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SITE INFORMATION AND CORRESPONDENCE CASE 2
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SITE INFORMATION AND CORRESPONDENCE CASE 2
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Last modified
8/5/2019 1:25:48 PM
Creation date
8/5/2019 10:50:52 AM
Metadata
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Template:
EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
SITE INFORMATION AND CORRESPONDENCE
FileName_PostFix
CASE 2
RECORD_ID
PR0521881
PE
2960
FACILITY_ID
FA0014865
FACILITY_NAME
CALIFORNIA NATURAL PRODUCTS
STREET_NUMBER
1250
Direction
E
STREET_NAME
LATHROP
STREET_TYPE
RD
City
LATHROP
Zip
95330
APN
19804001
CURRENT_STATUS
01
SITE_LOCATION
1250 E LATHROP RD
QC Status
Approved
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EHD - Public
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WASTE DISCHARGE REQUIREMENTS ORDER NO. -2- <br /> PAT MITCHELL AND CALIFORNIA NATURAL PRODUCTS <br /> WASTEWATER TREATMENT AND DISPOSAL FACILITY <br /> SAN JOAQUIN COUNTY <br /> 8. Products for retail sale are packaged on site. Aseptic packaging under sterile conditions requires <br /> heated water from boilers and regular acid/caustic tank and equipment cleaning cycles. Reverse <br /> Osmosis (RO) is used to treat boiler feed water. RO reject water with a total dissolved solids <br /> concentration of approximately 1,200 mg/l is discharged to the process wastewater discharge tank. <br /> 9. Caustic and acid cleaning solutions are recycled several times prior to discharge to the wastewater <br /> system. Ozone has recently been added to the processing plant for sanitation. <br /> 10. The specific conductance of the water supply, before use by the Discharger, ranges from 470 <br /> µmhos/cm to 660 µmhos/cm. There is approximately a three-fold increase in mineralization in <br /> wastewater. The Discharger is currently developing a plan to separate the acid/caustic cleaning <br /> waste stream from the rest of the wastewater and manage it by contracting with an off-site disposal <br /> firm. <br /> 11. Process and cleanup wastewater is piped to a central collection sump where it is pumped to the <br /> treatment system. <br /> 12. Wastewater generated in the processing plant is characterized by a high organic matter and solids <br /> content. It is anticipated that the average concentrations of analytes in the process wastewater and <br /> treated wastewater are as follows: <br /> Constituent Units Untreated Wastewater Treated Wastewater 2 <br /> Biochemical Oxygen mg/l 2,205 300 mg/1 <br /> Chemical Oxygen Demand mg/l 5,287 500 mg/l <br /> Electrical Conductivity mg/l 1,550 1,550 µmhos/cm <br /> Total Dissolved Solids mg/1 2,190 2,190 mg/l <br /> Fixed TDS mg/1 1,279 1,279 mg/l <br /> Total Nitrogen mg/l 49.3 40 mg/1 <br /> pH Standard 8.6 7.7 <br /> 1 Untreated wastewater data from Wastewater Capacity Plan, 17 January 2000,prepared by B.Dickson. <br /> Z Treated wastewater data from RWD. <br /> 13. CNP's treatment of process wastewater consists of screening using a rotary screen and two 100- <br /> micron stainless steel parabolic screens; holding/recycle tank; pH control; Dissolved Air Flotation <br /> (DAF) clarifier; a 45-foot diameter, 20-foot high trickling filter; and a 600 gallon per minute <br /> (gpm) lamella separator with flocculent metering system. Prior to discharge, the wastewater is <br /> stored in a 13,000 gallon tank. <br /> 14. The trickling filter operates at 2,500 gpm. Wastewater is recycled approximately ten times <br /> through the filter. Because the process wastewater is high in BOD and low in nitrogen, the <br /> Discharger adds ammonium nitrate to the wastewater to optimize BOD removal in the trickling <br /> filter. <br /> 15. Wastewater samples are collected by a time composite sampling device which collects a 100-m1 <br /> sample every one-half hour from the 13,000 gallon discharge tank. <br /> CWga_RLAtiNC.I N.�AJ NM1NDPIYi. <br />
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