Guidelines for the Operation, Assembly, Repair, Testing and Inspection of Hazardous Material Cargo Tanks
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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. -
A.22G Liquefied Natural Gas Management Plan
APPENDIX A.22G: Liquid Natural Gas Management Plan Volume A.i: PREFACE VOLUME A.V: Volume A.V: Volume A.ii: Volume A.iii: Volume A.iV: ADDITIONAL Project BioPhysicAl socio-economic AdditionAl introduction VAlued VAlued YESAAyesAA & oVerView comPonents comPonents REQUIREMENTSreQuirements A.1 Introduction A.6 Terrain Features A.13 Employment and A.20 Effects of the Income Environment on Concordance Table to the the Project A.1A A.7 Water Quality A.13A Economic Impacts of the Executive Committee’s Request Casino Mine Project for Supplementary Information A.21 Accidents and A.7A Variability Water Balance Model Malfunctions Report A.14 Employability First Nations and A.2 A.7B Water Quality Predictions Report A.22 Environmental Community A.15 Economic Management Consultation A.7c Potential Effects of Climate Change on Development and the Variability Water Balance A.22A Waste and Hazardous Business Sector Materials A.2A Traditional Knowledge Management Plan Bibliography A.7d Updated Appendix B5 to Appendix 7A A.16 Community A.22B Spill Contingency A.7e 2008 Environmental Vitality Management Plan A.3 Project Location Studies Report: Final A.17 Community A.22c Sediment and Erosion A.7F The Effect of Acid Rock Drainage on Control Management A.4 Project Description Casino Creek Infrastructure and Plan Services A.7G Toxicity Testing Reports A.22d Invasive Species A.4A Tailings Management Facility Management Plan Construction Material Alternatives A.7h Appendix A2 to Casino Waste Rock A.18 Cultural and Ore Geochemical Static Test As- A.22e Road Use -
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. -
Guidance on Estimating Condensate and Crude Oil Loading Losses from Tank Trucks Section I
Guidance on Estimating Condensate and Crude Oil Loading Losses from Tank Trucks Section I. Introduction The purpose of this guidance document is to provide general guidance on estimating condensate and crude oil evaporative emissions from tank trucks during loading operations. • OAC 165:10-1-2 defines condensate as “a liquid hydrocarbon which: (A) [w]as produced as a liquid at the surface, (B) [e]xisted as a gas in the reservoir, and (C) [h]as an API gravity greater than or equal to fifty degrees, unless otherwise proven.” • OAC 165:10-1-2 defines crude oil as “any petroleum hydrocarbon, except condensate, produced from a well in liquid form by ordinary production methods.” The Air Quality Division (AQD) has received permit applications requesting the use of a reduced Volatile Organic Compounds (VOC) loading emission factor for estimating tank truck loading loss emissions. This is to account for methane and ethane entrained in the petroleum liquid that, along with VOC, are released in the vapors as the petroleum liquid is loaded. In some cases, the proposed non-VOC reduction represents a combined methane and ethane vapor concentration of greater than 30 percent by weight. Permit applications are submitted with loading loss emissions calculated using the methodology outlined in AP-42 (6/08), Section 5.2, using process simulation software, or both. Process simulation software estimates emissions based on all streams reaching equilibrium. The majority of permitted loading losses are calculated assuming negligible concentrations of methane and/or ethane. Due to the high concentrations of methane and ethane proposed in some permit applications, a review of the calculation methodology was conducted and resulted in this guidance document. -
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 -
Safe Operation of Vacuum Trucks in Petroleum Service
Safe Operation of Vacuum Trucks in Petroleum Service API RECOMMENDED PRACTICE 2219 THIRD EDITION, NOVEMBER 2005 REAFFIRMED, NOVEMBER 2012 --``,,```,`,,,`,,`````,,,,``,``-`-`,,`,,`,`,,`--- Copyright American Petroleum Institute Provided by IHS under license with API Licensee=Shell Global Solutions International B.V. Main/5924979112, User=Elliott No reproduction or networking permitted without license from IHS Not for Resale, 12/30/2013 09:55:43 MST --``,,```,`,,,`,,`````,,,,``,``-`-`,,`,,`,`,,`--- Copyright American Petroleum Institute Provided by IHS under license with API Licensee=Shell Global Solutions International B.V. Main/5924979112, User=Elliott No reproduction or networking permitted without license from IHS Not for Resale, 12/30/2013 09:55:43 MST Safe Operation of Vacuum Trucks in Petroleum Service Downstream Segment API RECOMMENDED PRACTICE 2219 THIRD EDITION, NOVEMBER 2005 REAFFIRMED, NOVEMBER 2012 --``,,```,`,,,`,,`````,,,,``,``-`-`,,`,,`,`,,`--- Copyright American Petroleum Institute Provided by IHS under license with API Licensee=Shell Global Solutions International B.V. Main/5924979112, User=Elliott No reproduction or networking permitted without license from IHS Not for Resale, 12/30/2013 09:55:43 MST SPECIAL NOTES API publications necessarily address problems of a general nature. With respect to particular circumstances, local, state, and federal laws and regulations should be reviewed. Neither API nor any of API's employees, subcontractors, consultants, committees, or other assignees make any warranty or representation, either express or implied, with respect to the accuracy, completeness, or usefulness of the information contained herein, or assume any liability or responsibility for any use, or the results of such use, of any information or process disclosed in this publication. Neither API nor any of API's employees, subcontractors, con- sultants, or other assignees represent that use of this publication would not infringe upon pri- vately owned rights. -
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. -
Chemical Logistics: the Price of Success These Are Good Times for Chemical Manufacturing in the United States
—JOINT SPONSORED CONTENT FROM— Chemical Week Chemical Logistics: The Price of Success These are good times for chemical manufacturing in the United States. But an active market creates special challenges for companies that need to transport chemical products. 66 Inbound Logistics • June 2018 Chemical Logistics: The Price of Success he U.S. chemical industry is going strong, according to American Chemistry Council (ACC) figures released in late 2017. U.S. chemical president, chemical and oil and gas production volume for 2017, excluding pharmaceuticals, would be at Boston-based consulting firm 0.8 percent higher than in 2016, finds the ACC’s annual industry Maine Pointe. Tstudy. ACC predicts further growth of 3.7 percent in 2018, 3.9 percent in Companies that transport 2019, and 3 percent in 2020. chemicals, or manage chemicals transportation, saw a spike in Continued access to inexpensive creating a $32-billion trade business in 2017 in the wake of shale gas, used for feedstock in surplus for chemicals, excluding several major hurricanes, including the manufacturing process and pharmaceuticals, in 2017. Chemical Harvey, which ravaged southern for energy, gives U.S. chemical exports totaled $127 billion, and Texas in August of that year. “Some manufacturers an advantage over imports rose by 2.8 percent over of the production facilities we were competitors in other locations, 2017, reaching $96 billion. working with sustained damage,” says the ACC. Companies have Along with low-cost feedstock, recalls Adam Kroupa, general announced nearly 320 new the U.S. chemical industry manager of the ChemSolutions chemical production projects in benefits from the strength of the business at third-party logistics the United States, with a total general economy, which is driving (3PL) provider C.H. -
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.