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91 Cards in this Set
- Front
- Back
Most sewer pipes are laid at a slope steep enough to maintain a wastewater flow of |
2.0 fps (two feet per second) |
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A grit channel is designed to provide a flow-through velocity of |
1 fps ( one foot per second) |
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Manholes are placed every ______ to _____ feet to allow for inspection and cleaning of the sewer |
300 to 500 |
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List three types of sewers |
Sanitary sewer, storm sewer and combined sewer |
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Sewer inflow is |
A direct discharge into the sewer |
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Sewer inflow is |
A direct discharge into the sewer |
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Sewer infiltration is |
Seepage through defective or cracked pipes, pipe joints, connections or manholes. It leaks into the sewer itself. |
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Aereated grit chambers use |
Compressed air added through diffusers. |
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Most common flow measuring device at the plants headworks |
A parshall flume |
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A measuring device used in open channels is a |
Weir. The flow over the weir is determined by the depth of water going through the opening. |
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Flow velocity through primary treatment (sedimentation) is about |
.03 fps |
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Primary clarifiers are usually designed to provide ___ to ___ hours detention time |
1.5 to 2 hours |
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Removal of solids in a primary clarifier will reduce the (BOD) of the waste approximately ___ percent |
30 |
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A detention time of 2 hours in a primary clarifier will remove approximately ___ percent of suspended solids |
60% |
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Two processes used universally for biological treatment are the |
Trickling filter and the activated sludge |
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Trickling filters are designed to remove ___ to ___ of the bod-causing wastes and suspended solids present in the influent |
70 to 80% |
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Activated sludge plants are capable of bod and suspended solids reduction of ___ to ___ percent |
90 to 99% |
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By the time waste reaches the end of an activated sludge aeration tank usually ___ to ___ hours, most of the waste has been used by the bacteria |
4 to 8 hrs |
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Two types of bacteria are present in an anaerobic digester ______ and ______ . |
Acid formers and gas formers |
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Two types of bacteria are present in an anaerobic digester ______ and ______ . |
Acid formers and gas formers |
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Acid former bacteria eat the organic portion of the sludge to form _____ acids and ______ ______ gas. |
Organic acids and carbon dioxide |
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The gas formers in an anaerobic digester break down the organic acids to form _______ and _______ gas |
Methane and carbon dioxide |
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Sludge in an anaerobic digester is usually considered properly digested when ____ percent of the organic matter has been destroyed and converted to gas. |
50% |
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Proper digestion in an anaerobic digester normally takes ___ days if the temperature is kept about ___*f. |
30 days at 95*f |
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Most digestion tanks are mixed to |
Bring food to the organisms, provide a uniform temperature and to avoid the formation of thick scum blankets. |
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When a digester isn't being mixed properly, solids settle to the bottom leaving a ______ colored liquid above the sludge. |
Amber colored |
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Digester gas is usually around ___ percent methane and about ___ percent carbon dioxide |
70 and 30% |
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Liquid hypochlorite (bleach) can be used ________ . |
Directly |
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Liquid hypochlorite (bleach) can be used ________ . |
Directly |
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Chlorine contact basins or tanks are usually designed to provide approximately ___ to ___ minutes of contact time. |
20 to 30 minutes |
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______ ______ is used to dechlorinate or neutralize the remaining residual chlorine. |
Sulfur dioxide |
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Tertiary treatment remove nutrients such as ______ and ______ and the last traces of ______ materials. |
Nitrate, phosphorus, and organic |
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Chlorine has a specific gravity of ___ as a gas. Air has a specific gravity of 1.0 |
2.5 |
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Water has a specific gravity of ___ at 4*C ( 39%f) |
1.000 |
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A good practice is to change work ______ before going home. |
Clothes |
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Materials such as _____, ______ and similar items will cause pipes to plug, may damage pumps, etc. |
Metal and rocks |
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Grit may be dewatered in ______ ______. |
Cyclone separators |
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Parallel bars sometimes called racks have a spacing of ___ to ___ inches or more. |
3 to 4 |
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Parallel bars sometimes called racks have a spacing of ___ to ___ inches or more. |
3 to 4 |
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Bar screens have a spacing about ___ inch to ___ inches. Fine bar screens have a spacing of approximately ___ inches. |
3/8" to 2" and 1/4" |
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Aerated grit chambers usually have a detention time of ___ minutes at peak flows with detention times ranging from ___ to ___ minutes |
3 minutes 3 to 5 minutes |
|
Alkalinity |
The capacity of water/wastewater to neutralize acids. |
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Alkalinity |
The capacity of water/wastewater to neutralize acids. |
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Alkalinity is a measure of how much acid must be added to a liquid to lower the ph to ___. |
4.5 |
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A solution or liquid whose chemical make up neutralizes acids and bases without a great change in ph |
Buffer |
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Aerobic bacteria |
Bacteria which will live and reproduce only in an environment containing oxygen. |
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Aerobic bacteria |
Bacteria which will live and reproduce only in an environment containing oxygen. |
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Anaerobic bacteria |
Bacteria that live and reproduce in an environment containing no "free" or dissolved oxygen. |
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Anaerobic bacteria obtain their oxygen supply by breaking down chemical compounds which contain oxygen, such as ______. |
Sulfate |
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Bulking is caused by ______ |
Filamentous bacteria |
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Mpn is the most probable number of ______-group organisms. |
Coliform |
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Sludge volume index is a measure of the volume of sludge compared with its ______. |
Weight |
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Clarifiers should be shutdown for maintenance during ___ flow periods. |
Low |
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Typical primary clarifier efficiency of settle able solids is ___% to ___%. |
90 to 99 |
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Typical primary clarifier efficiency of settle able solids is ___% to ___%. |
90 to 99 |
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Typical primary clarifier efficiency of suspended solids is ___% to ___%. |
40 to 60 |
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Typical primary clarifier efficiency of settle able solids is ___% to ___%. |
90 to 99 |
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Typical primary clarifier efficiency of suspended solids is ___% to ___%. |
40 to 60 |
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Typical primary clarifier efficiency of total solids is ___% to ___%. |
10 to 15 |
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Typical primary clarifier efficiency of settle able solids is ___% to ___%. |
90 to 99 |
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Typical primary clarifier efficiency of suspended solids is ___% to ___%. |
40 to 60 |
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Typical primary clarifier efficiency of total solids is ___% to ___%. |
10 to 15 |
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Typical primary clarifier efficiency of bod is ___% to ___%. |
20 to 50 |
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Typical primary clarifier efficiency of settle able solids is ___% to ___%. |
90 to 99 |
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Typical primary clarifier efficiency of suspended solids is ___% to ___%. |
40 to 60 |
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Typical primary clarifier efficiency of total solids is ___% to ___%. |
10 to 15 |
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Typical primary clarifier efficiency of bod is ___% to ___%. |
20 to 50 |
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Typical primary clarifier efficiency of bacteria is ___% to ___%. |
25 to 75 |
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Wastewater ph will be about ___ to ___. |
6.5 to 8 |
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Trickling filter secondary clarifier surface loading is ___ to ___ gpd/sq ft |
800 to 1200 |
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Activated sludge secondary clarifier surface loading is ___ to ___ gpd/sq ft |
300 to 1200 |
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Activated sludge secondary clarifier surface loading is ___ to ___ gpd/sq ft |
300 to 1200 |
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Trickle filers and Activated sludge secondary clarifier detention time is ___ to ___ hours |
2 to 3 |
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Nitrogen gas bubbles attach themselves to biological flocs and float to the surface, this is called |
Rising sludge |
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Nitrogen gas bubbles attach themselves to biological flocs and float to the surface, this is called |
Rising sludge |
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Contact stabilization uses two aeration tanks. One tank is for separated reaeration of the returned sludge for ___ hours before flowing into the second aeration tank. |
4 hrs |
|
A reduced level of respiration in which organisms break down compounds within their own cells producing oxygen they need. |
Endogenous respiration |
|
Mean cell residence time (mrct) |
An expression of the average time that a microorganism will spend in the activated sludge process |
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Primary clarifiers remove much of the ______ and ______ material |
Floatable and settleable |
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Conversion of dissolved and suspended material to settle-able solids is the main objective of ______-_____ activated sludge process |
High-rate |
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Conversion of dissolved and suspended material to settle-able solids is the main objective of ______-_____ activated sludge process |
High-rate |
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______-______ process stress oxidation. Oxidation is the addition of oxygen, removal of hydrogen, or the removal of electrons from an element or compound. |
Low-rate |
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If low dissolved oxygen (do) ________ bacteria will thrive and sludge floc will not settle in the secondary clarifier. |
Filamentous |
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A high dissolved oxygen (do) will allow ______ floc to develop and not be removed from the secondary clarifier. |
Pinpoint |
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Extended aeration is similar to conventional activated sludge except the bugs retained in the aeration tank longer and don't get as much ______. |
Food |
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Extended aeration mixed liquor suspended solids concentrations are from ____ to ____ mg/l |
2000 to 5000 |
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Contact stabilization is similar to conventional activated sludge except that the capture of the waste and digestion by the bugs is done in ______ aeration tanks. |
Different |
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Contact stabilization bugs can ______ the waste material in 15 to 30 minutes. But it takes several hours to ______ the material through the cell walls. |
Adsorb, absorb |
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Conventional activated sludge, ______ and ______ happen in one tank. But, the settled bugs still have to digest their food. Another aeration tank called a ______ or re-aeration tank is provided separately for this step. The mixed liquor suspended solids is around 1500 to 2000 mg/l. |
Adsorption and absorption Stabilization |
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In an ideal complete-mix sludge plant, the contents of the tank are completely mixed. (The ______ are uniformly mixed throughout the entire aeration tank. The mlss ranges from 2000 to 5000. |
Mixed liquor suspended solids |
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If the water in the secondary clarifier appears murky or cloudy and the aeration side smells like rotten eggs. |
Not enough air is being supplied |