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2021-09-20_REVISION - M2012032
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2021-09-20_REVISION - M2012032
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Last modified
12/28/2024 2:25:49 PM
Creation date
9/20/2021 7:49:25 PM
Metadata
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Template:
DRMS Permit Index
Permit No
M2012032
IBM Index Class Name
REVISION
Doc Date
9/20/2021
Doc Name
Adequacy Review Response #2
From
Ouray Silver Mines, Inc.
To
DRMS
Type & Sequence
TR16
Email Name
LJW
Media Type
D
Archive
No
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AFL INDUSTRIES,INC. <br /> RIVIERA BEACH,FLORIDA <br /> SERVICE OPERATION PRINCIPLE Page 1 OF 4 <br /> MANUAL <br /> PRODUCT: VERTICAL TUBE COALESCING <br /> SEPARATOR-ALL MODELS <br /> BASIC OPERATING PRINCIPLE <br /> In a nearly motionless state,free oil and water separate because of the natural effects of gravity.Water,being heavier,will settle, <br /> and oil,being lighter,will rise.Solids,depending on their density and velocity,will also settle out due to gravity.AFL's gravity <br /> separators utilize this natural process in a carefully engineered structure.The separators provide a volume through which polluted <br /> water and solids flow.The oil accumulates on the top and can be skimmed off,the settleable solids collect on the floor for periodic <br /> removal,and the water passes through and is discharged.See assembly drawing in this brochure provided on the unit.The gravity <br /> separator model which your company has purchased is a Vertical Tube Coalescer Separator(VTC).The following is a description <br /> of the various VTC components and how they function in the system. See Fig. 1.0 for typical flow pattern and components. <br /> INLET CHAMBER <br /> The basic purpose of the inlet chamber is to remove gross solids and trash from the influent stream and to distribute the flow <br /> evenly throughout the separating chambers. <br /> INLET PIPE <br /> The inlet pipe(s)provided with elbows,direct the flow towards the separator bottom in order to reduce channeling and turbulence <br /> in the separating chamber.No flow control device is provided.As a result,care must be taken to insure that a flow rate greater <br /> than the designed flow rate is not fed to the unit. If larger than designed flow rates are permitted to enter the VTC,less time is <br /> available to separate the oil and water.The result can be a poor quality effluent. <br /> INLET SLUDGE/DIFFUSION BAFFLE <br /> The inlet sludge/diffusion baffle separates the inlet, and sludge chambers,and redirects the flow to the middle of the vertical <br /> coalescing tubes,thereby, forcing the solids to accumulate on the floor.The gross solids accumulated are removed through a <br /> sludge draw-off(optional)pipe or by dropping a pump suction hose through a manway. <br /> SEPARATING CHAMBER <br /> The separating chamber is essentially an area where polluted water stands nearly motionless for a period of time so <br /> gravity separation of oil,water and solids can occur. In the VTC,this chamber is filled with oleophilic,oil attracting Delta- <br /> Tubes. These AFL designed Delta-Tubes distribute the flow throughout the entire width and depth of the chamber and greatly <br /> reduce the turbulence,thereby,enhancing oil and water separation.The coalescing action of the Delta-Tubes provides additional <br /> assistance in separating oil and water. Small oil globules are attracted to the tubes,combine with other globules,and then float <br /> through the Delta-Tubes to the water surface. <br /> SLUDGE CHAMBER <br /> The sludge chamber is designed to contain settleable solids which have collected on the separator floor and prevent them <br /> from passing under the oil retention baffle and out of the VTC.The sludge will build up on the floor of the chamber and can be <br /> removed through the sludge draw-offs stem installed b AFL in Below Ground and Flush to Grade or pumped <br /> g g Y Y Y P P <br /> or gravity flow through sludge drain valves provided by AFL in Above Ground units. <br /> SUPERSEDES: I-O-M: 2.00-1 <br />
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