Physical Property Data Sheet SI Units
|
|
- Silvia Bailey
- 5 years ago
- Views:
Transcription
1 Physical Property Data Sheet SI Units
2 PHYSICAL PROPERTY DATA FOR KLEA 407C PROPERTY UNITS VALUE Bubble Point (1 atm) C Dew Point (1atm) C Bubble Point Pressure (25 C) bara 11.9 Estimated Critical Temperature C 86 Latent Heat of Vaporisation (Tm=25 C) kj/kg Trouton s constant kj/kg.k 1.08 Coeff.Vol.Therm.Exp. (LIQ,0-20 C) K Density (SAT VAPOUR) at 1 atm kg/m EQUATION OF STATE (MARTIN-HOU) P r = XT r + Σ (A i + B i T r +C i exp (-KT r )) V r -B i=1, 4 (V r -B) (i+1) Where : T r = T/T c, P r = P/P c, V r = V/V c = V x RHO c X = K = T c, P c, RHO c = 359.2(K), 46.52(bara), 490(kg/m 3 ) A 1, B 1, C 1 = , , A 2, B 2, C 2 = , , A 3, B 3, C 3 = , 0.0, 0.0 A 4, B 4, C 4 = , 0.0, Applicable range: bara, 0-100K superheat. SATURATION ENVELOPE BUBBLE POINT TEMPERATURES Bubble Point Temperature (T b ) = A + BX + CX 2 + DX T b = Bubble point temperature in K X = Ln(P) P = pressure in bara
3 SATURATION ENVELOPE DEW POINT TEMPERATURES Dew Point Temperature (T d ) = A + BX + CX 2 + DX T d = Dew point temperature in K X = Ln(P) P = pressure in bara SATURATION ENVELOPE MID POINT TEMPERATURES Mid Point Temperature (T m ) = A + BX + CX 2 + DX T m = Average of Dew & Bubble point temperatures in K X = Ln(P) P = pressure in bara LATENT HEAT OF VAPORISATION DH vap = A + Bx + Cx 2 + Dx 3 + Ex 4 Where x = (1-(T m /T c )) (1/3) T m = Mid point temperature K T c = Critical Temperature K T c = 359.2K DH vap = kj/kg E = IDEAL GAS HEAT CAPACITY C p (ideal) = A + BT + CT 2 + D/T E T = Temperature K C p (ideal) kj/kg.k
4 SATURATED LIQUID ENTHALPY H liq = A + Bx + Cx 2 + Dx 3 + Ex 4 where x = (1- (T b /T c )) (1/3) E = T b T c = Bubble point temperature K = Critical Temperature K T c = K H liq kj/kg LIQUID DENSITY d liq = A + Bx + Cx 2 + Dx 3 + Ex 4 where x = (1- (T b /T c )) (1/3) E = T b = Bubble point temperature K T c = Critical Temperature K T c = K d liq kg/m 3 LIQUID VISCOSITY Ln (µ liq ) = A + B/T m + CT m + DT 2 m E-5 T m = Mid point temperature K µ liq cp LIQUID THERMAL CONDUCTIVITY K liq = A + BT m + CT m 2 + DT m E T K liq = Mid point temperature K W/m K
5 SATURATED VAPOUR DENSITY d vap = A + Bx + Cx 2 + Dx 3 + Ex 4 where x = (1- (T d /T c )) (1/3) E = T d = Dew point temperature K T c = Critical Temperature K T c = K d vap kg/m 3 VAPOUR VISCOSITY (IDEAL VAPOUR) µ vap = A + BT + CT E E-8 T m = Temperature K µ vap cp VAPOUR VISCOSITY (SATURATED VAPOUR) µ vap = A + BT d + CT d 2 + D/T d E E T d = Dew point temperature K µ vap cp VAPOUR THERMAL CONDUCTIVITY (IDEAL VAPOUR) K gas = A + BT + CT E E E-8 T d K gas = Temperature K W/m.K
6 SATURATED VAPOUR THERMAL CONDUCTIVITY K gas = A + BT d + CT d 2 + D/T d E E T d K gas = Dew point temperature K W/m.K SPEED OF SOUND (SATURATED VAPOUR) µ vap = A + BT d + CT d 2 + D/T d E T d = Dew point temperature K µ vap = m/s SATURATION ENVELOPE PRESSURE TEMPERATURES ( C) Bara BUB pnt MID pnt DEW pnt
7 LIQUID PROPERTIES TEMP LIQUID LIQUID LATENT LIQUID LIQ.THERM DENSITY ENTH HEAT VISCOSITY COND C kg/m 3 kj/kg kj/kg cp W/m.K For Liquid Density and Liquid Enthalpy the bubble point temperatures are used. For Latent Heat, Liquid Viscosity and Liquid Thermal Conductivity mid point temperatures are used. IDEAL GAS PROPERTIES TEMP ID. GAS ID. GAS ID. GAS Cp VISCOSITY THERM COND C kj/kg.k cp W/m.K
8 SATURATED VAPOUR PROPERTIES TEMP SAT VAP SAT VAP SAT VAP SPEED DENSITY VISCOSITY THERM COND OF SOUND C kg/m 3 cp W/m.K m/s The temperatures used are Dew Point Temperatures.
9 Mexichem UK Limited, The Heath Business and Technical Park, Runcorn, Cheshire, WA7 4QX Telephone: +44 (0) Information contained in this publication, or as otherwise supplied to the Users is believed to be accurate and given in good faith, but it is for the User to satisfy itself of the suitability for its own particular purpose. Mexichem Fluor gives no warranty as to the fitness of the Product for any particular purpose and any implied warranty or condition (statutory or otherwise) is excluded except to the extent that such exclusion is prevented by law. Mexichem Fluor accepts no liability for loss or damage (other than that arising from death or personal injury caused by defective product, if proved), resulting from reliance on this information. Freedom under Patent, Copyright and Design cannot be assumed. KLEA and Mexichem Fluor are trademarks of Mexichem SAB de C.V. Mexichem Fluor All rights reserved. Not to be reproduced without the consent of the copyright owner.
Physical Property Data Sheet SI Units
Physical Property Data Sheet SI Units PHYSICAL PROPERTY DATA FOR KLEA 58 PROPERTY UNITS VALUE Bubble Point (1 atm) C -85.69 Dew Point (1 atm) C -85.68 Bubble Point Pressure (-4 C) bara 8.2 Estimated Critical
More informationKlea 407A Data Sheet SI Units
Klea 407A Data Sheet SI Units Physical Property Data for Klea 407A Property Units Value Bubble Point 1 (atm) C -45.5 Dew Point (1atm) C -38.9 Bubble Point Pressure (25 C) bara 12.6 Estimated Critical Temperature
More informationPhysical Property Data Sheet British Units
Physical Property Data Sheet British Units KLEA 407A Data Sheet KLEA 407A is a blend of HFCs 32, 125 and 134a designed for low-temperature applications in new refrigeration equipment and also for retrofit
More informationBoiling Point at One Atmosphere F Critical Temperature F
Opteon XP40 Refrigerant Transport Properties of Opteon XP40 Engineering (I/P) Units Physical Properties Molecular Weight 87.2 g/mol Boiling Point at One Atmosphere - 50.8 F Critical Temperature 178.7 F
More informationThermodynamics I Chapter 2 Properties of Pure Substances
Thermodynamics I Chapter 2 Properties of Pure Substances Mohsin Mohd Sies Fakulti Kejuruteraan Mekanikal, Universiti Teknologi Malaysia Properties of Pure Substances (Motivation) To quantify the changes
More informationME Thermodynamics I
HW-22 (25 points) Given: 1 A gas power cycle with initial properties as listed on the EFD. The compressor pressure ratio is 25:1 Find: 1 Sketch all the processes on a p-h diagram and calculate the enthalpy,
More informationM. Conde Engineering Eugen-Huber-Strasse 61 CH-8048 Zurich SWITZERLAND
M. Conde Engineering Eugen-Huber-Strasse 61 CH-8048 Zurich SWITZERLAND BRIEF DOCUMENTATION ON THE MATHCAD CALCULATION SHEET MOIST AIR WEBPROPS.MCD The nine attached pages show what the user of the calculation
More informationSolkane 410 Thermodynamics
SOLVAY FLUOR SOLKANE - INFORMATION SERVICE Solkane 410 Thermodynamics SOLVAY FLUOR Technical Service - Refrigerants - Product Bulletin no.: T/09.04/04/E P.O. Box 0 Phone +49/511/857-653 3000 Hannover Fax
More information2-412 PHYSICAL AND CHEMICAL DATA
2-412 PHYSICAL AND CHEMICAL DATA TABLE 2-304 Saturated Solid/Vapor Water* Volume, Enthalpy, Entropy, Temp., Pressure, ft 3 /lb Btu/lb Btu/(lb)( F) F lb/in 2 abs. Solid Vapor Solid Vapor Solid Vapor 160
More informationBoiling Point at One Atmosphere F Critical Temperature F
Opteon XP44 Refrigerant Transport Properties of Opteon XP44 (R-452A) Engineering (I/P) Units Physical Properties Molecular Weight 103.5 lb/lb-mole Boiling Point at One Atmosphere -52.7 F Critical Temperature
More informationMODULE TITLE : MASS AND ENERGY BALANCE TOPIC TITLE : ENERGY BALANCE TUTOR MARKED ASSIGNMENT 3
THIS BOX MUST BE COMPLETED Student Code No.... Student's Signature... Date Submitted... Contact e-mail... MODULE TITLE : MASS AND ENERGY BALANCE TOPIC TITLE : ENERGY BALANCE TUTOR MARKED ASSIGNMENT 3 NAME...
More informationLevel 7 Post Graduate Diploma in Engineering Heat and mass transfer
9210-221 Level 7 Post Graduate Diploma in Engineering Heat and mass transfer 0 You should have the following for this examination one answer book non programmable calculator pen, pencil, drawing instruments
More informationSL Series 85 SMD Ecap
Features: Designed for surface mounting on high density PC board Supplied with carrier taping for automatic mounting machine Guarantees 2,000 hours at 85 C Specifications Item Operating Temperature Range
More informationME 201 Thermodynamics
Spring 01 ME 01 Thermodynamics Property Evaluation Practice Problems II Solutions 1. Air at 100 K and 1 MPa goes to MPa isenthapically. Determine the entropy change. Substance Type: Ideal Gas (air) Process:
More informationChapter 3 PROPERTIES OF PURE SUBSTANCES SUMMARY
Chapter 3 PROPERTIES OF PURE SUBSTANCES SUMMARY PURE SUBSTANCE Pure substance: A substance that has a fixed chemical composition throughout. Compressed liquid (sub-cooled liquid): A substance that it is
More informationTernary Maps for Liquid-Liquid Equilibrium Illustration with Aspen Plus V8.0
Ternary Maps for Liquid-Liquid Equilibrium Illustration with Aspen Plus V8.0 Ethanol-Water-Cyclohexane System 1. Lesson Objectives Learn how to generate ternary maps in Aspen Plus for systems with two
More informationReview of Mathematics
Review for Exam #1 Review of Mathematics 2 Weighted Mean A certain property of material 1 is P 1 and that of material 2 is P 2 If x 1 amount (weight or volume) of material 1 is mixed with x 2 amount of
More informationThermodynamics Introduction and Basic Concepts
Thermodynamics Introduction and Basic Concepts by Asst. Prof. Channarong Asavatesanupap Mechanical Engineering Department Faculty of Engineering Thammasat University 2 What is Thermodynamics? Thermodynamics
More informationSub -T g Relaxation in Thin Glass
Sub -T g Relaxation in Thin Glass Prabhat Gupta The Ohio State University ( Go Bucks! ) Kyoto (January 7, 2008) 2008/01/07 PK Gupta(Kyoto) 1 Outline 1. Phenomenology (Review). A. Liquid to Glass Transition
More informationPure Substances Phase Change, Property Tables and Diagrams
Pure Substances Phase Change, Property Tables and Diagrams In this chapter we consider the property values and relationships of a pure substance (such as water) which can exist in three phases - solid,
More informationSupporting Information: On Localized Vapor Pressure Gradients Governing Condensation and Frost Phenomena
Supporting Information: On Localized Vapor Pressure Gradients Governing Condensation and Frost Phenomena Saurabh Nath and Jonathan B. Boreyko Department of Biomedical Engineering and Mechanics, Virginia
More informationEngineering Thermodynamics
David Ng Summer 2017 Contents 1 July 5, 2017 3 1.1 Thermodynamics................................ 3 2 July 7, 2017 3 2.1 Properties.................................... 3 3 July 10, 2017 4 3.1 Systems.....................................
More information0 o C. H vap. H evap
Solution. Energy P (00 ) Pν x 0 5 ρ 850,4 J kg - J kg Power kg s 000,4 600 70 W Solution. 00 o C H evap H vap 0 o C H liq 00 t H liq (4. x0 t ) dt 4.t x0 0 40 0 40 kj kg - H evap 40,68 J mol - (From Appendix
More informationDistinguish between. and non-thermal energy sources.
Distinguish between System & Surroundings We also distinguish between thermal We also distinguish between thermal and non-thermal energy sources. P Work The gas in the cylinder is the system How much work
More informationChapter 3 First Law of Thermodynamics and Energy Equation
Fundamentals of Thermodynamics Chapter 3 First Law of Thermodynamics and Energy Equation Prof. Siyoung Jeong Thermodynamics I MEE0-0 Spring 04 Thermal Engineering Lab. 3. The energy equation Thermal Engineering
More informationReview for Exam #1. Review of Mathematics. Weighted Mean
Review for Exam #1 Review of Mathematics Weighted Mean A certain property of material 1 is P 1 and that of material is P If x 1 amount (weight or volume) of material 1 is mixed with x amount of material,
More informationReview of Mathematics
Review for Exam #1 Review of Mathematics 2 Weighted Mean A certain property of material 1 is P 1 and that of material 2 is P 2 If x 1 amount (weight or volume) of material 1 is mixed with x 2 amount of
More informationSTP-TS THERMOPHYSICAL PROPERTIES OF WORKING GASES USED IN WORKING GAS TURBINE APPLICATIONS
THERMOPHYSICAL PROPERTIES OF WORKING GASES USED IN WORKING GAS TURBINE APPLICATIONS THERMOPHYSICAL PROPERTIES OF WORKING GASES USED IN GAS TURBINE APPLICATIONS Prepared by: ASME Standards Technology, LLC
More informationINTEGRATED CIRCUITS. 74LVC138A 3-to-8 line decoder/demultiplexer; inverting. Product specification 1998 Apr 28
INTEGRATED CIRCUITS -to-8 line decoder/demultiplexer; inverting 998 Apr 8 FEATURES Wide supply voltage range of. to. V In accordance with JEDEC standard no. 8-A Inputs accept voltages up to. V CMOS lower
More informationModified Transient Plane Source (MTPS): Theory of Operation
Pg of 0 Modified Transient Plane Source (MTPS): Theory of Operation The C-Therm TCi Thermal Conductivity Analyzer is based on the Modified Transient Plane Source (MTPS) technique. It employs a one-sided,
More informationName: Discussion Section:
CBE 141: Chemical Engineering Thermodynamics, Spring 2018, UC Berkeley Midterm 2 March 22, 2018 Time: 80 minutes, closed-book and closed-notes, one-sided 8 ½ x 11 equation sheet allowed Please show all
More informationSensible Heat and Enthalpy Calculations
Sensible Heat and Enthalpy Calculations Sensible Heat - The amount of heat that must be added when a substance undergoes a change in temperature from 298 K to an elevated temperature without a change in
More informationSolkane 134a Thermodynamics
SOLVAY FLUOR SOLKANE - INFORMATION SERVICE Solkane 134a Thermodynamics SOLVAY FLUOR Technical Service - Refrigerants - PRODUCT BULLETIN NO.: T/09.04/01/E P.O. Box 220 Phone +49/511/857-2653 30002 Hannover
More informationIAPWS-IF97 Water and Steam Properties DEMO VERSION USER GUIDE. Copyright Fluidika Techlabs S de RL de CV. All Rights Reserved.
IAPWS-IF97 Water and Steam Properties Excel Add-In Library DEMO VERSION USER GUIDE Windows Operating System SI and I-P Units Version 2.0 Copyright 2015-2019 Fluidika Techlabs S de RL de CV. All Rights
More informationFUNDAMENTALS of Thermodynamics
SOLUTION MANUAL SI UNIT PROBLEMS CHAPTER 15 SONNTAG BORGNAKKE VAN WYLEN FUNDAMENTALS of Thermodynamics Sixth Edition CONTENT SUBSECTION PROB NO. Correspondence table Concept-Study Guide Problems 1-20 Equilibrium
More informationWater and Steam Properties USER GUIDE
IAPWS-IF97 Water and Steam Properties Excel Add-In Library USER GUIDE Windows Operating System SI and I-P Units Version 2.0 Copyright 2015-2019 Fluidika Techlabs S de RL de CV. All Rights Reserved. Table
More information3.5. Kinetic Approach for Isotherms
We have arrived isotherm equations which describe adsorption from the two dimensional equation of state via the Gibbs equation (with a saturation limit usually associated with monolayer coverage). The
More informationEVALUATING PROPERTIES FOR A PURE SUBSTANCES. By Ertanto Vetra
EVALUATING PROPERTIES FOR A PURE SUBSTANCES 1 By Ertanto Vetra Outlines - TV, PV, PT, PVT Diagram - Property Tables - Introduction to Enthalpy - Reference State & Reference Values - Ideal Gas Equation
More informationHeat-storage ORC System of Vehicle ICE Exhaust Heat Recovery with the Capacity of Reducing Heat Fluctuation
Heat-storage ORC System of Vehicle ICE Exhaust Heat Recovery with the Capacity of Reducing Heat Fluctuation Tao CHEN, Lei ZHANG, Weilin ZHUGE, Yangjun ZHANG State Key Laboratory of Automotive Safety and
More informationChapter 6. Heat capacity, enthalpy, & entropy
Chapter 6 Heat capacity, enthalpy, & entropy 1 6.1 Introduction In this lecture, we examine the heat capacity as a function of temperature, compute the enthalpy, entropy, and Gibbs free energy, as functions
More informationINSTITUTO DE INGENIERÍA ENERGÉTICA. (Institute for Energy Engineering) Research Publications
INSTITUTO DE INGENIERÍA ENERGÉTICA UNIVERSIDAD POLITÉCNICA DE VALENCIA CPI, Edificio 8E, Cubo F, 5ª planta, Camino de Vera s/n, 46022 Valencia, Spain Tel. (34) 963877270, Fax (34) 963877272, Email: energeti@upvnet.upv.es
More informationLecture Ch. 6. Condensed (Liquid) Water. Cloud in a Jar Demonstration. How does saturation occur? Saturation of Moist Air. Saturation of Moist Air
Lecture Ch. 6 Saturation of moist air Relationship between humidity and dewpoint Clausius-Clapeyron equation Dewpoint Temperature Depression Isobaric cooling Moist adiabatic ascent of air Equivalent temperature
More informationSEM-2017(03HI MECHANICAL ENGINEERING. Paper II. Please read each of the following instructions carefully before attempting questions.
We RoU No. 700095 Candidate should write his/her Roll No. here. Total No. of Questions : 7 No. of Printed Pages : 7 SEM-2017(03HI MECHANICAL ENGINEERING Paper II Time ; 3 Hours ] [ Total Marks : 0 Instructions
More informationFluorocarbon C3F8 Properties. Table of Contents
Fluorocarbon C3F8 Properties (octafluoropropane R218) Table of Contents 1. C3F8... 2 1.1 Saturation line curve for C 3 F 8...3 1.2 logp-h diagram for C 3 F 8...4 1.3 Extended logp-h diagram for C 3 F 8...5
More informationThermodynamics SCQF Level 9, PHYS Wednesday 9th May, :30-16:30
College of Science and Engineering School of Physics & Astronomy H T O F E E U D N I I N V E B R U S I R T Y H G Thermodynamics SCQF Level 9, PHYS09021 Wednesday 9th May, 2012 14:30-16:30 Chairman of Examiners
More informationSILICA CATALYSTS High Performance Polyolefin Catalysts & Supports
SILICA CATALYSTS High Performance Polyolefin Catalysts & Supports High Performance Polyolefin Catalysts & Supports World class catalysts & supports designed to give exceptional performance within the polyolefin
More informationAppendix F. Steam Tables
Appendix F Steam Tables F.1 INTERPOLATION When a value is required from a table at conditions which lie between listed values, interpolation is necessary. If M, the quantity sought, is a function of a
More informationLECTURE 4 Variation of enthalpy with temperature
LECTURE 4 Variation of enthalpy with temperature So far, we can only work at 25 C. Like c v we define a constant pressure heat capacity, c p, as the amount of heat energy needed to raise the temperature
More informationExam 4 SCORE. MA 114 Exam 4 Spring Section and/or TA:
Exam 4 Name: Section and/or TA: Last Four Digits of Student ID: Do not remove this answer page you will return the whole exam. You will be allowed two hours to complete this test. No books or notes may
More informationThermodynamic behaviour of mixtures containing CO 2. A molecular simulation study
Thermodynamic behaviour of mixtures containing. A molecular simulation study V. Lachet, C. Nieto-Draghi, B. Creton (IFPEN) Å. Ervik, G. Skaugen, Ø. Wilhelmsen, M. Hammer (SINTEF) Introduction quality issues
More informationUSER GUIDE. IAPWS-IF97 Water and Steam Properties. MATLAB Functions Library. Windows Operating System SI and I-P Units Version 2.0
IAPWS-IF97 Water and Steam Properties MATLAB Functions Library USER GUIDE Windows Operating System SI and I-P Units Version 2.0 Copyright 2015-2019 Fluidika Techlabs S de RL de CV. All Rights Reserved.
More informationEsterification in CSTRs in Series with Aspen Plus V8.0
Esterification in CSTRs in Series with Aspen Plus V8.0 1. Lesson Objectives Use Aspen Plus to determine whether a given reaction is technically feasible using three continuous stirred tank reactors in
More information2326 Problem Sheet 1. Solutions 1. First Order Differential Equations. Question 1: Solve the following, given an explicit solution if possible:
2326 Problem Sheet. Solutions First Order Differential Equations Question : Solve the following, given an explicit solution if possible:. 2 x = 4x3, () = 3, ( ) The given equation is a first order linear
More informationWORKBOOK FOR CHEMICAL REACTOR RELIEF SYSTEM SIZING ANNEX 10 NOMENCLATURE A cross-sectional flow area of relief system (m 2 ) A actual actual cross-sectional area of safety valve nozzle (m 2 ) A approx
More informationSteamTablesIIE: An ActiveX to Calculate the Thermodynamic Properties of Water
Proceedings World Geothermal Congress 2010 Bali, Indonesia, 25-29 April 2010 SteamTablesIIE: An ActiveX to Calculate the Thermodynamic Properties of Water Mahendra P. Verma Geotermia, Instituto de Investigaciones
More informationUniversity of Rome Tor Vergata
University of Rome Tor Vergata Faculty of Engineering Department of Industrial Engineering THERMODYNAMIC AND HEAT TRANSFER HEAT TRANSFER dr. G. Bovesecchi gianluigi.bovesecchi@gmail.com 06-7259-727 (7249)
More informationAppendix A Physical and Critical Properties
Appendix A Physical and Critical Properties Table A1 Physical properties of various organic and inorganic substances Compound Formula MW Sp Gr T m (K) T b (K) DH v (kj/kg) DH m (kj/kg) Air 28.97 Ammonia
More informationSensible Heat and Enthalpy Calculations
* Sensible Heat and Enthalpy Calculations Sensible Heat - The amount of heat that must be added when a substance undergoes a change in temperature from 298 K to an elevated temperature without a change
More informationTHERMODYNAMICS, FLUID AND PLANT PROCESSES. The tutorials are drawn from other subjects so the solutions are identified by the appropriate tutorial.
THERMODYNAMICS, FLUID AND PLANT PROCESSES The tutorials are drawn from other subjects so the solutions are identified by the appropriate tutorial. THERMODYNAMICS TUTORIAL 1 LIQUIDS VAPOURS - GASES SAE
More informationIn data sheets and application notes which still contain NXP or Philips Semiconductors references, use the references to Nexperia, as shown below.
Important notice Dear Customer, On 7 February 217 the former NXP Standard Product business became a new company with the tradename Nexperia. Nexperia is an industry leading supplier of Discrete, Logic
More informationSIMULINK MODEL FOR A HEAT-EXCHANGER
The 3rd International Conference on Computational Mechanics and Virtual Engineering COMEC 2009 29 30 OCTOBER 2009, Brasov, Romania SIMULINK MODEL FOR A HEAT-EXCHANGER L. Costiuc 1, V. Popa 2 1 TRANSILVANIA
More informationA User-Friendly Software for Computations of Vapor Compression Cycles with Pure Fluids and Zeotropic Mixtures
Purdue University Purdue e-pubs International Refrigeration and Air Conditioning Conference School of Mechanical Engineering 1996 A User-Friendly Software for Computations of Vapor Compression Cycles with
More informationName: Discussion Section:
CBE 141: Chemical Engineering Thermodynamics, Spring 2018, UC Berkeley Midterm 2 March 22, 2018 Time: 80 minutes, closed-book and closed-notes, one-sided 8 ½ x 11 equation sheet allowed Please show all
More informationIAPWS-IF97 Water and Steam Properties. MATLAB Functions Library DEMO VERSION USER GUIDE
IAPWS-IF97 Water and Steam Properties MATLAB Functions Library DEMO VERSION USER GUIDE Windows Operating System SI and I-P Units Version 2.0 Copyright 2015-2019 Fluidika Techlabs S de RL de CV. All Rights
More informationCB Series Tantalum Capacitor
Features: Lead-Free Specially designed of general purpose Highly reliable resin dipped type Excellent frequency and temperature characteristics Non-flammable epoxy resin Technical Specifications: Item
More informationSolenoid valve Types CSV 2 - CSV 22 (NC) and solenoid coil
Data sheet Solenoid valve s CSV 2 - CSV 22 (NC) and solenoid coil CSV is a direct or servo-operated solenoid valve for liquid, suction, and hot gas lines with fluorinated refrigerants. CSV valves are for
More informationDESIGN OF A SHELL AND TUBE HEAT EXCHANGER
DESIGN OF A SHELL AND TUBE HEAT EXCHANGER Swarnotpal Kashyap Department of Chemical Engineering, IIT Guwahati, Assam, India 781039 ABSTRACT Often, in process industries the feed stream has to be preheated
More informationLecture 3: DESIGN CONSIDERATION OF DRIERS
Lecture 3: DESIGN CONSIDERATION OF DRIERS 8. DESIGN OF DRYER Design of a rotary dryer only on the basis of fundamental principle is very difficult. Few of correlations that are available for design may
More informationAECQ MLCC. Automotive Capacitors Qualified to AEC-Q200. Dimensions Table. Page <1> 07/01/11 V1.1. L (mm) W (mm) Thickness (mm)/symbol Remark M B (mm)
Automotive Capacitors Qualified to AEC-Q200 Dimensions Table L W Thickness /Symbol Remark M B 0402 (1005) 1.00±0.05 0.50±0.05 0.50±0.05 N # 0.25 +0.05/-0.10 0603 (1608) 1.60±0.20 0.80±0.10 0.80±0.07 S
More informationC-Therm TCi Principles of Operation Introduction
Fax: (506) 454-70 C-Therm TCi Principles of Operation Introduction The third generation of the technology expands the capabilities of this rapid, non-destructive testing instrumentation originally developed
More informationFirst major ( 043 ) a) 180 degrees b) 90 degrees c) 135 degrees d) 45 degrees e) 270 degrees
First major ( 043 ) 1) The displacement of a string carrying a traveling sinusoidal wave is given by y(x,t) = y m sin( kx ωt ϕ ). At time t = 0 the point at x = 0 has a displacement of zero and is moving
More informationState Polytechnic of Malang Malang Heat Effect. Thermodynamics Course Chapter 4 Agung Ari Wibowo S.T., M.Sc
State Polytechnic of Malang Malang 217 Heat Effect Thermodynamics Course Agung Ari Wibowo S.T., M.Sc Learning Objective Sensible Heat Heat Capacity & Integral Evaluation of Sensible Heat Laten Heat of
More informationChapter 3 PROPERTIES OF PURE SUBSTANCES
Thermodynamics: An Engineering Approach Seventh Edition in SI Units Yunus A. Cengel, Michael A. Boles McGraw-Hill, 2011 Chapter 3 PROPERTIES OF PURE SUBSTANCES Copyright The McGraw-Hill Companies, Inc.
More informationStuff. ---Tonight: Lecture 3 July Assignment 1 has been posted. ---Presentation Assignment on Friday.
Stuff ---Tonight: Lecture 3 July 0 ---Assignment 1 has been posted. Work from gravitational forces: h F gravity dx = h 0 0 mgh mg dx Where m (kg) and g is gravitational constant 9.8 m/s ---Presentation
More information2N7002T. 1. Product profile. 2. Pinning information. N-channel TrenchMOS FET. 1.1 General description. 1.2 Features. 1.
Rev. 1 17 November 25 Product data sheet 1. Product profile 1.1 General description N-channel enhancement mode Field-Effect Transistor (FET) in a plastic package using TrenchMOS technology. 1.2 Features
More informationEsterification in a PFR with Aspen Plus V8.0
Esterification in a PFR with Aspen Plus V8.0 1. Lesson Objectives Use Aspen Plus to determine whether a given reaction is technically feasible using a plug flow reactor. 2. Prerequisites Aspen Plus V8.0
More informationII/IV B.Tech (Regular) DEGREE EXAMINATION. (1X12 = 12 Marks) Answer ONE question from each unit.
Page 1 of 8 Hall Ticket Number: 14CH 404 II/IV B.Tech (Regular) DEGREE EXAMINATION June, 2016 Chemical Engineering Fourth Semester Engineering Thermodynamics Time: Three Hours Maximum : 60 Marks Answer
More informationPure Component Equations
Pure Component Equations Fitting of Pure Component Equations DDBSP - Dortmund Data Bank Software Package DDBST Software & Separation Technology GmbH Marie-Curie-Straße 10 D-26129 Oldenburg Tel.: +49 (0)
More informationThermodynamics I Spring 1432/1433H (2011/2012H) Saturday, Wednesday 8:00am - 10:00am & Monday 8:00am - 9:00am MEP 261 Class ZA
Thermodynamics I Spring 1432/1433H (2011/2012H) Saturday, Wednesday 8:00am - 10:00am & Monday 8:00am - 9:00am MEP 261 Class ZA Dr. Walid A. Aissa Associate Professor, Mech. Engg. Dept. Faculty of Engineering
More informationMAE 320 THERODYNAMICS FINAL EXAM - Practice. Name: You are allowed three sheets of notes.
50 MAE 320 THERODYNAMICS FINAL EXAM - Practice Name: You are allowed three sheets of notes. 1. Fill in the blanks for each of the two (Carnot) cycles below. (a) 5 a) Heat engine or Heat pump/refrigerator
More informationIntroduction to Engineering thermodynamics 2 nd Edition, Sonntag and Borgnakke. Solution manual
Introduction to Engineering thermodynamics nd Edition, Sonntag and Borgnakke Solution manual Chapter 4 Claus Borgnakke The picture is a false color thermal image of the space shuttle s main engine. The
More informationAbout this document. This document contains screenshots of software available from Cheresources.com. You can find this title in our online store at:
About this document This document contains screenshots of software available from Cheresources.com. You can find this title in our online store at: http://www.cheresources.com/cheplusstore/catalogue.php
More informationIn data sheets and application notes which still contain NXP or Philips Semiconductors references, use the references to Nexperia, as shown below.
Important notice Dear Customer, On 7 February 2017 the former NXP Standard Product business became a new company with the tradename Nexperia. Nexperia is an industry leading supplier of Discrete, Logic
More informationMiSeq System. Denature and Dilute Libraries Guide
MiSeq System Denature and Dilute Libraries Guide Overview 3 Protocol A: Standard Normalization Method 4 Protocol B: Bead-Based Normalization Method 6 Denature and Dilute PhiX Control 7 Supplemental Information
More informationX STEAM FOR MATLAB By Magnus Holmgren, Date:
X STEAM FOR MATLAB By Magnus Holmgren, www.x-eng.com Date: 2006-01-20 By Magnus Holmgren, www.x-eng.com The steam tables are free and provided as is. We take no responsibilities for any errors in the code
More informationIn data sheets and application notes which still contain NXP or Philips Semiconductors references, use the references to Nexperia, as shown below.
Important notice Dear Customer, On 7 February 217 the former NXP Standard Product business became a new company with the tradename Nexperia. Nexperia is an industry leading supplier of Discrete, Logic
More informationSpecifications: The shelf life of product is within 6 months. Features Description Test Conditions Requirements
Specifications: Operating Temperature Range : -25 C to+70 C Storage Temperature Range : -30 C to +80 C Current Range : 50mA, 12V DC The shelf life of product is within 6 months Test Sequence: Appearance
More informationIn data sheets and application notes which still contain NXP or Philips Semiconductors references, use the references to Nexperia, as shown below.
Important notice Dear Customer, On 7 February 2017 the former NXP Standard Product business became a new company with the tradename Nexperia. Nexperia is an industry leading supplier of Discrete, Logic
More informationPHD110NQ03LT. 1. Product profile. 2. Pinning information. N-channel TrenchMOS logic level FET. 1.1 Description. 1.2 Features. 1.
M3D3 Rev. 1 16 June 24 Product data 1. Product profile 1.1 Description N-channel enhancement mode field-effect transistor in a plastic package using TrenchMOS technology. 1.2 Features Logic level threshold
More information8.21 The Physics of Energy Fall 2009
MIT OpenCourseWare http://ocw.mit.edu 8.21 The Physics of Energy Fall 2009 For information about citing these materials or our Terms of Use, visit: http://ocw.mit.edu/terms. 8.21 Lecture 10 Phase Change
More informationThe Research of Heat Transfer Area for 55/19 Steam Generator
Journal of Power and Energy Engineering, 205, 3, 47-422 Published Online April 205 in SciRes. http://www.scirp.org/journal/jpee http://dx.doi.org/0.4236/jpee.205.34056 The Research of Heat Transfer Area
More informationCHAPTER. Properties of Pure Substances
CHAPTER 2 Properties of Pure Substances A Pure Substance Is a substance that is chemically homogenous and fixed in chemical composition.(e.g. water, nitrogen, air & etc.) mixture of oil and water is not
More informationIn data sheets and application notes which still contain NXP or Philips Semiconductors references, use the references to Nexperia, as shown below.
Important notice Dear Customer, On 7 February 217 the former NXP Standard Product business became a new company with the tradename Nexperia. Nexperia is an industry leading supplier of Discrete, Logic
More informationT718. c Dr. Md. Zahurul Haq (BUET) HX: Energy Balance and LMTD ME 307 (2018) 2/ 21 T793
HX: Energy Balance and LMTD Dr. Md. Zahurul Haq Professor Department of Mechanical Engineering Bangladesh University of Engineering & Technology (BUET) Dhaka-000, Bangladesh http://zahurul.buet.ac.bd/
More informationThere are five problems on the exam. Do all of the problems. Show your work
CHM 3400 Fundamentals of Physical Chemistry Second Hour Exam March 8, 2017 There are five problems on the exam. Do all of the problems. Show your work R = 0.08206 L atm/mole K N A = 6.022 x 10 23 R = 0.08314
More informationThermo. Dr. Nuri Solak, Asst. Prof.
Thermo Dr. Nuri Solak, Asst. Prof. http://web.itu.edu.tr/solaknu/ www.ninova.itu.edu.tr http://web.itu.edu.tr/solaknu/ 1 11.09.2014 => Introduction, Definition of terms, Importance of thermodynamics
More informationME Thermodynamics I
Homework - Week 01 HW-01 (25 points) Given: 5 Schematic of the solar cell/solar panel Find: 5 Identify the system and the heat/work interactions associated with it. Show the direction of the interactions.
More informationDr Ali Jawarneh. Hashemite University
Dr Ali Jawarneh Department of Mechanical Engineering Hashemite University Examine the moving boundary work or P d work commonly encountered in reciprocating devices such as automotive engines and compressors.
More information2N7002F. 1. Product profile. 2. Pinning information. N-channel TrenchMOS FET. 1.1 General description. 1.2 Features. 1.
Rev. 3 28 April 26 Product data sheet. Product profile. General description N-channel enhancement mode Field-Effect Transistor (FET) in a plastic package using TrenchMOS technology..2 Features Logic level
More informationIn data sheets and application notes which still contain NXP or Philips Semiconductors references, use the references to Nexperia, as shown below.
Important notice Dear Customer, On 7 February 217 the former NXP Standard Product business became a new company with the tradename Nexperia. Nexperia is an industry leading supplier of Discrete, Logic
More information