What Is The Operation Of The High Rate Activated Sludge ( HRAS ) Process

Three ways to assess water are positive/negative, membrane filtration and IDEXX Colilert and Enterolert assays. For membrane filtration, petri dishes and an incubator are used. For IDEXX coliert powdered medium is used for total coliform and E. Coli, while Enterolert media is used for enterococci. Also an incubator, colilert trays are used. IDEXX is more expensive than membrane filtration.

The materials used in this lab were, two glass beakers, four dialysis membranes: 20 (MWCO), 50 (MWCO), 100 (MWCO), and 200 (MWCO), a membrane holder, a membrane barrier, four solutes: NaCl, Urea, Albumin, and Glucose, a solution dispenser, deionized water, a timer, and a beaker flush. The four dialysis membranes are placed between the beakers and during each trial, certain concentrations are increased by adding one of the four solutes in the left beaker. Deionized water is added to the right beaker and replaced before the next test. A timer is adjusted to 60 minutes and the barrier between the beaker descends, allowing the solutions in each beaker to have access to the dialysis membrane separating them. The concentration is checked at the end of the 60-minute period indicating diffusing from the left to right or vice versa. If diffusion occurs in the experiment, repeat with the same membrane and change the concentrations. If no diffusion occurred, continue to the next sized membrane.

PH sensors are used in many scientific laboratories to measure the hydrogen-ion concentration of a liquid substance and to determine the basicity and acidity of a liquid. PH meters measure the electrical potential difference between a reference electrode probe and a pH electrode probe. Since these probes are very sensitive, they are required to be kept cleansed from contaminants. If exposed to contamination, one risks faulty or unreliable data, since their accuracy is dependent on a regular calibration and upkeep. To avoid this risk, and accurately measure hydrogen-ion concentration, the probes are kept in a buffer solution and calibrated before each use. [1]

Environmental Protection Agency (EPA) described the general treatment of wastewater and its two basic stages, primary and secondary. In the primary treatment most solids are caught in a screen, then the sewage goes to a grit chamber to settle small pieces of debris at the bottom, then through the sedimentation tank. Afterwards, secondary treatment removes a majority of the organic matter, eventually being chlorinated before reaching an effluent (EPA, 1998).

PH sensors are used in many scientific laboratories to measure the hydrogen-ion concentration of a liquid substance and to determine the basicity and acidity of a liquid. PH meters measure the electrical potential difference between a reference electrode probe and a pH electrode probe. Since these probes are very sensitive, they are required to be kept cleansed from contaminants. If exposed to contamination, one risks faulty or unreliable data, since their accuracy is dependent on a regular calibration and upkeep. To avoid this risk, and accurately measure hydrogen-ion concentration, the probes are kept in a buffer solution and calibrated before each use. [1]

The pipette was used to transfer 8 mL of the 0.5 molarity solution into the graduated cylinder. Distilled water was added to raise the bottom of the meniscus to the 20.0 mL line and the solution was transferred into the beaker after it was rinsed with the solution. The pipette was used to take a small quantity of the solution and rinse and then fill a test tube with the solution. The amount of 0.2 molarity solution needed to create 20.0 mL of 0.1 molarity solution was calculated as 10.0 mL. The pipette was used to transfer 10.0 mL of 0.2 molarity solution into the graduated cylinder and distilled water added until the bottom of the meniscus reached the 20.0 mL line. The solution was transferred to the rinsed beaker and then a portion placed into a test tube that had been rinsed with the solution. The amount of 0.1 molarity solution required to create 20.0 mL of 0.05 molarity solution was calculated to be 10.0 mL. The pipette was used to transfer 10.0 mL of 0.2 molarity solution into the graduated cylinder and distilled water added until the bottom of the meniscus reached the 20.0 mL line. The solution was then placed into a beaker that had been rinsed with the solution and then into a rinsed test

Due to diverse composition of the wastewater, which can be high concentrations of volatile organic compounds, chemicals, and materials of radioactivity. (Chameides, 2011) This diverse composition of wastewater can disrupt the natural operation of municipal treatment plants by inhibiting biological treatment. Additionally, the wastewater may facilitate the formation of harmful disinfection by products. Hence the need for specialized treatment plants for the oil and gas industry. (Maloney & Yoxtheimer, 2012) These specialized treatment plants will customarily be made up of 4 subcategories, “Metals Treatment and Recovery,” “Oils Treatment and Recovery,” “Organics Treatment and Recovery,” and “Multiple Waste streams.” (“Natural Gas Extraction – Hydraulic Fracturing | US EPA”,

Gather the following lab equipment: Goggles, test tubes, 24 well plate, Gas assembly with copper and plastic tubing and a #00 stopper, short stem pipet, rubber stopper #00 with one hole and a pipet tip with plastic gas delivery tube, 2 small tables of AlkaSeltzer, 4mL Bromothymol blue .04%, 20 mL hydrochloric acid, 4-6 pieces of manganese metal, 4-6 pieces of mossy zinc, and 3 pipet bulbs.

The Hattiesburg South Lagoon is a 20 MGD designed wastewater treatment plant (WWTP) located at 1903 East Hardy Street in Hattiesburg, Mississippi. The plant serves the city of Hattiesburg, City of Petal, and surround areas of forest County. The plant consists of four lagoons with floating mechanical aerators and a chlorine contact chamber. Cell #3 also includes a sub-cell area that uses diffuse aeration to support the treatment of the industrial influent coming from the yeast plant. Most of the industrial wastewater received at the plant comes from a chicken processing facility and a yeast manufacturer plant. The plant effluent is discharged into the Leaf River.

After the dirty water flows in to the treatment plant it goes through Bar Screens, then Grit Channels, which is followed by Influent Pumping, followed by Primary Settling, then to Oxygenation Tanks which undergoes a Secondary Setting then Effluent Pumping. Afterwards the water is then disposed either in the upper NY Bay or the Newark Bay. If after the Effluent Pumping process the water goes to the Main outfall is directed to the Upper NY Bay, if it instead goes to the Chlorine Contact Tank then it is disposed of in the Newark Bay

A group of subject 48350 Environmental and Sanitation Engineering students visited both plants, and observed the operations and maintenance of these wastewater treatment systems.

The purpose of the fluid flow meters experiment was to determine the operating characteristics of the Venturi and orifice meters. The purpose of the tray hydraulics experiment was to study the vapor and liquid tray hydraulics parameters for sieve, or perforated, trays in a distillation column. By performing experiments based on theory and comparing results to literature values, the objectives of this experiment can be achieved.

To filter the foul water, 100.1 mL were poured into a graduated cylinder. The water had a dark brown color, with tiny particles floating around in the substance. It was also murky and hard to see through with a small

This report provides analysis and evaluation of a newly designed wastewater treatment facility for Sand Valley, Nevada. Analysis will include Biological Oxygen Demand (BOD) along with total, volatile, and fixed suspended solids. Methods for analysis will include the Winkler Test for BOD and a Hatch test for the suspend solids.

The disposal of untreated wastewater coming from the industries into the water bodies will pollute the water bodies because of its high concentrations. So, the wastewater produced from the industry should be treated properly to meet the permissible limits given by central and state pollution control boards. Therefore it is necessary to treat the wastewater properly with the help of an appropriate treatment plant. However, the treatment plant even though properly planned may not work satisfactory because of several reasons. Hence, it is essential to evaluate the treatment plant considering individual treatment unit in the entire treatment flow. In the present work emphasis has been given to the study of the performance of treatment facilities because of its importance in the conventional treatment of wastewater. Hence, the literature review related to the evaluation of the entire treatment process along with biological treatment process particularly suspended growth process Activated Sludge Process (ASP), attached growth process Trickling Filter (TF) and a combination of the both suspended and attached growth process Hybrid Reactor (HR) is presented in the following sections of this chapter.