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ARCHIVED REPORTS LEC APPLICATION FOR CERTIFICATION
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2900 - Site Mitigation Program
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ARCHIVED REPORTS LEC APPLICATION FOR CERTIFICATION
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Last modified
9/26/2019 8:41:30 AM
Creation date
9/25/2019 4:52:39 PM
Metadata
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Template:
EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
ARCHIVED REPORTS
FileName_PostFix
LEC APPLICATION FOR CERTIFICATION
RECORD_ID
PR0516806
PE
2965
FACILITY_ID
FA0012817
FACILITY_NAME
WHITE SLOUGH WATER POLLUTION CONTRO
STREET_NUMBER
12751
Direction
N
STREET_NAME
THORNTON
STREET_TYPE
RD
City
LODI
Zip
95241
APN
05513016
CURRENT_STATUS
01
SITE_LOCATION
12751 N THORNTON RD
P_LOCATION
02
P_DISTRICT
004
QC Status
Approved
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® WorleyParsons <br /> resources&energy <br /> 3.16.1 Design Temperature and Pressure <br /> The design pressure and temperature for piping will be consistent with conditions <br /> established for the design of the associated system. <br /> The design pressure of a piping system will be the maximum of- <br /> The <br /> £The set pressure of a relief valve mounted in the line <br /> • The set pressure of a relief valve installed on equipment that is connected to <br /> the line, adjusted accordingly to account for static head and friction loss <br /> • If the system has no PSV or can be isolated from a PSV, the maximum pressure <br /> upstream equipment can generate (i.e.,pump shutoff pressure). <br /> • The maximum sustained pressure that may act on the system plus 25 psi. <br /> The main and process steam piping design pressures will be in accordance with <br /> applicable codes. All design pressure values will be rounded up to the next 5-psig <br /> increment. <br /> The design temperature of a piping system will be based on: <br /> • The maximum sustained temperature which may act on the system plus 25°F <br /> If a heat exchanger of piece of equipment in which heat is being removed can be taken out <br /> of service or bypassed, then the line downstream of that equipment will be designed for <br /> the resulting higher temperature. <br /> 3.16.2 General Design and Selection Criteria <br /> Piping will be designed in accordance with the requirements of the Code for Pressure <br /> Piping, ASME B31.1-Power Piping, and other codes and standards referenced in Section <br /> 2, Codes and Standards. Pipe stress analysis will be performed in accordance with ASME <br /> B3 1.1. All pipe supports will be suitable to restrain the piping where subjected to <br /> external loads as stipulated by the California Building Code — Seismic and Wind Load <br /> Criteria. Vents and drains will be provided, as service requires. <br /> Material selection will generally be based on the design temperature and service conditions <br /> in accordance with the following: <br /> • Carbon steel piping materials will be specified for design temperatures up to and <br /> including 800°F. <br /> • One and one-quarter percent chromium alloy steel piping materials will be <br /> specified for design temperatures ranging from 805°F to 950°F. 21/4 percent <br /> chromium alloy steel piping may be specified for design temperatures ranging <br /> from 955°F to 1100°F, however, 9 percent chromium alloy steel piping will be <br /> specified for high pressure steam and hot reheat steam systems which have a <br /> design temperature of approximately 1065°F. <br /> Lodi Energy Center 3.3 - 19 LEC AFC <br /> 071508 Rev.A <br />
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