<?xml version="1.0" encoding="windows-1252"?><SEC xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:noNamespaceSchemaLocation="http://si.ksc.nasa.gov/sidownloads/xml/specsintactSEC.xsd"><MTA NAME="SUBFORMAT" CONTENT="NEW"/><BRK/>
<HDR><AST/><BRK/>
USACE / NAVFAC / AFCESA / NASA                  UFGS-33 56 53 (April 2008)<BRK/>
                                                --------------------------<BRK/>
Preparing Activity:  <PRA>USACE</PRA>                      Superseding<BRK/>
                                                UFGS-33 56 53 (April 2006)<BRK/>
<BRK/>
<HL4>UNIFIED FACILITIES GUIDE SPECIFICATIONS</HL4><BRK/>
<BRK/>
<HL4>References are in agreement with UMRL dated January 2009</HL4><BRK/>
<AST/><BRK/></HDR>
<BRK/>
<SCN>SECTION 33 56 53</SCN><BRK/>
<BRK/>
<STL>PRESSURE VESSELS FOR STORAGE OF COMPRESSED GASES</STL><BRK/>
<DTE>04/08</DTE><BRK/>
<NTE><BRK/>
<AST/><BRK/>
<NPR>NOTE:  This guide specification covers the requirements for <SCP>pressure vessels 
for the storage of compressed gases</SCP>.<BRK/>
<BRK/>
Edit this guide specification for project specific requirements by adding, deleting, 
or revising text.  For bracketed items, choose applicable items(s) or insert 
appropriate information.<BRK/>
<BRK/>
Remove information and requirements not required in respective project, whether 
or not brackets are present.<BRK/>
<BRK/>
Comments and suggestions on this guide specification are welcome and should 
be directed to the technical proponent of the specification.  A listing of <URL HREF="http://65.204.17.188/report/ufgs.html">technical 
proponents</URL>, including their organization designation and telephone number, is 
on the Internet.<BRK/>
<BRK/>
Recommended changes to a UFGS should be submitted as a  <URL HREF="http://65.204.17.188/projnet/cms/public.html">Criteria Change Request 
(CCR)</URL>.</NPR><BRK/>
<AST/><BRK/></NTE>
<BRK/>
<PRT><TTL>PART 1   GENERAL</TTL><BRK/>
<NTE><BRK/>
<AST/><BRK/>
<NPR>NOTE:  This guide specification is intended to be used for installation of unfired 
pressure vessels for the storage of compressed gases such as helium, nitrogen, 
oxygen, and air in the temperature range of plus 49 degrees C to minus 40 degrees 
C (plus 120 degrees F to minus 40 degrees F).  Its use is not intended for cryogenic 
fluids nor for commercial compressed air receivers operating at pressures of 
approximately 2.07 MPa (300 psig) or below.  If corrosive gases are stored, 
special treatment for the interior of the vessel will be specified.  Lining 
materials such as alloy or epoxy coatings may be used for the interior of the 
vessels.  The drawings will show all piping connection points both in physical 
location and size.</NPR><BRK/>
<AST/><BRK/></NTE>
<BRK/>
<SPT><TTL>1.1   REFERENCES</TTL><BRK/>
<NTE><BRK/>
<AST/><BRK/>
<NPR>NOTE:  This paragraph is used to list the publications cited in the text of 
the guide specification.  The publications are referred to in the text by basic 
designation only and listed in this paragraph by organization, designation, 
date, and title.<BRK/>
<BRK/>
Use the Reference Wizard's Check Reference feature when you add a RID outside 
of the Section's Reference Article to automatically place the reference in the 
Reference Article.  Also use the Reference Wizard's Check Reference feature 
to update the issue dates.<BRK/>
<BRK/>
References not used in the text will automatically be deleted from this section 
of the project specification when you choose to reconcile references in the 
publish print process.</NPR><BRK/>
<AST/><BRK/></NTE>
<BRK/>
<TXT>The publications listed below form a part of this specification to the extent referenced.  The publications are 
referred to within the text by the basic designation only.</TXT><BRK/>
<BRK/>
<REF><ORG>ASME INTERNATIONAL (ASME)</ORG><BRK/><BRK/><RID>ASME B16.20</RID><RTL>(2007) Metallic Gaskets for Pipe Flanges - Ring-Joint, Spiral Wound, and Jacketed</RTL><BRK/><BRK/><RID>ASME B16.5</RID><RTL>(2003) Standard for Pipe Flanges and Flanged Fittings:  NPS 1/2 Through NPS 24</RTL><BRK/><BRK/><RID>ASME B31.3</RID><RTL>(2008) Process Piping</RTL><BRK/><BRK/><RID>ASME BPVC SEC IX</RID><RTL>(2007; Addenda 2008) Boiler and Pressure Vessel Code; Section IX, Welding and Brazing Qualifications</RTL><BRK/><BRK/><RID>ASME BPVC SEC V</RID><RTL>(2007; Addenda 2008) Boiler and Pressure Vessel Code; Section V, Nondestructive Examination</RTL><BRK/><BRK/><RID>ASME BPVC SEC VIII D1</RID><RTL>(2007; Addenda 2008) Boiler and Pressure Vessel Code; Section VIII, Pressure Vessels Division 1 - Basic Coverage</RTL><BRK/><BRK/></REF><REF><ORG>ASTM INTERNATIONAL (ASTM)</ORG><BRK/><BRK/><RID>ASTM A 182/A 182M</RID><RTL>(2008a) Standard Specification for Forged or Rolled Alloy-Steel Pipe Flanges, Forged Fittings, and Valves and Parts for High-Temperature Service</RTL><BRK/><BRK/><RID>ASTM A 193/A 193M</RID><RTL>(2008b) Standard Specification for Alloy-Steel and Stainless Steel Bolting Materials for High-Temperature Service</RTL><BRK/><BRK/><RID>ASTM A 194/A 194M</RID><RTL>(2008b) Standard Specification for Carbon and Alloy Steel Nuts for Bolts for High-Pressure or High-Temperature Service, or Both</RTL><BRK/><BRK/><RID>ASTM A 240/A 240M</RID><RTL>(2008) Standard Specification for Chromium and Chromium-Nickel Stainless Steel Plate, Sheet, and Strip for Pressure Vessels and for General Applications</RTL><BRK/><BRK/><RID>ASTM A 312/A 312M</RID><RTL>(2008a) Standard Specification for Seamless, Welded, and Heavily Worked Austenitic Stainless Steel Pipes</RTL><BRK/><BRK/><RID>ASTM A 320/A 320M</RID><RTL>(2008) Standard Specification for Alloy/Steel Bolting Materials for Low-Temperature Service</RTL><BRK/><BRK/><RID>ASTM A 36/A 36M</RID><RTL>(2008) Standard Specification for Carbon Structural Steel</RTL><BRK/><BRK/><RID>ASTM A 370</RID><RTL>(2008b) Standard Test Methods and Definitions for Mechanical Testing of Steel Products</RTL><BRK/><BRK/><RID>ASTM A 376/A 376M</RID><RTL>(2006) Standard Specification for Seamless Austenitic Steel Pipe for High-Temperature Central-Station Service</RTL><BRK/><BRK/><RID>ASTM A 403/A 403M</RID><RTL>(2007a) Standard Specification for Wrought Austenitic Stainless Steel Piping Fittings</RTL><BRK/><BRK/><RID>ASTM E 165</RID><RTL>(2002) Standard Test Method for Liquid Penetrant Examination</RTL><BRK/><BRK/><RID>ASTM E 709</RID><RTL>(2008) Standard Guide for Magnetic Particle Examination</RTL><BRK/><BRK/></REF><REF><ORG>MANUFACTURERS STANDARDIZATION SOCIETY OF THE VALVE AND FITTINGS INDUSTRY (MSS)</ORG><BRK/><BRK/><RID>MSS SP-58</RID><RTL>(2002) Standard for Pipe Hangers and Supports - Materials, Design and Manufacture</RTL><BRK/><BRK/><RID>MSS SP-69</RID><RTL>(2003; R 2004) Standard for Pipe Hangers and Supports - Selection and Application</RTL><BRK/><BRK/></REF><REF><ORG>SOCIETY OF AUTOMOTIVE ENGINEERS INTERNATIONAL (SAE)</ORG><BRK/><BRK/><RID>SAE ARP598</RID><RTL>(2003; Rev C) Aerospace Microscopic Sizing and Counting of Particulate Contamination for Fluid Power Systems</RTL><BRK/><BRK/></REF><REF><ORG>THE SOCIETY FOR PROTECTIVE COATINGS (SSPC)</ORG><BRK/><BRK/><RID>SSPC Paint 21</RID><RTL>(1982; E 2004) Paint Specification No. 21 White or Colored Silicone Alkyd Paint (Type I, High Gloss and Type II, Medium Gloss)</RTL><BRK/><BRK/><RID>SSPC Paint 25</RID><RTL>(1997; E 2004) Paint Specification No. 25Zinc Oxide, Alkyd, Linseed Oil Primer for Use Over Hand Cleaned Steel Type I and Type II</RTL><BRK/><BRK/></REF></SPT><SPT><TTL>1.2   SUBMITTALS</TTL><BRK/>
<NTE><BRK/>
<AST/><BRK/>
<NPR>NOTE:  Review submittal description (SD) definitions in Section <SRF>01 33 00</SRF> SUBMITTAL 
PROCEDURES and edit the following list to reflect only the submittals required 
for the project.  Submittals should be kept to the minimum required for adequate 
quality control.<BRK/>
<BRK/>
A “G” following a submittal item indicates that the submittal requires Government 
approval.  Some submittals are already marked with a “G”.  Only delete an existing 
“G” if the submittal item is not complex and can be reviewed through the Contractor’s 
Quality Control system.  Only add a “G” if the submittal is sufficiently important 
or complex in context of the project.<BRK/>
<BRK/>
For submittals requiring Government approval on Army projects, a code of up 
to three characters within the submittal tags may be used following the "G" 
designation to indicate the approving authority.  Codes for Army projects using 
the Resident Management System (RMS) are:  "AE" for Architect-Engineer; "DO" 
for District Office (Engineering Division or other organization in the District 
Office); "AO" for Area Office; "RO" for Resident Office; and "PO" for Project 
Office.  Codes following the "G" typically are not used for Navy, Air Force, 
and NASA projects.<BRK/>
<BRK/>
Choose the first bracketed item for Navy, Air Force and NASA projects, or choose 
the second bracketed item for Army projects.</NPR><BRK/>
<AST/><BRK/></NTE>
<BRK/>
<TXT>Government approval is required for submittals with a "G" designation; submittals not having a "G" designation 
are for [Contractor Quality Control approval.][information only.  When used, a designation following the "G" 
designation identifies the office that will review the submittal for the Government.]  Submit the following in 
accordance with Section <SRF>01 33 00</SRF> SUBMITTAL PROCEDURES:</TXT><BRK/>
<BRK/>
<LST><SUB>SD-02 Shop Drawings</SUB></LST><BRK/>
<BRK/>
<ITM><SUB>Installation</SUB>[; <SUB>G</SUB>][; <SUB>G, [_____]</SUB>]</ITM><BRK/>
<BRK/>
<ITM>  Drawings showing the locations of weld seams, sizes and types of welds, piping arrangements, 
nozzle reinforcement, method of nozzle attachment, plate and head thicknesses, vessel weights, 
details of gas relief holes in multiple-layered shells, lifting lugs [manways] [details of drains 
and vents] details required for fabrication of the vessels, and a complete list of materials.  
Include design calculations for vessels and manifolds with the drawings, including chemical 
composition and mechanical properties of the steels used, and including reference to <RID>ASME BPVC SEC VIII D1</RID>
.  Loading, lifting, shipping, unloading, field testing, and installation instructions, prior 
to completion of fabrication.  [Installation drawings for piping manifolds showing field piece 
markings.] [The pressure vessel foundation design drawings.]</ITM><BRK/>
<BRK/>
<LST><SUB>SD-06 Test Reports</SUB></LST><BRK/>
<BRK/>
<ITM><SUB>Test</SUB></ITM><BRK/>
<BRK/>
<ITM>  Test reports for radiographic, magnetic particle, liquid penetrant, impact, and hydrostatic 
tests performed to prove compliance with specified criteria, upon completion and testing of 
the installed system.</ITM><BRK/>
<BRK/>
<ITM><SUB>Procedure for Welding Vessels and Manifolds</SUB></ITM><BRK/>
<BRK/>
<ITM>  Certified copies of performance test records indicating that the welders have passed qualification 
test in conformance with <RID>ASME BPVC SEC IX</RID>, prior to work on piping or vessel fabrication.  Where 
such test records are not furnished, perform qualification tests witnessed by Contracting Officer.  
Each welder shall be qualified for the position and type of material assigned.  Requalification 
tests will be required when work of the welder creates a reasonable doubt as to the welder's 
proficiency.  Such a retest may include both radiographic and mechanical tests.  Welders failing 
a requalification test will not be permitted to work.</ITM><BRK/>
<BRK/>
<LST><SUB>SD-07 Certificates</SUB></LST><BRK/>
<BRK/>
<ITM><SUB>Cleaning</SUB></ITM><BRK/>
<BRK/>
<ITM>  A certified record of satisfactory cleaning of similar vessels or a record certifying not 
less than 2 years of experience in chemical cleaning to similar standards and for similar service.  
No organization performing cleaning will be considered qualified unless such proof of cleaning 
experience is submitted.</ITM><BRK/>
<BRK/></SPT>
</PRT><PRT><TTL>PART 2   PRODUCTS</TTL><BRK/>
<BRK/>
<SPT><TTL>2.1   MATERIALS</TTL><BRK/>
<NTE><BRK/>
<AST/><BRK/>
<NPR>NOTE:  The vessel design pressure will determine the schedule of pipe, type 
of flange facing, and whether pipe or tubing and flanges or high-pressure fittings 
are required.</NPR><BRK/>
<AST/><BRK/></NTE>
<BRK/>
<TXT>Use a nameplate on vessels except when stamping is directly applied.  A nameplate plainly stamped in letters 
not less than<MET> 10 mm</MET><ENG> 3/8 inch</ENG> high shall be permanently attached to vessel or vessel assembly structure at a conspicuous 
location.  Attachment to shell or head portions or around the nozzle openings of vessel shall be by welding, 
brazing, soldering, or by tamper-resistant mechanical fasteners of suitable metal construction.  Attachment by 
pressure sensitive adhesives of any type is not acceptable.  Stamping shall show serial number, symbols of the 
manufacturer, specification number, date of manufacture, design pressure, test pressure, maximum allowable working 
pressure at operating temperature, minimum working temperature for vessels that operate, and water volume capacity 
in cubic feet to nearest tenth.  Manifolds shall be identified by a stainless steel plate or tag attached by 
stainless steel bands or clamps and shall show serial number, if any, symbols of the manufacturer, specification 
number, date of manufacture, design pressure, and test pressure.  Vessels shall be code stamped in accordance 
with <RID>ASME BPVC SEC VIII D1</RID>.  Asbestos and asbestos-containing products will not be allowed.</TXT><BRK/>
<BRK/>
<SPT><TTL>2.1.1   Piping for Manifolds</TTL><BRK/>
<BRK/>
<TXT>Piping for manifolds shall be seamless stainless steel pipe or stainless steel tubing suitable for service and 
pressure through a temperature range of<MET> plus 49 to minus 87 degrees C</MET><ENG> plus 120 to minus 125 degrees F</ENG>, in accordance 
with <RID>ASME B31.3</RID>.  Stainless steel pipe in thicknesses up to and including Schedule 80S shall conform to <RID>ASTM A 312/A 312M</RID>
, Grade TP 304L or <RID>ASTM A 376/A 376M</RID>, Grade TP 304; thicknesses greater than Schedule 80S shall conform to <RID>ASTM A 376/A 376M</RID>
, Grade TP 304.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.1.2   Fittings for Manifolds</TTL><BRK/>
<BRK/>
<TXT>Fittings for manifolds shall be seamless buttweld or socket-weld type and of material conforming to <RID>ASTM A 403/A 403M</RID>
, Grade WP 304L, or if tubing is used, fittings shall be stainless steel positive mechanical high-pressure threaded 
type.  Fittings shall be suitable for pressures specified for vessels and shall be compatible with manifold piping 
or tubing.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.1.3   Flanges for Manifolds</TTL><BRK/>
<BRK/>
<TXT>Flanges for manifolds shall be of forged stainless steel conforming to <RID>ASTM A 182/A 182M</RID>, Grades F 304, F 316, 
or F 347.  Flanges shall conform to <RID>ASME B16.5</RID> where pressure-temperature ratings fall within limits established 
therein.  For pressure-temperature outside such limits, flanges shall conform to Appendix 2 of <RID>ASME BPVC SEC VIII D1</RID>
.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.1.4   Bolts, Studs, and Nuts for Flanges</TTL><BRK/>
<BRK/>
<TXT>Bolts and studs for flanges for stainless steel manifolds shall be strain hardened and shall conform to <RID>ASTM A 320/A 320M</RID>
, Grade B8 or equivalent age-hardened material.  Nuts shall conform to <RID>ASTM A 194/A 194M</RID>, Grade 4, and shall 
be hexagonal American Standard Heavy Series.  For manways and for other than stainless steel flanges, bolts and 
studs shall conform to <RID>ASTM A 193/A 193M</RID>, Grade B7, and nuts shall conform to <RID>ASTM A 194/A 194M</RID>, Grade 2H.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.1.5   Flange Gaskets</TTL><BRK/>
<BRK/>
<TXT>Gaskets for ring type joint flanges shall be octagonal, fully annealed stainless steel ring type gaskets with 
dimensions conforming to <RID>ASME B16.20</RID>.  Gaskets for helium service shall be oval type.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.1.6   Supports and Attachments</TTL><BRK/>
<BRK/>
<TXT>Structural steel for supports or structural attachments shall conform to requirements specified for vessel or 
to <RID>ASTM A 36/A 36M</RID>.  Where legs of <RID>ASTM A 36/A 36M</RID> steel are attached to stainless steel vessels, pads of <RID>ASTM A 240/A 240M</RID>
 steel shall be used to make the attachment.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.1.7   Vessels</TTL><BRK/>
<BRK/>
<TXT>Vessels shall be constructed of steels which meet the requirements for design pressure and temperatures.  No 
steel shall be used which does not meet the following minimum requirements at room temperature:  elongation in<MET>
 50 mm</MET><ENG> 2 inches</ENG>, minimum 15 percent; reduction of area, minimum 40 percent.  Where heat treatment is employed, 
reheat treatment will be permitted.  Supporting information shall be furnished attesting to chemical composition 
and mechanical properties based on test results of the steel used for the design of the vessels.  Where <RID>ASME BPVC SEC VIII D1</RID>
 is applicable to material from which the pressure vessels are fabricated, requirements of <RID>ASME BPVC SEC VIII D1</RID>
 shall be adhered to, except as modified in this section.</TXT><BRK/>
<BRK/></SPT>
</SPT><SPT><TTL>2.2   SPECIAL REQUIREMENTS</TTL><BRK/>
<BRK/>
<SPT><TTL>2.2.1   Multiple-Layered or Banded Vessels</TTL><BRK/>
<BRK/>
<TXT>Longitudinally-welded seams in individual layers shall be spaced in an offset pattern so that centers of the 
welded longitudinal joints of adjacent layers are separated circumferentially by a distance of at least 5 times 
the layer thickness.  Thickness of circumferential welds for attaching heads or flanges, and the combined thickness 
of circumferential welds for layers, shall not be less than minimum required thickness of a hemispherical head 
divided by the efficiency of head-to-shell joint.  Longitudinal seam welds on inner shell and all intermediate 
layers shall be ground flush before application of next layer.</TXT><BRK/>
<BRK/>
<SPT><TTL>2.2.1.1   Slag</TTL><BRK/>
<BRK/>
<TXT>Slag shall be removed after each weld layer in both longitudinal and circumferential weld joints, and each layer 
of weld shall be visually inspected for undercut, lack of fusion, irregularity of weld deposit, slag inclusions, 
and porosity.  Corrections shall be made before next weld layer is deposited.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.2.1.2   Post-Weld Heat Treatment</TTL><BRK/>
<BRK/>
<TXT>Post-weld heat treatment shall be accomplished in accordance with <RID>ASME BPVC SEC VIII D1</RID>.  Heads shall be stress 
relieved after forming operations and attachments by welding have been completed, and before assembly to vessel.  
Inner shell shall be stress relieved after completion of longitudinal welds.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.2.1.3   Inner Shell Thickness Less Than One-Half Head Thickness</TTL><BRK/>
<BRK/>
<TXT>Where thickness of inner shell is less than one-half the required head thickness and layers are<MET> 10 mm</MET><ENG> 3/8 inch</ENG>
 thick or less, vessel shall conform to the following:</TXT><BRK/>
<BRK/>
<LST>a.  Multiple-layered shells in which layers are welded circumferentially in which each layer may be made 
of one or more plates shall have holes drilled radially from the outside of vessel to inner shell.  Each 
layer plate shall have at least two vent holes of<MET> 6 mm</MET><ENG> 1/4 inch</ENG> minimum diameter.  Holes shall not penetrate 
inner shell of vessel.  Drawings shall show such holes in detail.</LST><BRK/>
<BRK/>
<LST>b.  After longitudinal seam of each layer has been welded, the layer shall be hammer tested for contact 
with layer underneath.  A loose area greater than<MET> 300 mm</MET><ENG> 12 inches</ENG> circumferentially and<MET> 600 mm</MET><ENG> 24 inches</ENG>
 longitudinally will not be accepted.  A maximum single radial gap of<MET> 3 mm</MET><ENG> 0.120 inch</ENG> between any two 
layers, as measured at the ends of the shell sections at right angles to vessel axis, will be acceptable.  
A gap of<MET> 1.5 mm</MET><ENG> 0.060 inch</ENG> shall be limited to a length of<MET> 100 mm</MET><ENG> 4 inches</ENG>; a gap of<MET> 1 mm</MET><ENG> 0.040 inch</ENG> 
shall be limited to<MET> 150 mm</MET><ENG> 6 inches</ENG>; a gap of<MET> 0.508 mm</MET><ENG> 0.020 inch</ENG> shall be limited to<MET> 300 mm</MET><ENG> 12 inches</ENG>
.  In event of more than one loose area circumferentially in any<MET> 600 mm</MET><ENG> 24 inch</ENG> length, total of such 
areas shall not exceed the area prescribed by the above limits.</LST><BRK/>
<BRK/></SPT>
<SPT><TTL>2.2.1.4   Inner Shell Thickness Greater Than One-Half Head Thickness</TTL><BRK/>
<BRK/>
<TXT>Where thickness of inner shell is greater than one-half required head thickness, vessel shall conform to one 
of the following requirements, as applicable.</TXT><BRK/>
<BRK/>
<LST>a.  Tightness of layers having a nominal thickness of<MET> 10 mm</MET><ENG> 3/8 inch</ENG> and under shall be established as 
specified.</LST><BRK/>
<BRK/>
<LST>b.  Tightness of vessels with layers over<MET> 10 mm</MET><ENG> 3/8 inch</ENG> nominal thickness, in which inner layer is expanded 
to outer layer, shall be determined by demonstrated elastic behavior as substantiated by pressure volume 
curve during repressurization, after expansion to the design pressure to demonstrate that the layers 
act together.</LST><BRK/>
<BRK/>
<LST>c.  The tightness of vessels with layers over<MET> 10 mm</MET><ENG> 3/8 inch</ENG> nominal thickness, in which outer layer 
or layers are shrunk over inner layer or layers, shall be determined by measuring the diameter or circumference 
of layers in cold condition to show that there is sufficient interference between layers to demonstrate 
that the layers act together.</LST><BRK/>
<BRK/></SPT>
</SPT><SPT><TTL>2.2.2   Seamless Cylinders</TTL><BRK/>
<NTE><BRK/>
<AST/><BRK/>
<NPR>NOTE:  End connections will be determined by piping system to which vessels 
will be connected and by the design pressure.</NPR><BRK/>
<AST/><BRK/></NTE>
<BRK/>
<TXT>Seamless cylinders shall be of a type and size suitable for manifolding together to meet gaseous-storage volume 
requirements.  Seamless cylinders shall have two outlets, one at each end on longitudinal centerline; each outlet 
shall be a minimum of<MET> 50 mm</MET><ENG> 2 inches</ENG> in diameter for connection to piping or manifold and for inspection purposes.  
Vessel connections for seamless vessels shall be [adapted for and connected to in accordance with <RID>ASME B16.5</RID>] 
[suitable for connection of stainless steel positive mechanical high-pressure threaded type fittings].  Connections 
shall be suitable for pressures specified for vessels.  After fabrication, seamless cylinders shall be normalized 
or liquid-quenched and tempered.</TXT><BRK/>
<BRK/></SPT>
</SPT><SPT><TTL>2.3   DESIGN AND FABRICATION</TTL><BRK/>
<BRK/>
<TXT>Design and fabrication of vessels shall conform to <RID>ASME BPVC SEC VIII D1</RID>, except as modified herein.  Vessels 
shall be welded cylinders or spheres, seamless cylinders, or cylinders of multiple-layered or banded construction.  
Vessels shall be suitable for stationary, aboveground [horizontal] [vertical] installation, exposed to atmospheric 
elements.  Capacities of vessels shall be as shown.</TXT><BRK/>
<BRK/>
<SPT><TTL>2.3.1   Design Pressure</TTL><BRK/>
<BRK/>
<TXT>Vessels shall be designed for a pressure of [_____]<MET> kPa</MET><ENG> psig</ENG>.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.3.2   Design Temperature</TTL><BRK/>
<BRK/>
<TXT>Vessels shall be designed for a temperature range of<MET> plus 49 to minus 40 degrees C</MET><ENG> plus 120 to minus 40 degrees 
F</ENG>.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.3.3   Outlets</TTL><BRK/>
<NTE><BRK/>
<AST/><BRK/>
<NPR>NOTE:  The drawings will indicate high-pressure threaded type fittings where 
required, based on design pressure.</NPR><BRK/>
<AST/><BRK/></NTE>
<BRK/>
<SPT><TTL>2.3.3.1   Nozzles</TTL><BRK/>
<BRK/>
<TXT>Nozzles or outlets for welded monobloc, multiple-layered, and banded vessels shall be a minimum of two in number, 
one at each end on the longitudinal centerline for connection to piping or manifold, and for inspection purposes 
and shall have a minimum diameter of<MET> 50 mm</MET><ENG> 2 inches</ENG>.  Nozzles and outlets shall be fully reinforced regardless 
of size.  Flanged outlets shall conform to <RID>ASME B16.5</RID> or to <RID>ASME BPVC SEC VIII D1</RID>.  Nozzles or outlets shall 
be suitable for the pressures specified for vessels.  Material for nozzles, outlets and flanges preferably shall 
be the same as that of the vessel, but may be of any other material that is compatible with vessel material.  
[Where shown, outlets shall be suitable for connection to stainless steel positive mechanical high-pressure threaded 
type fittings.]</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.3.3.2   Manholes and Handholes</TTL><BRK/>
<NTE><BRK/>
<AST/><BRK/>
<NPR>NOTE:  Manholes and handholes for internal inspection of the vessels will be 
specified if required.</NPR><BRK/>
<AST/><BRK/></NTE>
<BRK/>
<TXT>Manholes and handholes shall conform to the requirements of subsections UG-36 through UG-46 of <RID>ASME BPVC SEC VIII D1</RID>
 as applicable.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.3.3.3   Drains and Vents</TTL><BRK/>
<NTE><BRK/>
<AST/><BRK/>
<NPR>NOTE:  Drains and vents to facilitate cleaning of the vessels will be specified 
if required.</NPR><BRK/>
<AST/><BRK/></NTE>
<BRK/>
<TXT>Drains and vents to facilitate cleaning of vessels shall be provided and shall be leakproof.</TXT><BRK/>
<BRK/></SPT>
</SPT><SPT><TTL>2.3.4   Multiple Vessels</TTL><BRK/>
<NTE><BRK/>
<AST/><BRK/>
<NPR>NOTE:  To provide for maximum competition and latitude by the Contractor in 
sizing the pressure vessels, the total volume of each system will be specified 
in cubic feet (water volume) and ample physical space allocated to accommodate 
various arrangements and sizes of pressure vessels.</NPR><BRK/>
<BRK/>
<NPR>The drawings will show the piping connection point both in physical location 
and size.</NPR><BRK/>
<AST/><BRK/></NTE>
<BRK/>
<TXT>Multiple-vessel assemblies shall be manifolded together to furnish required gaseous-storage volume.  Manifold 
shall terminate at the piping connection point as shown.  The total cross-sectional area of manifold piping in 
a system shall be not less than 1.5 times the cross-sectional area of the piping connection point.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.3.5   Structural Attachments</TTL><BRK/>
<BRK/>
<TXT>Permanent structural attachments, including lifting lugs and erection brackets, shall not be welded to vessel 
parts subject to pressure stress, unless otherwise approved.  If approved, such welds shall be full penetration 
and shall have welded layers inspected progressively by the magnetic particle method.  No welding shall be performed 
after final stress relief or hydrostatic testing.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.3.6   Shell and Head Thickness</TTL><BRK/>
<NTE><BRK/>
<AST/><BRK/>
<NPR>NOTE:  If vessels are used for the storage of compressed air, an appropriate 
corrosion allowance on the shell and head thickness will be included.</NPR><BRK/>
<AST/><BRK/></NTE>
<BRK/>
<TXT>Shell and head thickness shall be calculated in conformance with <RID>ASME BPVC SEC VIII D1</RID>.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.3.7   <SUB>Procedure for Welding Vessels and Manifolds</SUB></TTL><BRK/>
<BRK/>
<TXT>Welding procedures shall conform to requirements of <RID>ASME BPVC SEC IX</RID> and to requirements specified below.  Information 
required by recommended Form QW-483, Article IV, of <RID>ASME BPVC SEC IX</RID> shall be submitted for approval.  An inert-gas 
shielded welding process with an inert-gas backup shall be used for the first pass of all manifold welds.  Separate 
qualification tests shall be made on maximum joint thickness of each material and each procedure used in production 
of double-welded butt joints and single-welded joints.  Procedures qualified for thickness greater than those 
specified shall be acceptable without requalification.  Joint design used in test plates shall be the same as 
for joints used in production.  A requalification test shall be made for any change in the nominal weld metal 
composition and for changes in any essential variables listed in <RID>ASME BPVC SEC IX</RID>.  A separate qualification 
test shall be made for each joint design.  For multiple-layered or banded vessels, the tension and guided-bend 
tests shall be performed on inner shell and outer layer thicknesses.  For girth welds between multiple-layered 
shells and heads, the test specimen shall include head material as well as layered shell material.  In addition 
to tests specified in <RID>ASME BPVC SEC IX</RID>, procedure qualification test plates shall be radiographed following the 
same heat-treating procedure used in production.  Using radiographic procedures specified for production welds, 
radiographs shall conform to requirements specified.</TXT><BRK/>
<BRK/>
<SPT><TTL>2.3.7.1   Weld Layer Thickness</TTL><BRK/>
<BRK/>
<TXT>Individual layer thickness of production welds shall not exceed 1.1 times that of individual layer thickness 
deposited in the performance qualification.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.3.7.2   Continuity of Backing Ring</TTL><BRK/>
<BRK/>
<TXT>Backing rings shall be permitted only for circumferential weld joints which, due to access limitations, cannot 
be welded from both sides.  If a backing bar, strap, or ring is used on inside of single buttweld joints, ends 
of backing bar shall be welded to produce a continuous backing element.</TXT><BRK/>
<BRK/></SPT>
</SPT><SPT><TTL>2.3.8   Joint Efficiency</TTL><BRK/>
<BRK/>
<TXT>A joint efficiency not greater than 0.95 shall be used for staggered buttwelded longitudinal seams of multiple-layered 
or banded vessels, provided welds in inner shell and adjacent layer are fully radiographed and the finished weld 
in each of the subsequent layers is fully magnetic-particle inspected and is<MET> 7 mm</MET><ENG> 9/32 inch</ENG> or less in thickness.  
A penetrometer thickness not more than 1 percent of total wall thickness being radiographed shall be used when 
radiographing adjacent layer.  Joint efficiency for other buttwelded seams shall conform to <RID>ASME BPVC SEC VIII D1</RID>
.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.3.9   Pressure Relief Devices</TTL><BRK/>
<BRK/>
<TXT>All vessels, regardless of size or internal pressure, shall be provided with protective pressure relief devices 
conforming to the design requirements of parts UG-125 through UG-136 of <RID>ASME BPVC SEC VIII D1</RID>.</TXT><BRK/>
<BRK/></SPT>
</SPT><SPT><TTL>2.4   TESTING</TTL><BRK/>
<BRK/>
<TXT>The Contracting Officer shall be notified [_____] days before the performance and fabrication tests are to be 
conducted.  Tests shall be performed in the presence of the Contracting Officer.</TXT><BRK/>
<BRK/>
<SPT><TTL>2.4.1   Notched-Bar Impact Tests for Material</TTL><BRK/>
<BRK/>
<TXT>Materials for shells, heads, nozzles, and other vessel parts subject to stress due to pressure shall be impact 
tested at<MET> minus 40 degrees C</MET><ENG> minus 40 degrees F</ENG> in accordance with requirements of <RID>ASME BPVC SEC VIII D1</RID>, with 
the following modifications:</TXT><BRK/>
<BRK/>
<SPT><TTL>2.4.1.1   Impact Specimens</TTL><BRK/>
<BRK/>
<LST>a.  Test Plates for Welded Vessels:  In addition to requirements of <RID>ASME BPVC SEC VIII D1</RID>, one set of 
impact specimens shall be taken from the head-to-shell weld with notch in adjacent head metal in heat-affected 
zone.  Test specimens shall be taken from mid-length of test plates.</LST><BRK/>
<BRK/>
<LST>b.  Multiple-Layered Plate Material:  In multiple-layered vessels which use plates<MET> 10 mm</MET><ENG> 3/8 inch</ENG> or 
less in thickness, exclusive of the inner shell, the requirements for testing plates shall be met by 
testing at least one set of impact specimens for each<MET> 600 mm</MET><ENG> 2 feet</ENG> of cylindrical length of each vessel.</LST><BRK/>
<BRK/>
<LST>c.  Seamless Vessels:  The requirements for testing impact specimens shall be met by testing one set 
of specimens from a test sample of the lot it represents.  A lot shall consist of a maximum of six vessels 
having the same inside diameter and wall thickness in a heat-treat furnace charge from the same heat 
of steel.  Test sample shall be at least<MET> 600 mm</MET><ENG> 24 inches</ENG> long and shall be subjected to the same working, 
normalizing or quenching, and tempering and shall be heated with the lot of production vessels.  Impact 
test specimens shall be cut from the central<MET> 300 mm</MET><ENG> 12 inches</ENG>of the test sample.</LST><BRK/>
<BRK/></SPT>
<SPT><TTL>2.4.1.2   Minimum Impact Value</TTL><BRK/>
<BRK/>
<TXT>In lieu of requirements in <RID>ASME BPVC SEC VIII D1</RID>, each specimen of the set of three<MET> 10 by 10 mm</MET><ENG> 3/8 by 3/8 inch</ENG>
 specimens shall have a specified minimum impact value of<MET> 20 J</MET><ENG> 15 foot pounds</ENG> for material thickness of<MET> 13 mm</MET><ENG>
 1/2 inch</ENG> or greater.  For thinner material, a similar specimen shall be used, except that the dimension along 
the axis of the notch and the specified minimum impact value shall be reduced to the largest possible of:</TXT><BRK/>
<BRK/>
<LST><MET> 7.5 mm and 17 J</MET><ENG> 12.5 foot pounds</ENG> minimum.</LST><BRK/>
<BRK/>
<LST><MET> 5.0 mm and 14 J</MET><ENG> 10 foot pounds</ENG> minimum.</LST><BRK/>
<BRK/>
<LST><MET> 2.5 mm and 7 J</MET><ENG> 5 foot pounds</ENG> minimum.</LST><BRK/>
<BRK/>
<TXT>If the value of only one of the specimen is less than the specified value, a retest will be permitted, in which 
case all three retest specimens shall have an impact value of not less than the specified value.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.4.1.3   Additional Tests of Welded and Seamless Vessels</TTL><BRK/>
<BRK/>
<LST>a.  Materials and weld metal shall be tested at the lowest temperature at which pressure will be applied 
to the vessel, or the design temperature, whichever is lower, and shall meet the following:</LST><BRK/>
<BRK/>
<ITM>(1)  Specimen shall be in accordance with <RID>ASTM A 370</RID> for Charpy Impact Test.</ITM><BRK/>
<BRK/>
<ITM>(2)  Minimum values shall be as given below:</ITM><BRK/>
<BRK/>
<MET><TBL><THD><BRK/>
                                    Base Metal and<BRK/>
                                    Heat-Affected             Weld<BRK/>
          Size of Specimen               Zone                 Metal<BRK/>
                                      (joules)               (joules)<BRK/></THD>
<BRK/>
          10 mm x 10 mm                   41                   34<BRK/>
<BRK/>
          10 mm x 7.5 mm                  34                   27<BRK/>
<BRK/>
          10 mm x 5 mm                    27                   22<BRK/>
<BRK/>
          10 mm x 2.5 mm                  14                   11<BRK/></TBL>
</MET><TBL><ENG><THD><BRK/>
                                    Base Metal and<BRK/>
                                    Heat-Affected             Weld<BRK/>
          Size of Specimen               Zone                 Metal<BRK/></THD>
<BRK/>
          10 mm x 10 mm                   30                   25<BRK/>
<BRK/>
          10 mm x 7.5 mm                  25                   20<BRK/>
<BRK/>
          10 mm x 5 mm                    20                   16<BRK/>
<BRK/>
          10 mm x 2.5 mm                  10                    8</ENG><BRK/>
<BRK/>
If the value of only one of the specimens is less than the specified value, a retest will be permitted, in which 
case all three retest specimens shall have an impact value of not less than the specified value.</TBL><BRK/>
<BRK/>
<LST>b.  For welded vessels, one set of Charpy Tests shall be made with notch located in base metal at least<MET>
 50 mm</MET><ENG> 2 inches</ENG> from weld, one set with notch located in heat-affected zone of shell, and one set with 
notch located in weld metal.</LST><BRK/>
<BRK/>
<LST>c.  For seamless vessels, tests shall be performed on base metal only, in the same quantities as required 
above for seamless vessels.</LST><BRK/>
<BRK/></SPT>
</SPT><SPT><TTL>2.4.2   Mechanical Property Tests</TTL><BRK/>
<BRK/>
<SPT><TTL>2.4.2.1   Welded Vessels</TTL><BRK/>
<BRK/>
<TXT>Two tension tests and one bend test shall be made from each parent plate as rolled from a slab or ingot.  Plates 
which are quenched and tempered by steel supplier shall be tested by performing one bend test from each parent 
plate as rolled from a slab or ingot, and two tension tests from each plate as heat-treated.  In addition, one 
tension test shall be made on each quenched and tempered plate used for vessel shells and heads when the heat-treatment 
is performed by fabricator.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.4.2.2   Seamless Vessels</TTL><BRK/>
<BRK/>
<TXT>One impact specimen tension test shall be made from test sample for each lot.  Test specimen shall be taken from 
the central<MET> 300 mm</MET><ENG> 12 inches</ENG> of test sample.</TXT><BRK/>
<BRK/></SPT>
</SPT><SPT><TTL>2.4.3   Hydrostatic Testing</TTL><BRK/>
<BRK/>
<TXT>Hydrostatic testing shall be performed after fabrication and heat treatment.  Pressure vessels and manifolds 
shall be hydrostatically tested in accordance with <RID>ASME BPVC SEC VIII D1</RID>, except that holding time at test pressure 
shall not be less than 6 hours.</TXT><BRK/>
<BRK/></SPT>
</SPT><SPT><TTL>2.5   INSPECTION AND REPAIR OF DEFECTS</TTL><BRK/>
<BRK/>
<SPT><TTL>2.5.1   Personnel Qualifications</TTL><BRK/>
<BRK/>
<TXT>Radiographic, liquid penetrant and magnetic particle inspections of buttwelded pipe joints and welded vessels 
listed below shall be performed by personnel qualified in accordance with applicable portion of <RID>ASME BPVC SEC V</RID>
 as appropriate.  Certified <SUB>test</SUB> results shall be submitted by the reviewing inspector.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.5.2   Radiography of Buttwelded Pipe Joints</TTL><BRK/>
<BRK/>
<TXT>Buttwelded pipe joints shall be radiographed 100 percent.  Radiographic technique and interpretation shall conform 
to <RID>ASME B31.3</RID>, except as modified.  The negatives and interpretation report shall be submitted for examination 
within 24 hours after taking radiographs.  Unacceptable areas of joints shall be cut out, remade, and reradiographed.  
The negatives shall be accessible for examination by the Contracting Officer.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.5.3   Radiography of Welded Vessels</TTL><BRK/>
<BRK/>
<TXT>Extent of radiography shall be based on joint efficiencies used for design purposes.  Radiographic technique 
and interpretation shall conform to <RID>ASME BPVC SEC VIII D1</RID>.  Radiographic film shall be the fine grain or extra 
fine type.  Radiographic negatives and interpretation shall be submitted for approval at fabricator's plant.  
Unacceptable welds shall be repaired and reradiographed.  A complete set of radiographs and records for each 
vessel or vessel part shall be retained by the manufacturer until the Manufacturer's Data Report has been signed 
by the inspector.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.5.4   Magnetic Particle Inspection</TTL><BRK/>
<BRK/>
<TXT>Except for inside surface of closing girth seam, accessible surfaces of welds, including all layers of multiple-layered 
or banded vessels, shall be magnetic-particle inspected during fabrication in accordance with <RID>ASTM E 709</RID>, using 
dc direct probe only.  In addition, inspection of accessible outside surface of welds shall be made after hydrostatic 
testing.  Swaged ends of seamless vessels shall be magnetic-particle inspected after forming and heat treatment.  
Cracks shall be repaired.  Linear defects, except linear inclusions not exceeding<MET> 6 mm</MET><ENG> 1/4 inch</ENG> for thicknesses 
up to<MET> 19 mm</MET><ENG> 3/4 inch</ENG>, <MET>8 mm</MET><ENG> 1/3 inch</ENG> for thicknesses<MET> 19 mm</MET><ENG> 3/4 inch</ENG> to<MET> 57 mm</MET><ENG> 2-1/4 inches</ENG>, and<MET> 19 mm</MET><ENG> 3/4 inch</ENG> 
for thicknesses over<MET> 57 mm</MET><ENG> 2-1/4 inches</ENG>, shall be repaired.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.5.5   Inspection for Laminations</TTL><BRK/>
<BRK/>
<TXT>Laminations found at edges of plates shall be chipped or ground out to depth of the lamination or<MET> 13 mm</MET><ENG> 1/2 inch</ENG>
, whichever is less, and the resulting groove shall be repaired by welding.  Linear defects<MET> 75 mm</MET><ENG> 3 inches</ENG> or 
less in length which are parallel to plate surface shall not be considered as laminations and are acceptable.  
Linear defects over<MET> 75 mm</MET><ENG> 3 inches</ENG> in length which are parallel to plate surface shall be considered as laminations 
and shall be repaired.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.5.6   Dye Penetrant Inspection</TTL><BRK/>
<BRK/>
<TXT>Piping and seal welds shall be liquid-penetrant inspected at the root and final weld layers.  Cracks and linear 
indications, except minor inclusions, shall be eliminated.  Inspection procedure shall be in conformance with <RID>
ASTM E 165</RID>.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.5.7   Repair of Defects</TTL><BRK/>
<BRK/>
<TXT>Defects shall be repaired in accordance with approved procedures.  Wherever a defect is removed and repair by 
welding is not required, affected area shall be blended into the surrounding surface so as to avoid sharp notches, 
crevices, or corners.  After a defect is removed, and prior to making repairs, the area shall be examined by 
suitable methods to ensure that the defect has been eliminated.  After repairs have been made, the repaired area 
shall be re-examined by the same methods that were originally required for the area.  Any indication of a defect 
shall be regarded as a defect unless reevaluation by nondestructive methods and/or by surface conditioning shows 
that no unacceptable defect is present.</TXT><BRK/>
<BRK/></SPT>
</SPT><SPT><TTL>2.6   <SUB>CLEANING</SUB></TTL><BRK/>
<BRK/>
<SPT><TTL>2.6.1   Internal Cleaning</TTL><BRK/>
<NTE><BRK/>
<AST/><BRK/>
<NPR>NOTE:  If this specification is used for the procurement of vessels, but not 
for installation, the time of final inspection will be revised.</NPR><BRK/>
<AST/><BRK/></NTE>
<BRK/>
<TXT>Internal surfaces of each vessel and manifold shall be cleaned until permissible contamination limits are complied 
with and then shall be dried and protected.  Cleaning procedures as necessary to comply with permissible contamination 
limits specified shall be employed.  Cleaning, except during fabrication, shall be performed at place of manufacture 
or at installation site.  Cleaning solvents that contain chlorine shall not be used on stainless steel vessels.  
Inspection and tests will be witnessed by the Contracting Officer at time of final acceptance.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.6.2   Permissible Contamination Limits</TTL><BRK/>
<NTE><BRK/>
<AST/><BRK/>
<NPR>NOTE:  Each individual vessel and its application has to be considered from 
the standpoint of the control system and end use of the product. Permissible 
contamination limits will be inserted to suit requirements.  The limits specified 
will not be more stringent; for economical reasons, the limits will be relaxed 
wherever possible.</NPR><BRK/>
<AST/><BRK/></NTE>
<BRK/>
<TXT>Permissible contamination limits for vessels and manifolds shall not exceed the following:</TXT><BRK/>
<BRK/>
<LST>a.  No hydrocarbon as evidenced by visual and ultraviolet light inspections.</LST><BRK/>
<BRK/>
<LST>b.  No solid or fibrous particle concentration greater than<MET> [54] [_____] mg/square m</MET><ENG> [5] [_____] mg/psf</ENG>
 as measured in effluent on final rinse or [10] [_____] ppm by weight of sample.</LST><BRK/>
<BRK/>
<LST>c.  No particles greater than [150] [_____]-micrometer size.</LST><BRK/>
<BRK/>
<LST>d.  No fibers greater in size than [150] [_____]-micrometer diameter by [1,000] [_____]-micrometer length.</LST><BRK/>
<BRK/></SPT>
<SPT><TTL>2.6.3   Miscellaneous Requirements</TTL><BRK/>
<BRK/>
<SPT><TTL>2.6.3.1   Nominal-Rated Filters</TTL><BRK/>
<BRK/>
<TXT>Filters shall remove 98 percent by weight of particles whose two smallest dimensions are greater than openings 
in filter media.  Filters made by powder metallurgy processes shall not be used.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.6.3.2   Clean Water</TTL><BRK/>
<BRK/>
<TXT>Water shall be color free and shall contain no visible suspended particles or hydrocarbons.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.6.3.3   Dry Air</TTL><BRK/>
<BRK/>
<TXT>Air shall be oil-free air which has been processed through a dehydrator so that the dew point is<MET> minus 53 degrees 
C</MET><ENG> minus 63.5 degrees F</ENG> at<MET> 101 kPa (one atmosphere)</MET><ENG> one atmosphere</ENG> or a maximum of 26.3 ppm water vapor by volume.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.6.3.4   Nitrogen</TTL><BRK/>
<BRK/>
<TXT>Nitrogen  shall have been filtered through a 40-micrometer absolute-rated filter with an element constructed 
of stainless steel dutch twill weave.  Filter shall be cleaned so as not to contaminate the system in excess 
of filter rating.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.6.3.5   Hydrocarbon</TTL><BRK/>
<BRK/>
<TXT>Hydrocarbon shall be a combustible compound containing carbon and hydrogen.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.6.3.6   Solid Particle</TTL><BRK/>
<BRK/>
<TXT>Solid particle shall be solid material which cannot be classified as a fiber.  Size of a solid particle shall 
be determined by longest dimension.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.6.3.7   Fiber</TTL><BRK/>
<BRK/>
<TXT>Fiber shall be a threadlike structure composed of any material.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.6.3.8   White Metal</TTL><BRK/>
<BRK/>
<TXT>"White metal" shall have surface of a gray white, uniform metallic color. Surface, when viewed without magnification, 
shall be found free of visible mill scale, rust, corrosion, oxides, paint, or other foreign matter.</TXT><BRK/>
<BRK/></SPT>
</SPT><SPT><TTL>2.6.4   Cleaning Procedures</TTL><BRK/>
<BRK/>
<TXT>Cleaning procedures shall be as follows, and additional procedures shall be employed as necessary to comply with 
the permissible contamination limits.</TXT><BRK/>
<BRK/>
<SPT><TTL>2.6.4.1   Cleaning During Fabrication</TTL><BRK/>
<BRK/>
<TXT>During vessel fabrication, surfaces and welds of vessels and manifolds which will be exposed to gas shall be 
thoroughly cleaned to white metal. Wire brushes used on stainless steel shall be of stainless steel.  Grinding 
discs that have been used on carbon steel shall not be used on stainless steel vessels.  Descaling may be accomplished 
prior to welding of final seam.  When performed after cleaning, stress relieving shall be performed using an 
inert gas within the vessel.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.6.4.2   After Cleaning</TTL><BRK/>
<BRK/>
<TXT>After cleaning, surfaces shall be treated to inhibit rust.</TXT><BRK/>
<BRK/></SPT>
</SPT><SPT><TTL>2.6.5   Drying</TTL><BRK/>
<BRK/>
<TXT>Drying of vessels shall be by heating or vacuum evacuation.  Manifolds shall be dried by purge with gaseous nitrogen 
or dry air at a minimum of<MET> 60 degrees C</MET><ENG> 140 degrees F</ENG>.  Vessels and manifolds shall be considered dry when the 
dew point apparatus shows that the purging medium has a dew point no higher than the dew point of influent gas 
which is not above<MET> minus 53 degrees C</MET><ENG> minus 63.5 degrees F</ENG> at<MET> 101 kPa (one atmosphere)</MET><ENG> one atmosphere</ENG> or 26.3 
ppm water vapor by volume.  If vacuum evacuation is used, vessel shall be considered dry when pressure is maintained 
at<MET> 1.69 kPa (0.5 inch of mercury absolute)</MET><ENG> 0.5 inch of mercury absolute</ENG> for a minimum of 5 minutes at a temperature 
of<MET> 15.6 degrees C</MET><ENG> 60 degrees F</ENG> or higher temperature or at such lower pressure which is 96 percent of the vapor 
pressure of water for the vessel temperature.  For example, for a vessel at<MET> 4 degrees C</MET><ENG> 40 degrees F</ENG> a pressure 
of<MET> 804 Pa (0.238 inch of mercury absolute)</MET><ENG> 0.238 inch of mercury absolute</ENG> shall be maintained for 5 minutes.  
Dry gas used for purging and drying shall be filtered through a 10-micron nominal rated filter.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.6.6   Testing of Cleaned Vessels and Manifolds</TTL><BRK/>
<BRK/>
<TXT>Tests during or after cleaning shall be conducted so as not to contaminate vessels or manifolds.  Should testing 
contaminate vessels and manifolds, recleaning shall be performed.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.6.7   Inspection</TTL><BRK/>
<BRK/>
<TXT>Each vessel and manifold shall be inspected for compliance with permissible contamination limits specified herein.  
Certified results of such inspections shall be submitted for approval.  Inspections, tests, and sampling shall 
be performed in the order listed below.  Any vessel or manifold which is rejected in any one of these inspection 
procedures shall be recleaned or reworked to the extent necessary to meet requirements specified.</TXT><BRK/>
<BRK/>
<SPT><TTL>2.6.7.1   Inspection No. 1, Final Rinse</TTL><BRK/>
<BRK/>
<TXT>During final rinse and prior to drying operation, a 1-liter sample of effluent shall be examined by Millipore 
method or equivalent method in accordance with <RID>SAE ARP598</RID>.  For this purpose, rinse shall be performed using 
clean water and a pressure spray nozzle on interior surfaces to ensure dislodgement of particles.  Effluents 
containing contamination in excess of permissible contamination limits shall be cause for recleaning and reinspection.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.6.7.2   Inspection No. 2, Visual</TTL><BRK/>
<BRK/>
<TXT>Vessels and manifolds shall be examined for evidence of corrosion products including rust, metal chips, scale, 
weld scale, oil, grease, paints, preservatives, decals, or other foreign matter.  Special devices such as inspection 
mirrors or bore scopes shall be used to visually examine inaccessible areas of vessels or manifolds.  Contamination 
in excess of permissible contamination limits shall be cause for recleaning and reinspection.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.6.7.3   Inspection No. 3, Ultraviolet Light</TTL><BRK/>
<BRK/>
<TXT>Visual inspection with aid of an ultraviolet light shall be accomplished on accessible surfaces to determine 
the presence of petroleum type hydrocarbons.  Wipe pads shall also be inspected by ultraviolet light. Inspectors 
shall be qualified to use the ultraviolet light.  Contamination in excess of permissible contamination limits 
shall be cause for recleaning and reinspection.  Ultraviolet light used for this inspection and light-intensity 
meter shall conform to the following:</TXT><BRK/>
<BRK/>
<LST>a.  Light source shall be 100-watt spot mercury and bulb<MET> 250 to 370 nanometers (2500 to 3700 Angstrom 
units)</MET><ENG> 2500 to 3700 Angstrom units</ENG>.</LST><BRK/>
<BRK/>
<LST>b.  Transformer shall meet the recommendations of bulb manufacturer.</LST><BRK/>
<BRK/>
<LST>c.  Filter shall be approximately<MET> 127 mm</MET><ENG> 5 inches</ENG> in diameter, convex and round.</LST><BRK/>
<BRK/>
<LST>d.  Bulb shall be replaced when intensity of ultraviolet light through filter is less than 550 microwatts 
per square centimeter when measured<MET> 600 mm</MET><ENG> 24 inches</ENG> from outside surface of filter, or after 500 hours 
of use, whichever occurs first.</LST><BRK/>
<BRK/></SPT>
<SPT><TTL>2.6.7.4   Inspection No. 4, Wipe Test</TTL><BRK/>
<BRK/>
<TXT>Wipe test shall be made at each end of each cleaned section of pipe and on interior surfaces of vessels and manifolds 
which are accessible with a probe.  Clean filter paper shall be used.  Interior surfaces are to be wiped on a 
random basis or as indicated by the results of visual inspection.  Test shall consist of a linear movement of 
filter paper over a distance approximately<MET> 600 mm</MET><ENG> 2 feet</ENG> long when large areas are being tested.  Smaller areas, 
such as manifold ends, shall receive a full circular wipe.  Filter paper shall then be examined under clean-room 
conditions.  Contamination in excess of permissible contamination limits shall be cause for recleaning and reinspection.</TXT><BRK/>
<BRK/></SPT>
</SPT></SPT><SPT><TTL>2.7   SEALING</TTL><BRK/>
<BRK/>
<SPT><TTL>2.7.1   Seals</TTL><BRK/>
<BRK/>
<TXT>Vessels and manifolds shall be sealed immediately after passing the cleaning inspections.  Seals shall be tight 
enough to prevent contamination and shall be protected so that they will not be broken or warped.  Tape for sealing 
procedures shall not leave any residue on connections when removed.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.7.2   Flanged Openings</TTL><BRK/>
<NTE><BRK/>
<AST/><BRK/>
<NPR>NOTE:  Comparable type closures will be specified for other type connections.</NPR><BRK/>
<AST/><BRK/></NTE>
<BRK/>
<TXT>Flanged openings shall be sealed with a suitable full-face blank gasket<MET> 3.2 mm</MET><ENG> 1/8 inch</ENG> thick or disk at least<MET>
 1.6 mm</MET><ENG> 1/16 inch</ENG> thick consisting of polytetrafluorethylene or other nonflammable, noncontaminating material 
and a bolted blank flange of aluminum or corrosion-resisting steel at least<MET> 6 mm</MET><ENG> 1/4 inch</ENG> thick.  Stainless steel 
bolts shall be used in contact with stainless steels.  Cadmium-plated bolts maybe used in contact with aluminum 
but shall not be used in contact with stainless steels.  A bolt correctly torqued to correspond to particular 
blank flange and gasket design shall be placed in each bolt hole.  Gaskets and flanges shall be cleaned as specified.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.7.3   Threaded Openings</TTL><BRK/>
<BRK/>
<TXT>Threaded openings shall be sealed with appropriately cleaned caps or plugs made of corrosion-resisting steel.</TXT><BRK/>
<BRK/></SPT>
</SPT><SPT><TTL>2.8   CERTIFICATE</TTL><BRK/>
<BRK/>
<TXT>Certificate of inspection indicating conformance to requirements specified shall be attached to each item.  Certificate 
shall show the date of inspection and the signature of the Contractor's inspector.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.9   PRESSURIZING</TTL><BRK/>
<BRK/>
<TXT>Vessels shall be pressurized to<MET> 103 kPa</MET><ENG> 15 psig</ENG> with nitrogen immediately following cleaning inspections and 
sealing of vessels.  Vessels shall be maintained at positive pressure up to and during the time of final acceptance.  
Vessels shall be equipped with a shutoff valve and gauge for pressurizing.  The gauge shall be capable of<MET> 103 
kPa</MET><ENG> 15 psig</ENG> minimum with<MET> 10 kPa</MET><ENG> 1.5 psig</ENG> increments between<MET> 0 to 34 kPa</MET><ENG> 0 to 5 psig</ENG>.  A protective metal cover 
shall be provided around the gauge and valving.  Complete loss of pressure shall be cause for reinspection and 
recleaning as necessary to meet permissible contamination limits by and at the expense of the Contractor.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.10   PAINTING</TTL><BRK/>
<BRK/>
<SPT><TTL>2.10.1   Exterior Surfaces</TTL><BRK/>
<BRK/>
<TXT>Exterior surfaces of all vessels, including supports but excluding stainless steel surfaces, shall be cleaned 
and painted in the shop.  Abraded or corroded spots shall be wire brushed and touched up with the same material 
as the paint coat.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.10.2   Cleaning and Preparation of Surfaces</TTL><BRK/>
<BRK/>
<TXT>Exterior surfaces shall be cleaned before applying paint.  Oil, grease, dirt, loose dust, loose mill scale, and 
other foreign substances shall be removed.  Removal of oil and grease shall be accomplished before mechanical 
cleaning is started, using mineral spirits or other paraffin-free solvents having a flash point higher than<MET> 37 
degrees C</MET><ENG> 100 degrees F</ENG>.  Cleaning shall be accomplished with clean cloths, fluid emulsions, steam, flame cleaning, 
high-speed power wire brushing, blast cleaning, or other approved methods.  Use of chipping tools that produce 
cuts, burrs, and other forms of excessive roughness will not be permitted.  Tight mill scale that cannot be removed 
by applying a sharp knife to any edge and minor amounts of residual rust not removable except by thorough blast 
cleaning will be permitted.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>2.10.3   Painting of Surfaces</TTL><BRK/>
<BRK/>
<TXT>A primer coat of paint conforming to <RID>SSPC Paint 25</RID> shall be applied to exterior surfaces of the vessel.  Vessel 
shall be finished with two coats of gray enamel conforming to <RID>SSPC Paint 21</RID>.  Paint shall be applied under dry 
and dust-free conditions when an ambient temperature is not below<MET> 4 degrees C</MET><ENG> 40 degrees F</ENG>.  Painting shall be 
done so as to produce an even film of uniform thickness.  The three-coat paint system shall be applied so that 
their dry film thickness at any point shall be not less than<MET> 0.10 mm</MET><ENG> 4.0 mils</ENG>, with the primer having a minimum 
dry film thickness of<MET> 0.04 mm</MET><ENG> 1.5 mils</ENG>.  Edges, corners, crevices, and joints shall be thoroughly cleaned and 
painted.</TXT><BRK/>
<BRK/></SPT>
</SPT></PRT><PRT><TTL>PART 3   EXECUTION</TTL><BRK/>
<BRK/>
<SPT><TTL>3.1   FOUNDATIONS</TTL><BRK/>
<BRK/>
<TXT>Foundations shall be designed by the Contractor.  Design shall be based on the soils investigation provided by 
the Government.  Any additional information required shall be specified by the Contractor and obtained by the 
Government.  Foundations for the pressure vessel [and manifold] shall be constructed of<MET> [21] [_____] MPa</MET><ENG> [3000] 
[_____] psi</ENG> concrete, reinforced where necessary, and constructed in conformance with the applicable requirements 
of Section <SRF>03 31 00.00 10</SRF> CAST-IN-PLACE STRUCTURAL CONCRETE, except as shown or specified herein.</TXT><BRK/>
<BRK/>
<SPT><TTL>3.1.1   Excavation, Filling, and Grading</TTL><BRK/>
<BRK/>
<TXT>Excavating, filling, and grading shall conform to the applicable requirements of Section <SRF>31 00 00</SRF> EARTHWORK.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>3.1.2   Anchor Bolts</TTL><BRK/>
<BRK/>
<TXT>Anchor bolts shall be set accurately and shall be of adequate length to install the pressure vessel.  When embedded 
in concrete, anchor bolts shall be provided with plates welded on the head and shall be protected against damage 
until the equipment is installed.</TXT><BRK/>
<BRK/></SPT>
</SPT><SPT><TTL>3.2   <SUB>INSTALLATION</SUB></TTL><BRK/>
<BRK/>
<SPT><TTL>3.2.1   Equipment</TTL><BRK/>
<BRK/>
<TXT>All tanks and equipment shall be installed in accordance with fabricator's instructions and recommendations.  
All vessels shall be bolted in place on concrete foundations.  Care shall be exercised during the placement of 
vessel on foundation so as not to scratch or dent vessel, or crack foundation.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>3.2.2   Piping</TTL><BRK/>
<BRK/>
<TXT>All interconnecting piping shall be assembled in accordance with fabricator's drawings and instructions.  All 
piping shall conform to the requirements of <RID>ASME B31.3</RID>.  Adequately support interconnecting piping to avoid producing 
large stresses on the pipe or the vessel nozzles.  Pipe hangers and supports shall conform to <RID>MSS SP-58</RID>.  Piping 
supports shall allow for movement of the pipe from thermal expansion or contraction.  Pipe support spacing and 
installation shall conform to the requirements of <RID>MSS SP-69</RID>.</TXT><BRK/>
<BRK/></SPT>
</SPT><SPT><TTL>3.3   <TST>FIELD TESTING</TST></TTL><BRK/>
<BRK/>
<TXT>Upon completion of all related work and prior to acceptance, the Contractor shall subject the pressure vessel 
and associated piping and instrumentation to a pressure test to demonstrate system performance.  Notify the Contracting 
Officer [_____] days prior to conducting the test.  The Contracting Officer shall be present during the testing.</TXT><BRK/>
<BRK/>
<SPT><TTL>3.3.1   <TST>Testing Materials</TST></TTL><BRK/>
<BRK/>
<TXT>Furnish all equipment, instruments, materials, and personnel required to perform the test.  The Government will 
supply the utilities to perform the test such as [nitrogen,] [water,] [and] electric power.</TXT><BRK/>
<BRK/></SPT>
<SPT><TTL>3.3.2   <TST>Procedure</TST></TTL><BRK/>
<BRK/>
<TXT>The test medium shall be clean, dry nitrogen.  Piping test pressure shall be not less than 1.2 nor more than 
1.5 times the design pressure.  The test pressure shall be continuously maintained for a minimum of 10 minutes, 
and the required test procedure shall be in accordance with <RID>ASME B31.3</RID>.  To pass the pressure test, the piping 
system shall show no evidence of leaking at all joints and connections by soap bubble or equivalent method.  
If system does not pass the pressure test, the problem will be corrected and the system will be retested.  Any 
retesting will be performed by the Contractor at the Contractor's expense.  If piping test pressure is above 
the pressure vessel test pressure, the pressure vessel will be isolated from the piping test.</TXT><BRK/>
<BRK/></SPT>
</SPT><SPT><TTL>3.4   TOUCHUP PAINTING</TTL><BRK/>
<BRK/>
<TXT>Perform touchup painting to equipment [and piping manifold] as required from the inspection of the Contracting 
Officer. Painting materials and procedure shall conform to the requirements of paragraph PAINTING.</TXT><BRK/>
<BRK/></SPT>
</PRT>    <END/><BRK/></SEC>