﻿<?xml version='1.0' encoding='UTF-8'?><rss version="2.0" xmlns:dc="http://purl.org/dc/elements/1.1/"><channel><title>Water Environment Federation (WEF) Discussion Forums / Academic and Student Issues / Archives / Archived Forum Topics  / Grit System Design / Latest Posts</title><generator>Water Environment Federation (WEF) Discussion Forums</generator><description>Water Environment Federation (WEF) Discussion Forums</description><link>http://www.wef.org/TechnicalDiscussions/</link><webMaster>jfuller@wef.org</webMaster><lastBuildDate>Sat, 06 Sep 2008 23:07:42 GMT</lastBuildDate><ttl>20</ttl><item><title>RE: Grit System Design</title><link>http://www.wef.org/TechnicalDiscussions/Topic6487-5-1.aspx</link><description>I will have a go as well. The typical performance numbers are 95% removal of 100 mesh particles at peak flow. Typical settling velocities for 50 mesh particles is 9.6 ft/min and 2.5 ft/min for 100 mesh.&lt;/P&gt;&lt;P&gt;I don't quite know what you are looking for , but i hope this helps.&lt;/P&gt;&lt;P&gt;Regards&lt;/P&gt;&lt;P&gt;TerryF</description><pubDate>Sun, 02 Sep 2007 17:16:25 GMT</pubDate><dc:creator>TerryF</dc:creator></item><item><title>RE: Grit System Design</title><link>http://www.wef.org/TechnicalDiscussions/Topic6487-5-1.aspx</link><description>Since no one else has bit on this one, I'll take a stab.&lt;br&gt;&lt;br&gt;My MOP 8 is older (1975), and I don't have the table that you reference.  But, I do have a table 9-I, titled: Theoretical Maximum Overflow Rates for Grit Chambers.  The data include "settling velocity of quartz particles" and "theoretical maximum permissible overflow rates for substantially complete removal," for various "grit sizes."&lt;br&gt;&lt;br&gt;In what way are you to evaluate the operation of the grit removal system?&lt;br&gt;&lt;br&gt;The purpose of a grit removal system is to remove as much of the "non-putrescable (sp?)" material, while allowing the biologically-treatable stuff to be carried over for removal in the primaries.  If an entirely "real world" evaluation is desired, I would guess performing tests on the "grit" already being removed might be needed.  Perhaps more knowledgeable folks that deal with grit removal on a regular basis might chime in here.</description><pubDate>Sun, 02 Sep 2007 13:43:06 GMT</pubDate><dc:creator>Jeff Naumann</dc:creator></item><item><title>Grit System Design</title><link>http://www.wef.org/TechnicalDiscussions/Topic6487-5-1.aspx</link><description>&lt;P class=MsoNormal style="MARGIN: 0in 0in 0pt"&gt;&lt;FONT face="Times New Roman" color=#000000 size=3&gt;Hello,&lt;/FONT&gt;&lt;/P&gt;&lt;P class=MsoNormal style="MARGIN: 0in 0in 0pt"&gt;&lt;?xml:namespace prefix = o ns = "urn:schemas-microsoft-com:office:office" /&gt;&lt;o:p&gt;&lt;FONT face="Times New Roman" color=#000000 size=3&gt; &lt;/FONT&gt;&lt;/o:p&gt;&lt;/P&gt;&lt;P class=MsoNormal style="MARGIN: 0in 0in 0pt"&gt;&lt;FONT face="Times New Roman" color=#000000 size=3&gt;I have been asked to review and evaluate the operation of a grit facility that employs three square detritus tanks to treat a municipal wastewater.&lt;SPAN style="mso-spacerun: yes"&gt;  &lt;/SPAN&gt;The only information I have been able to find regarding the initial design parameters are that the facility was intended to use two of the tanks to handle the plant’s daily average flow of 70 MGD, with the third as a stand-by, or in-use to handle, a design peak flow of 105 MGD.&lt;SPAN style="mso-spacerun: yes"&gt;  &lt;/SPAN&gt;The tanks are 35 ft. square, with a SWD of 4.5 ft, and an overflow rate of 28,600 gpd/ft&lt;SUP&gt;2&lt;/SUP&gt; at average flow.&lt;/FONT&gt;&lt;/P&gt;&lt;P class=MsoNormal style="MARGIN: 0in 0in 0pt"&gt;&lt;o:p&gt;&lt;FONT face="Times New Roman" color=#000000 size=3&gt; &lt;/FONT&gt;&lt;/o:p&gt;&lt;/P&gt;&lt;P class=MsoNormal style="MARGIN: 0in 0in 0pt"&gt;&lt;FONT face="Times New Roman" color=#000000 size=3&gt;I have attempted to evaluate the design protocol for such detritus tanks and I have used the 1992 edition of MOP 8 as a reference.&lt;SPAN style="mso-spacerun: yes"&gt;  &lt;/SPAN&gt;My problem is that no manner what methodology I use to determine particle settling velocity I do not obtain the same results as presented by Table 9.9 in MOP 8.&lt;SPAN style="mso-spacerun: yes"&gt;  &lt;/SPAN&gt;I was hoping someone could shed some light as to the calculation procedures used to develop the data for Table 9.9, or possibly, a reference from which Table 9.9 was obtained.&lt;/FONT&gt;&lt;/P&gt;&lt;P class=MsoNormal style="MARGIN: 0in 0in 0pt"&gt;&lt;o:p&gt;&lt;FONT face="Times New Roman" color=#000000 size=3&gt; &lt;/FONT&gt;&lt;/o:p&gt;&lt;/P&gt;&lt;P class=MsoNormal style="MARGIN: 0in 0in 0pt"&gt;&lt;FONT face="Times New Roman" color=#000000 size=3&gt;Thanks. &lt;/FONT&gt;</description><pubDate>Wed, 29 Aug 2007 11:49:34 GMT</pubDate><dc:creator>Waterman</dc:creator></item></channel></rss>