Guidelines for the Operation, Assembly, Repair, Testing and Inspection of Hazardous Material Cargo Tanks

Total Page:16

File Type:pdf, Size:1020Kb

Guidelines for the Operation, Assembly, Repair, Testing and Inspection of Hazardous Material Cargo Tanks Guidelines for the Operation, Assembly, Repair, Testing and Inspection of Hazardous Material Cargo Tanks FINAL REPORT Submitted to: U.S Department of Transportation Federal Motor Carrier Safety Administration June 2009 FOREWORD The purpose of this report is to assist the Federal Motor Carrier Safety Administration (FMCSA) in identifying factors that affect the service life of a cargo tank and to assist in the development of industry-informed guidelines to provide methods, programs, processes, and procedures that will minimize the effects of factors that reduce the service life of a cargo tank. The basis for these guidelines includes industry comments, regulatory documents, and professional organizations’ guidance. NOTICE This document is disseminated under the sponsorship of the Department of Transportation in the interest of information exchange. The United States Government assumes no liability for its contents or the use thereof. The contents of this Report reflect the views of the contractor, who is responsible for the accuracy of the data presented herein. The contents do not necessarily reflect the official policy of the Department of Transportation. This Report does not constitute a standard, specification, or regulation. The United States Government does not endorse products or manufacturers named herein. Trade or manufacturers’ names appear herein only because they are considered essential to the objective of this document. 1. Report No. 2. Government Accession No. 3. Recipient's Catalog No. 4. Title and Subtitle 5. Report Date Guidelines for the Operation, Assembly, Repair, Testing and June 30, 2009 Inspection of Hazardous Material Cargo Tanks 6. Performing Organization Code 7. Author(s) 8. Performing Organization Report No. Darrell Bowman, Andrew Marinik, Tammy Trimble, Stephanie Baker, and Allen Selz (Pressure Sciences, Inc.) 9. Performing Organization Name and Address 10. Work Unit No. (TRAIS) Virginia Tech Transportation Institute 3500 Transportation Research Plaza 11. Contract or Grant No. Blacksburg, Virginia 24061 VTRC # 08-0669-10 FMCSA # TMC75-07-H-00008 Task Order # 2 12. Sponsoring Agency Name and Address 13. Type of Report and Period Covered Department of Transportation Federal Motor Carrier Safety Administration Draft Report. Hazardous Materials Division West Wing, MC-ECH 14. Sponsoring Agency Code 1200 New Jersey Ave. SE FMCSA Washington, DC 20590 15. Supplementary Notes This program was administered through the Federal Motor Carrier Safety Administration (FMCSA) and the Virginia Transportation Research Council (VTRC). The FMCSA Authorized Organizational Technical Representative (AOTR) is James Simmons and the VTRC Principal Investigator (PI) is Mike Perfater. 16. Abstract This document consists of guidelines and recommendations related to operations, assembly, repair, testing and inspection of cargo tanks hauling hazardous materials. This document is the result of research findings from the project titled: Research to Identify the Factors that Affect the Service Life of Cargo Tanks [VTRC # 08-0669-10, FMCSA # TMC75-07-H-00008 Task Order # 2]. 17. Key Words 18. Distribution Statement Hazardous Materials, Specification Cargo Tanks, Maintenance, Repair, Assembly, Testing, Inspection, Operations 19. Security Classif. (of this 20. Security Classif. (of this page) 21. No. of 22. Price report) Pages Unclassified N/A Unclassified 105 Form DOT F 1700.7 (8-72) Reproduction of completed page authorized. SI* (MODERN METRIC) CONVERSION FACTORS APPROXIMATE CONVERSIONS TO SI UNITS Symbol When You Know Multiply By To Find Symbol LENGTH in inches 25.4 millimeters mm ft feet 0.305 meters m yd yards 0.914 meters m mi miles 1.61 kilometers km AREA in2 square inches 645.2 square millimeters mm2 ft2 square feet 0.093 square meters m2 yd2 square yard 0.836 square meters m2 ac acres 0.405 hectares ha mi2 square miles 2.59 square kilometers km2 VOLUME fl oz fluid ounces 29.57 milliliters mL gal gallons 3.785 liters L ft3 cubic feet 0.028 cubic meters m3 yd3 cubic yards 0.765 cubic meters m3 NOTE: volumes greater than 1000 L shall be shown in m3 MASS oz ounces 28.35 grams g lb pounds 0.454 kilograms kg T short tons (2000 lb) 0.907 megagrams (or "metric ton") Mg (or "t") TEMPERATURE (exact degrees) oF Fahrenheit 5 (F-32)/9 Celsius oC or (F-32)/1.8 ILLUMINATION fc foot-candles 10.76 lux lx fl foot-Lamberts 3.426 candela/m2 cd/m2 FORCE and PRESSURE or STRESS lbf poundforce 4.45 newtons N lbf/in2 poundforce per square inch 6.89 kilopascals kPa APPROXIMATE CONVERSIONS FROM SI UNITS Symbol When You Know Multiply By To Find Symbol LENGTH mm millimeters 0.039 inches in m meters 3.28 feet ft m meters 1.09 yards yd km kilometers 0.621 miles mi AREA mm2 square millimeters 0.0016 square inches in2 m2 square meters 10.764 square feet ft2 m2 square meters 1.195 square yards yd2 ha hectares 2.47 acres ac km2 square kilometers 0.386 square miles mi2 VOLUME mL milliliters 0.034 fluid ounces fl oz L liters 0.264 gallons gal m3 cubic meters 35.314 cubic feet ft3 m3 cubic meters 1.307 cubic yards yd3 MASS g grams 0.035 ounces oz kg kilograms 2.202 pounds lb Mg (or "t") megagrams (or "metric ton") 1.103 short tons (2000 lb) T TEMPERATURE (exact degrees) oC Celsius 1.8C+32 Fahrenheit oF ILLUMINATION lx lux 0.0929 foot-candles fc cd/m2 candela/m2 0.2919 foot-Lamberts fl FORCE and PRESSURE or STRESS N newtons 0.225 poundforce lbf kPa kilopascals 0.145 poundforce per square inch lbf/in2 *SI is the symbol for the International System of Units. Appropriate rounding should be made to comply with Section 4 of ASTM E380. (Revised March 2003) TABLE OF CONTENTS 1. INTRODUCTION.................................................................................................................1 1.1 THE CARGO TANK INDUSTRY ..................................................................................1 1.2 CARGO TANK REGULATIONS, STANDARDS, AND CODES .................................1 1.3 METHODS .......................................................................................................................2 1.3.1 Participants ........................................................................................................... 2 1.3.2 Data Collection .................................................................................................... 3 1.3.3 Data Analysis ....................................................................................................... 3 1.4 RESULTS AND DISCUSSION .......................................................................................4 1.5 STRUCTURE OF THE GUIDELINES DOCUMENT ....................................................4 2. CARGO TANK FLEET/FACILITY OPERATIONS .......................................................5 2.1 INTRODUCTION ............................................................................................................5 2.2 FLEET MANAGEMENT .................................................................................................5 2.2.1 Lading Management ............................................................................................ 5 2.2.2 Record Keeping/Tracking Key Measures ............................................................ 6 2.2.3 Safety Policies/Procedures ................................................................................... 7 2.2.4 Fleet/Facility Investment ..................................................................................... 8 2.3 DRIVER MANAGEMENT ..............................................................................................9 2.3.1 Driver Training .................................................................................................. 10 2.3.2 Driver Inspection ............................................................................................... 12 2.4 MAINTENANCE ...........................................................................................................14 2.4.1 Preventative Maintenance .................................................................................. 14 2.4.2 Maintenance: Protective Coating ....................................................................... 17 2.4.3 Cleaning ............................................................................................................. 18 2.4.4 Maintenance Training ........................................................................................ 19 3. CARGO TANK ASSEMBLY ............................................................................................21 3.1 INTRODUCTION ..........................................................................................................21 3.2 MOUNTING OF CARGO TANKS ON FRAMES........................................................21 3.2.1 Mounting ............................................................................................................ 21 3.2.2 Attachments ....................................................................................................... 22 3.3 INSTALLATION OF EQUIPMENT AND COMPONENTS (DOT 406/DOT 407/ DOT 412) .....................................................................................................................23 3.3.1 Manhole Assemblies .......................................................................................... 24 3.3.2 Accident Damage Protection ............................................................................. 24 vi 3.3.3 Pressure Relief ..................................................................................................
Recommended publications
  • 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.
    [Show full text]
  • 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.
    [Show full text]
  • 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
    [Show full text]
  • 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.
    [Show full text]
  • 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.
    [Show full text]
  • 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.
    [Show full text]
  • 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
    [Show full text]
  • 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.
    [Show full text]
  • 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.
    [Show full text]
  • 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.
    [Show full text]
  • 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.
    [Show full text]
  • 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.
    [Show full text]