdoor air (building materials and furnishings, n pollen, dust, fungal spores moisture, processes and activities within the n industrial pollutants building, and outdoor sources), and n general vehicle exhaust building occupants. Emissions from nearby sources The following four elements are involved n exhaust from vehicles on nearby roads Four elements— in the development of indoor air quality or in parking lots, or garages sources, the HVAC n loading docks problems: system, pollutant n odors from dumpsters Source: there is a source of contamination pathways, and or discomfort indoors, outdoors, or within n re-entrained (drawn back into the occupants—are the mechanical systems of the building. building) exhaust from the building itself or from neighboring buildings involved in the HVAC: the HVAC system is not able to n unsanitary debris near the outdoor air development of IAQ control existing air contaminants and ensure intake thermal comfort (temperature and humidity problems. conditions that are comfortable for most Soil gas occupants). n radon n leakage from underground fuel tanks Pathways: one or more pollutant pathways n contaminants from previous uses of the connect the pollutant source to the occu- site (e.g., landfills) pants and a driving force exists to move n pesticides pollutants along the pathway(s). -
Liquefied Gas Conversion Chart
LIQUEFIED GAS CONVERSION CHART Cubic Feet / Pound Pounds / Gallon Product Name Column A Column B Acetylene UN/NA: 1001 14.70 4.90 CAS: 514-86-2 Air UN/NA: 1002 13.30 7.29 CAS: N/A Ammonia Anhydrous UN/NA: 1005 20.78 5.147 CAS: 7664-41-7 Argon UN/NA: 1006 9.71 11.63 CAS: 7440-37-1 Butane UN/NA: 1075 6.34 4.86 CAS: 106-97-8 Carbon Dioxide UN/NA: 2187 8.74 8.46 CAS: 124-38-9 Chlorine UN/NA: 1017 5.38 11.73 CAS: 7782-50-5 Ethane UN/NA: 1045 12.51 2.74 CAS: 74-84-0 Ethylene Oxide UN/NA: 1040 8.78 7.25 CAS: 75-21-8 Fluorine UN/NA: 1045 10.17 12.60 CAS: 7782-41-4 Helium UN/NA: 1046 97.09 1.043 CAS: 7440-59-7 Hydrogen UN/NA: 1049 192.00 0.592 CAS: 1333-74-0 1. Find the gas you want to convert. 2. If you know your quantity in cubic feet and want to convert to pounds, divide your amount by column A 3. If you know your quantity in gallons and want to convert to pounds, multiply your amount by column B 4. If you know your quantity in pounds and want to convert to gallons, divide your amount by column B If you have any questions, please call 1-800-433-2288 LIQUEFIED GAS CONVERSION CHART Cubic Feet / Pound Pounds / Gallon Product Name Column A Column B Hydrogen Chloride UN/NA: 1050 10.60 8.35 CAS: 7647-01-0 Krypton UN/NA: 1056 4.60 20.15 CAS: 7439-90-9 Methane UN/NA: 1971 23.61 3.55 CAS: 74-82-8 Methyl Bromide UN/NA: 1062 4.03 5.37 CAS: 74-83-9 Neon UN/NA: 1065 19.18 10.07 CAS: 7440-01-9 Mapp Gas UN/NA: 1060 9.20 4.80 CAS: N/A Nitrogen UN/NA: 1066 13.89 6.75 CAS: 7727-37-9 Nitrous Oxide UN/NA: 1070 8.73 6.45 CAS: 10024-97-2 Oxygen UN/NA: 1072 12.05 9.52 CAS: 7782-44-7 Propane UN/NA: 1075 8.45 4.22 CAS: 74-98-6 Sulfur Dioxide UN/NA: 1079 5.94 12.0 CAS: 7446-09-5 Xenon UN/NA: 2036 2.93 25.51 CAS: 7440-63-3 1. -
Refrigerants and the Refrigeration System
M25_STAN0893_00_SE_C25.QXD 9/4/08 9:54 PM Page 1 SECTION FOUR Refrigerants and the Refrigeration System UNIT 25 Accessing Sealed Refrigeration Systems OBJECTIVES determine the pressures. Knowing the temperature differ- ence across the coils, the amperage, and the airflow all give After completing this unit you will be able to: the technician vital information; but sometimes without the system operating pressures a final determination of a prob- ■ describe the different types of refrigeration service lem cannot be accurately made. valves. It is important to attach and remove a gauge manifold ■ explain the operation of gauge manifold valves. ■ explain how to properly install and remove a gauge set properly. Understanding how to properly manipulate sys- manifold set on manual service valves. tem access valves and install gauge manifolds is vital to the ■ explain the operation of split system installation personal safety of the service technician. Improper technique valves. can damage the system or injure the technician. Proper tech- ■ explain how to properly install and remove a gauge niques should always be practiced so that they become a manifold set on Schrader valves. habit performed the same way each time. ■ describe how to gain access to systems without service valves. SAFETY TIP 25.1 INTRODUCTION One of the last things a service technician should do when The proper personal protective equipment, PPE, for in- troubleshooting a system is attach a set of gauges to the sys- stalling refrigeration gauges and manipulating valves includes safety glasses and gloves. When liquid refrig- tem. Each time a sealed system is accessed there is a chance erant escapes into the atmosphere it boils at ex- that some contaminants can be introduced to the system, or tremely cold temperatures. -
R-22 Safety Data Sheet
R-22 Safety Data Sheet R-22 1. CHEMICAL PRODUCT AND COMPANY IDENTIFICATION PRODUCT NAME: R-22 OTHER NAME: Chlorodifluoromethane USE: Refrigerant Gas DISTRIBUTOR: National Refrigerants, Inc. 661 Kenyon Avenue Bridgeton, New Jersey 08302 FOR MORE INFORMATION CALL: IN CASE OF EMERGENCY CALL: (Monday-Friday, 8:00am-5:00pm) CHEMTREC: 1-800-424-9300 1-800-262-0012 2. HAZARDS IDENTIFICATION CLASSIFICATION: Gases under pressure, Liquefied Gas SIGNAL WORD: WARNING HAZARD STATEMENT: Contains gas under pressure, may explode if heated SYMBOL: Gas Cylinder PRECAUTIONARY STATEMENT: STORAGE: Protect from sunlight, store in a well ventilated place EMERGENCY OVERVIEW: Colorless, volatile liquid with ethereal and faint sweetish odor. Non-flammable material. Overexposure may cause dizziness and loss of concentration. At higher levels, CNS depression and cardiac arrhythmia may result from exposure. Vapors displace air and can cause asphyxiation in confined spaces. At higher temperatures, (>250C), decomposition products may include Hydrochloric Acid (HCI), Hydrofluoric Acid (HF) and carbonyl halides. POTENTIAL HEALTH HAZARDS SKIN: Irritation would result from a defatting action on tissue. Liquid contact could cause frostbite. EYES: Liquid contact can cause severe irritation and frostbite. Mist may irritate. INHALATION: R-22 is low in acute toxicity in animals. When oxygen levels in air are reduced to 12-14% by displacement, symptoms of asphyxiation, loss of coordination, increased pulse rate and deeper respiration will occur. At high levels, cardiac arrhythmia may occur. INGESTION: Ingestion is unlikely because of the low boiling point of the material. Should it occur, discomfort in the gastrointestinal tract from rapid evaporation of the material and consequent evolution of gas would result.