My WebLink
|
Help
|
About
|
Sign Out
Home
Browse
Search
SR0033424_ENG DESIGNED PLAN
EnvironmentalHealth
>
EHD Program Facility Records by Street Name
>
A
>
AIRPORT
>
10948
>
4200 – Liquid Waste Program
>
SR0033424_ENG DESIGNED PLAN
Metadata
Thumbnails
Annotations
Entry Properties
Last modified
2/17/2021 5:01:01 PM
Creation date
2/17/2021 4:48:15 PM
Metadata
Fields
Template:
EHD - Public
ProgramCode
4200 – Liquid Waste Program
FileName_PostFix
ENG DESIGNED PLAN
RECORD_ID
SR0033424
PE
4202
STREET_NUMBER
10948
Direction
S
STREET_NAME
AIRPORT
STREET_TYPE
WY
City
MANTECA
Zip
95336
ENTERED_DATE
4/9/2003 12:00:00 AM
SITE_LOCATION
10948 S AIRPORT WY
P_LOCATION
99
P_DISTRICT
003
QC Status
Approved
Scanner
SJGOV\sshih
Tags
EHD - Public
There are no annotations on this page.
Document management portal powered by Laserfiche WebLink 9 © 1998-2015
Laserfiche.
All rights reserved.
/
189
PDF
Print
Pages to print
Enter page numbers and/or page ranges separated by commas. For example, 1,3,5-12.
After downloading, print the document using a PDF reader (e.g. Adobe Reader).
View images
View plain text
742 CHAPTER 11: Intermittent and Recirculating Packed-Bed Filters <br /> TABLE 11-11 <br /> Typical performance of recirculating filters for BOD and TSS removal` <br /> Filter medium BOD, mg1L TSS, mg/L <br /> Locations C6,mm UC Influent Effluent influent Effluent <br /> Elkton, Oregon 3.5 1.8 141 6 32 6 <br /> Orcas Village,Washington 2.0 1.75 166 4 113 5 <br /> South Prairie,Washington 4.3 1.6 181 4 34 4 <br /> 'Courtesy Orenco Systems,Inc. <br /> Treatment Performance <br /> The removal of BOD in'recirculating filters depends on the loading rate and the <br /> size of the filter medium. Recirculating filters can produce an effluent with less than <br /> 10 mg/L of BOD and TSS when loading rates are less than 5 gal/ft2•d (200 mm/d) <br /> and the medium size is 3 mm or less. Typical removals for BOD are presented in <br /> Table 1141 for a range of filter medium sizes varying from sand to pea gravel. Per- <br /> formance data for the RGF used for the Stonehurst development described above are <br /> presented in Table 11-12. <br /> Recirculating filters can produce a high-quality, partially nitrified effluent. Ni- <br /> trogen removal with recirculating filters is typically 40 to 50 percent, as shown in <br /> TABU 11-12' <br /> Performance data for Stonehurst wastewater treatment system <br /> For the 28-month period from June 1994 through September 1996- Effluent samples taken after <br /> recirculating gravel filter and UV disinfection as shown in Fig. 11-22' <br /> Total Observed values <br /> Sample number of <br /> reporting samples Arithmetic Geometric <br /> Constituent' Unit period$ to date Range mean mean Median <br /> BODS mg1L Monthly 56 Oto c5 c5 <5 <br /> COD mg/L . Monthly 120 1.0-18.0 4.7 5.0 <br /> TSS mg/L Monthly 118 2.0-15.0 5.0 4.9 <br /> pH Unitless Monthly 120 6.96-8.65 t a 7.61 <br /> Total coliform MPN/100 mL Monthly 118 <2--12.5 ° <2 <br /> NH4 mg/L Quarterly 9 0-15 1 0.0 <br /> IV03 mg/L Quarterly 9 '-3.55--37.0 12.5 12.2 <br /> TKN ' mg/L Quarterly 9 0-3 ' 0.4 <br /> Oil and grease mg/L Quarterly 9 0--12 ' 0.0 <br /> TDS mg/L Quarterly 9 340-770 630 656 <br /> EC p.mhos/cm Quarterly 9 433-1200 894 1000 <br /> 'Crites et at.(1997). <br /> t TDS = total dissolved solids,EC=electrical conductivity. <br /> =Monthly values for BODS are based on an average of two samples per month.Monthly values for TSS,COD,pH,and total <br /> conform are based on an average of at least four samples per month. <br /> 4 Mean values cannot be reported for pH,which is a logarithmic function,and total coliform,which is based on a Poisson dis- <br /> tribution. <br /> 'Unable to define nature of distribution,because of the number of zero values reported. <br />
The URL can be used to link to this page
Your browser does not support the video tag.