Pressure Vessels
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12.1 12. Pressure Vessels: Combined Stresses Cylindrical Or Spherical
12. Pressure Vessels: Combined Stresses Cylindrical or spherical pressure vessels (e.g., hydraulic cylinders, gun barrels, pipes, boilers and tanks) are commonly used in industry to carry both liquid s and gases under pressure. When the pressure vessel is exposed to this pressure, the material comprising the vessel is subjected to pressure loading, and hence stresses, from all directions. The normal stresses resulting from this pressure are functions of the radius of the element under consideration, the shape of the pressure vessel (i.e., open ended cylinder, closed end cylinder, or sphere) as well as the applied pressure. Two types of analysis are commonly applied to pressure vessels. The most common method is based on a simple mechanics approach and is applicable to “thin wall” pressure vessels which by definition have a ratio of inner radius, r, to wall thickness, t, of r/t≥10. The second method is based on elasticity solution and is always applicable regardless of the r/t ratio and can be referred to as the solution for “thick wall” pressure vessels. Both types of analysis are discussed here, although for most engineering applications, the thin wall pressure vessel can be used. Thin-Walled Pressure Vessels Several assumptions are made in this method. 1) Plane sections remain plane 2) r/t ≥ 10 with t being uniform and constant 3) The applied pressure, p, is the gage pressure (note that p is the difference between the absolute pressure and the atmospheric pressure) 4) Material is linear-elastic, isotropic and homogeneous. 5) Stress distributions throughout the wall thickness will not vary 6) Element of interest is remote from the end of the cylinder and other geometric discontinuities. -
Coalescing Filters - to 175 Psig @ -20 to 200°F Series R20- Enameled Carbon Steel ◊ Series R22- 304 Stainless • Intake Air Flows to 40,000 SCFM Std
click here to return to website Coalescing Filters - to 175 psig @ -20 to 200°F Series R20- Enameled Carbon Steel ◊ Series R22- 304 Stainless • Intake Air Flows to 40,000 SCFM Std. • ASME U Stamp Std., Nat’l. Board Registered • Exceptionally Low ∆P, High Flow • Pleated Element Design - Exceptional Useful Filter Area • Hinged Swing Bolt Closure, Easy Access, O Ring Seal • 304SS Throat Safety Cages and ∆P Taps Std. • Rugged Enameled Steel or 304SS Construction Series R20 coalescing filters are fabricated from rugged enameled carbon steel, designed, constructed in accordance w/ASME Boiler & Pressure Vessel Code requirements for unfired pressure vessels. Any model can be modified to fit your needs. • Standard Connection Sizes from 1" to 12" NPT or raised face flange in-line connections are std. Alt. connections and/or an elevated discharge are avail- able. A hinged swing bolt closure is standard on models R20-0002 & larger. • Coalescing Filter Media. Sparks™ #907 media is composed of microfine borosilicate glass fibers bonded with phenolic resin. Together with a textile prefilter and a final drain layer, these pleated elements are remarkably effective at coalescing fine entrained oil and aqueous vapor mist from air/gas flows with very low ∆P. Experience has demonstrated high removal (over 90%) in dealing with 1.0 to 0.3µ aerosols. Other optional filter media such as #926 exceeds 95% removals. Individual performance will vary with the specific viscosity and vapor pressure of liquid con- taminates. • Options: Models R20-0202-RF-030 and larger include CS leg supports. (add 18" to OH) Carbon steel support legs in any length, gauges, and special finishes, are optional on any model. -
Design of Pressure Vessle (Air Bottle)
INTERNATIONAL JOURNAL FOR RESEARCH IN EMERGING SCIENCE AND TECHNOLOGY, VOLUME-4, ISSUE-1, JAN-2017 E-ISSN: 2349-7610 Design of Pressure Vessle (Air Bottle) N.V.Mahesh Babu.T1, Nersu Radhika2, Dr.P.Srinivasa Rao3 and Dr.B.Sudheer Prem Kumar4 1Associate Professor, Department of Mechanical Engineering, Guru Nanak Institutions Technical Campus, Ibrahimpatnam, Telangana 501 506, [email protected]. 2Assistant Professor, H & S Department, Sri Indu College of Engineering and Technology, Ibrahimpatnam, Telangana 501 506. 2 [email protected]. 3 Professor, Department of Mechanical Engineering,Al-Habeeb College of Engineering and Technology,Chevella, Telangana, [email protected] 4Professor & Chairman(Board of Studies) Mechanical Engineering, JNT University,Hyderabad, Telangana 500 085, [email protected], [email protected] ABSTRACT This is a paper that presents the design of a pressure vessel (Air Bottle). High pressure rise is developed in the pressure vessel and pressure vessel has to withstand severe forces. In the design of pressure vessel safety is the primary consideration, due the potential impact of possible accident. There have a few main factors to design the safe pressure vessel. This writing is focusing on analyzing the safety parameter for allowable working pressure. The cylinder is designed by considering the pressure, temperature and other constraints. Analysis of strength is made analytically and validation is done by ANSYS model and analysis. Keywords — Air bottle, ASME Code, Finite Element Analysis, ANSYS, Design for Fatigue. 1. INTRODUCTION 2. TYPE OF STRESS INDUCED IN VESSELS Pressure vessels are containers for containment of pressure, Generally there are two types of stresses induced. -
Chapter 3. Second and Third Law of Thermodynamics
Chapter 3. Second and third law of thermodynamics Important Concepts Review Entropy; Gibbs Free Energy • Entropy (S) – definitions Law of Corresponding States (ch 1 notes) • Entropy changes in reversible and Reduced pressure, temperatures, volumes irreversible processes • Entropy of mixing of ideal gases • 2nd law of thermodynamics • 3rd law of thermodynamics Math • Free energy Numerical integration by computer • Maxwell relations (Trapezoidal integration • Dependence of free energy on P, V, T https://en.wikipedia.org/wiki/Trapezoidal_rule) • Thermodynamic functions of mixtures Properties of partial differential equations • Partial molar quantities and chemical Rules for inequalities potential Major Concept Review • Adiabats vs. isotherms p1V1 p2V2 • Sign convention for work and heat w done on c=C /R vm system, q supplied to system : + p1V1 p2V2 =Cp/CV w done by system, q removed from system : c c V1T1 V2T2 - • Joule-Thomson expansion (DH=0); • State variables depend on final & initial state; not Joule-Thomson coefficient, inversion path. temperature • Reversible change occurs in series of equilibrium V states T TT V P p • Adiabatic q = 0; Isothermal DT = 0 H CP • Equations of state for enthalpy, H and internal • Formation reaction; enthalpies of energy, U reaction, Hess’s Law; other changes D rxn H iD f Hi i T D rxn H Drxn Href DrxnCpdT Tref • Calorimetry Spontaneous and Nonspontaneous Changes First Law: when one form of energy is converted to another, the total energy in universe is conserved. • Does not give any other restriction on a process • But many processes have a natural direction Examples • gas expands into a vacuum; not the reverse • can burn paper; can't unburn paper • heat never flows spontaneously from cold to hot These changes are called nonspontaneous changes. -
Boiler and Pressure Vessel Code Or BPVC
2017 Boiler and Pressure Vessel Code AN INTERNATIONAL CODE GO.ASME.ORG/BPVC17 The American Society of Mechanical Engineers® (ASME®) FOR DETAILS, CALL 1-800-THE-ASME (1-800-843-2763) (OR) 1-973-882-1170 (OR) VISIT GO.ASME.ORG/BPVC17 BOILERS AND PRESSURE VESSELS Since its first issuance in 1914, ASME’s BPVC has pioneered modern standards-development, maintaining a commitment to enhance public safety and technological advancement to meet the needs of a changing world. This “International Historic Mechanical Engineering Landmark” now has been incorporated into the laws of state and local jurisdictions of the United States and nine Canadian provinces. The BPVC is in use in 100 countries ASME’S BOILER AND PRESSURE VESSEL CODE (BPVC) 2017 around the world, with translations into a number of languages. The boiler and pressure-vessel sections of the BPVC have long been considered essential within such industries as electric power-generation, petrochemical, and transportation, among others. NUCLEAR ASME has played a vital role in supporting the nuclear industry since its inception, when ASME codes, standards and conformity assessment programs, ASME issued its first Standard, Code for originally developed for fossil fuel-fired the Conduct of Trials of Steam Boilers, in plants, were applied to nuclear power- 1884. This paper evolved into Rules for the plant construction. The nuclear sections Construction of Stationary Boilers and for of the BPVC reflect the best-practices Allowable Working Pressure – the first of industry, while contributing to more edition of ASME’s now-legendary Boiler than a half-century of safety for the and Pressure Vessel Code (BPVC) – issued general public. -
Pressure Vessels BT Series Replaceable Bladder Expansion Tank with Bottom System Connection RDT Series Fixed Bladder Expansion Tank
SINCE 1981 Pressure Vessels BT Series Replaceable Bladder Expansion Tank with Bottom System Connection RDT Series Fixed Bladder Expansion Tank SEP Series Vortex - Tangential Air Separator ADSR/AD Series In-Line Air/Dirt Separator (With or Without Strainer) RLU/RWU Series Hot Water Storage Tank CBT Series Buffer Tank www.flofab.com 003-cat-2019-pv Tanks (1).indd 1 2019-03-29 18:19:06 TABLE OF CONTENT RDT EXPANSION TANKS...........................................................................................................................2 BT EXPANSION TANKS..............................................................................................................................3 BT & RDT EXPANSION TANKS................................................................................................................4 INSTALLATION OF TANKS.......................................................................................................................5 SEP VORTEX TANGENTIAL AIR SEPARATOR..............................................................................6-8 ADSR/AD & ADSF IN-LINE AIR/DIRT SEPARATOR.................................................................9-14 RLU HOT WATER STORAGE TANK...............................................................................................15-20 RWU HOT WATER STORAGE TANK..............................................................................................21-24 CBT BUFFER TANK............................................................................................................................25-26 -
Guidelines for Pressure Vessel Safety Assessment
11^^^^ United States Department of Commerce National Institute of Standards and Tectinology NIST Special Publication 780 Guidelines for Pressure Vessel Safety Assessment Sumio Yukawa NATIONAL INSTITUTE OF STANDARDS & TECHNOLOGY Research Information Center Gaithersburg, MD 20899 DATE DUE Demco. Inc. 38-293 NIST Special Publication 780 Guidelines for Pressure Vessel Safety Assessment Sumio Yukawa Materials Reliability Division Materials Science and Engineering Laboratory National Institute of Standards and Technology Boulder, CO 80303 Sponsored by Occupational Safety and Health Administration U.S. Department of Labor Washington, DC 20210 Issued April 1990 U.S. Department of Commerce Robert A. Mosbacher, Secretary National Institute of Standards and Technology John W. Lyons, Director National Institute of Standards U.S. Government Printing Office For sale by the Superintendent and Technology Washington: 1990 of Documents Special Publication 780 U.S. Government Printing Office Natl. Inst. Stand. Technol. Washington, DC 20402 Spec. Publ. 780 75 pages (Apr. 1990) CODEN: NSPUE2 CONTENTS Page ABSTRACT vii 1. INTRODUCTION 1 2. SCOPE AND GENERAL INFORMATION 1 2 . 1 Scope 1 2.2 General Considerations 3 3. PRESSURE VESSEL DESIGN 4 3.1 ASME Code 4 3.1.1 Section VIII of ASME Code 5 3.1.2 Scope of Section VIII 5 3.1.3 Summary of Design Rules and Margins 6 3.1.4 Implementation of ASME Code 9 3.2 API Standard 620 10 3.2.1 Scope of API 620 12 3.2.2 Design Rules 12 3.2.3 Implementation of API 620 12 3.3. Remarks on Design Codes 14 4. DETERIORATION AND FAILURE MODES 14 4.1 Preexisting Causes 14 4.1.1 Design and Construction Related Deficiencies. -
21027 CBC Kettle Broch.Indd
DOT-106A500W Ton Containers 106A500W Ton Tank for Chlorine Service CBC 106A500W ton containers are manufactured with ASTM 516 Grade 70 material and all joints are completed using the electric fusion welding process. Unlike other electric fusion welded chlorine containers that have the circumferential weld joints under tension, the 106A500W utilizes a joint design, unique for chlorine containers, whereby the circumferential weld joint is in compression. In addition, unlike containers with the circumferential weld joint on the outside corner of the chime, the circumferential weld joint of the Columbiana 106A500W container is on the inside of the chime, where it is protected from damage by forklifts, collisions and other potentially damaging impact events. Like the Columbiana DOT 106A500X, Columbiana 106A500W containers have the exclusive safety- engineered feature of “inverted heads”—if a container is accidentally over-pressurized, the heads will reverse (become convex), providing an immediate visual indication of over- 106A500W pressurization. The reversed heads also create addi¬tional capacity to reduce the pressure and provide valuable time for corrective action. Through extensive prototype testing, the performance of the DOT 106A500W container has proved to equal and in many areas exceed that of the well proven DOT 106A500X. As with the DOT 106A500X multi unit tank car tank, the Columbiana DOT 106A500W multi unit tank car tank is approved by the US DOT with all the same performance and testing requirements as the DOT 106A500X. The DOT 106A500W container accommodates the Chlorine Institute emergency kit. Quality Steel Fabrication Since 1894 US DOT 49 CFR 179.300 Chlorine Institute Approved Columbiana Boiler Company ASME Certified Welders & NDT Level III Inspectors DOT-106A500W Ton Containers Fusion Welded Pressure Vessel Since 1936, Columbiana Boiler has manufactured over 200,000 transport containers for hazardous liquids and gases. -
Estimation of Internal Pressure of Liquids and Liquid Mixtures
Available online at www.ilcpa.pl International Letters of Chemistry, Physics and Astronomy 5 (2012) 1-7 ISSN 2299-3843 Estimation of internal pressure of liquids and liquid mixtures N. Santhi 1, P. Sabarathinam 2, G. Alamelumangai 1, J. Madhumitha 1, M. Emayavaramban 1 1Department of Chemistry, Government Arts College, C.Mutlur, Chidambaram-608102, India 2Retd. Registrar & Head of the Department of Technology, Annamalai University, Annamalainagar-608002, India E-mail address: [email protected] ABSTRACT By combining the van der Waals’ equation of state and the Free Length Theory of Jacobson, a new theoretical model is developed for the prediction of internal pressure of pure liquids and liquid mixtures. It requires only the molar volume data in addition to the ratio of heat capacities and critical temperature. The proposed model is simple, reliably accurate and capable of predicting internal pressure of pure liquids with an average absolute deviation of 4.24% in the predicted internal pressure values compared to those given in literature. The average absolute deviation in the predicted internal pressure values through the proposed model for the five binary liquid mixtures tested varies from 0.29% to 1.9% when compared to those of literature values. Keywords: van der Waals, pressure of liquids, theory of Jacobson, capacity of heat liquids, equation of Srivastava and Berkowitz 1. INTRODUTION The importance of internal pressure in understanding the properties of liquids and the full potential of internal pressure as a structural probe did become apparent with the pioneering work of Hildebrand 1, 2 and the first review of the subject by Richards 3 appeared in 1925. -
QDHP Bid Spec
quincycompressor.com 701 North Dobson Avenue Bay Minette, AL 36507 Phone: 251.937.5900 Fax: 251.937-1457 BID SPECIFICATION QHP SERIES HEATED REGENERATIVE AIR DRYER 1. SCOPE The specification outlines the requirements for the design, fabrication and supply of a dual tower, automatic, externally heated compressed air or gas dryer completely piped, wired, shop assembled and test run as a single unit. 2. GENERAL REFERENCE SPECIFICATIONS The air/gas dryer system shall be designed, fabricated and assembled in accordance with the applicable sections of the following codes, standards, and specifications: A. ASME Boiler and Pressure Vessel Code – Latest Edition, Section VIII, Division 1 of unfired pressure vessels. B. ASME Boiler and Pressure Vessel Code – Latest Edition, Section IX (Welding Qualification). C. NEMA Standard governing auto-cycling equipment and electrical components. D. National Electrical Code E. ANSI B31.1 Code for Power Piping F. ANSI B16.5 Code for Forged Steel Flanges. G. ANSI B16.9 & ASTM SA-234 for fittings. H. ANSI B16.3 Class 150 Threaded Iron Fittings. I. Customer Specification J. ISA – Instrument Society of America 3. PERFORMANCE REQUIREMENTS The dryer shall be designed to handle the following operating conditions: Fluid Compressed Air Capacity: Flow in SCFM rated @ 14.7 PSIA and 680F. Operating Pressure 100 PSIG (Normal) Design Pressure: 150 PSIG. (Standard) Inlet Temperature: 100° F (Normal) Moisture Content: Saturated Electrical Classification: NEMA Class 4 Power Supply: 115V-1PH-60HZ (35cfm to 100cfm) 460/480V-3PH – 60HZ (150 cfm and larger) Outlet Dew Point: -40F CONSTANT at the operating pressure. 1 4. SPECIFICATIONS Input Power: 120VAC or 230VAC, Single Phase Frequency: 50 or 60 Hertz Operating Temperature: 32° F to 122° F (0°C to 50°C) Time Delays Type: Digital Integrated Circuitry NEMA Cycle: 8 hours 1% Thermocouple Inputs: Three (3) Type ‘K’ Temperature measurement range: 50° F to 500° F (10°C to 260°C) Mechanical: Control unit with molded housing and encapsulated circuitry. -
7.3 the Thin-Walled Pressure Vessel Theory T
Section 7.3 7.3 The Thin-walled Pressure Vessel Theory An important practical problem is that of a cylindrical or spherical object which is subjected to an internal pressure p. Such a component is called a pressure vessel, Fig. 7.3.1. Applications arise in many areas, for example, the study of cellular organisms, arteries, aerosol cans, scuba-diving tanks and right up to large-scale industrial containers of liquids and gases. In many applications it is valid to assume that (i) the material is isotropic (ii) the strains resulting from the pressures are small (iii) the wall thickness t of the pressure vessel is much smaller than some characteristic radius: t ro ri ro ,ri p t 2ri 2r o Figure 7.3.1: A pressure vessel (cross-sectional view) Because of (i,ii), the isotropic linear elastic model is used. Because of (iii), it will be assumed that there is negligible variation in the stress field across the thickness of the vessel, Fig. 7.3.2. p actual stress t p approximate stress t Figure 7.3.2: Approximation to the stress arising in a pressure vessel As a rule of thumb, if the thickness is less than a tenth of the vessel radius, then the actual stress will vary by less than about 5% through the thickness, and in these cases the constant stress assumption is valid. Solid Mechanics Part I 185 Kelly Section 7.3 Note that a pressure xx yy zz pi means that the stress on any plane drawn inside the vessel is subjected to a normal stress pi and zero shear stress (see problem 6 in section 3.5.7). -
The Carnot Cycle, Reversibility and Entropy
entropy Article The Carnot Cycle, Reversibility and Entropy David Sands Department of Physics and Mathematics, University of Hull, Hull HU6 7RX, UK; [email protected] Abstract: The Carnot cycle and the attendant notions of reversibility and entropy are examined. It is shown how the modern view of these concepts still corresponds to the ideas Clausius laid down in the nineteenth century. As such, they reflect the outmoded idea, current at the time, that heat is motion. It is shown how this view of heat led Clausius to develop the entropy of a body based on the work that could be performed in a reversible process rather than the work that is actually performed in an irreversible process. In consequence, Clausius built into entropy a conflict with energy conservation, which is concerned with actual changes in energy. In this paper, reversibility and irreversibility are investigated by means of a macroscopic formulation of internal mechanisms of damping based on rate equations for the distribution of energy within a gas. It is shown that work processes involving a step change in external pressure, however small, are intrinsically irreversible. However, under idealised conditions of zero damping the gas inside a piston expands and traces out a trajectory through the space of equilibrium states. Therefore, the entropy change due to heat flow from the reservoir matches the entropy change of the equilibrium states. This trajectory can be traced out in reverse as the piston reverses direction, but if the external conditions are adjusted appropriately, the gas can be made to trace out a Carnot cycle in P-V space.