Consider a pilot scale sand filter with the following characteristics.Diameter of cylindrical filter: 80 cmDepth of sand bed: 40 cmDiameter of sand grains: 0.5 mmPorosity in filter bed: 0.45The filter is used to treat 40 L/min of 25°C water containing 106particles/mL. The particles have a uniform diameter of 3 µm, adensity of 1.5 g/cm³ and have been effectively destabilized (a=1) bya preceding coagulation step. Determine the expected concentrationof the particles in the filter effluent during the steady state portion ofthe filter run.

Answered: Image /qna-images/answer/221cdca4-e77a-4012-ae41-8975e0e11719.jpg

Answered: Consider a pilot scale sand filter with…

Structural Analysis

6th Edition

ISBN:9781337630931

Author:KASSIMALI, Aslam.

Publisher:KASSIMALI, Aslam.

Chapter2: Loads On Structures

Section: Chapter Questions

Problem 1P

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Water analysis was carried out for solid analysis. The test was performed and the following information collected. Mass of empty dish = 51.5494 g; Mass of dish + Sample = 109.5 g; Mass of dish + dry solids =51.587 g; Mass of dish + ignited solid =51.541 g; Mass of empty filter = 0.1154 g; Mass of filter after drying = 0.1241 g; Mass of filter at ignition = 0.1160 g; Volume of sample =25 mL Compute the concentration of total solids, total volatile and fixed solids, suspended, volatile suspended solids and fixed suspended solids.
A primary clarifier is to be designed to treat a municipal wastewater. The influent to the clarifier has a flow rate of 7570 m³/d and a total suspended solids concentration of 320 mg/L. A laboratory settling test was performed with the following results: Suspended Solids Concentration (mg/L) at Given Depths Sampling Depth (m) Time (min) 0.61 1.22 246 2.44 272 243 1.83 3.05 10 230 262 282 20 157 195 230 253 30 115 160 211 221 230 45 90 134 163 179 195 60 48 102 131 154 170 90 29 58 86 115 141 (a) Determine the design overflow rate and detention time assuming 65% of the suspended solids are to be removed. Use typical scaling/safety factors as appropriate. (b) Determine the required diameter (to the nearest 0.1 m) and the required depth (to the nearest 0.01 m) for the clarifier.
Determine the suspended solids and the percent volatile matter in a solids sample based on the following data: Sample size 25 mL Tare mass of filter = 1.5325 g Tare mass of filter plus retained solids = 1.5415 g Tare mass of filter plus retained ash = 1.5378 g
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An anaerobic digester (AD) is designed with the following data. Organic loading rate 1.0 kg VSS/m³.day VSS load 120 kg/day (i). (ii). Estimate the volume of the AD. If the VSS is 12 kg/m³, estimate the retention time.
Enter T next to the following true statements and F next to the false statements. Settling of suspended solids in secondary clarifiers is typical of Type II sedimentation. Thickening prior to digestion is common in many wastewater treatment plants because it reduces the size needed for the digester. Based on a temperature of 30°C, a design mean cell residenee time of about 20 days would be reasonable for a completely-mixed anaerobic digester without recycle. A volatile suspended solid is defined as an organic solid that can be oxidized to CO2 (g) at 250°C. The theoretical yield coefficient can be estimated from the observed yield coefficient if the specific growth rate constant is known. Air flotation would likely be more efficient for thickening waste activated sludge than primary sludge, while the opposite would be true for gravity thickening. The net mass of cells produced in the activated sludge process equals the total cell mass synthesized minus the cell mass wasted as waste…
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(₁ ) A PM10 sampler was operated for a period of 24 hours at a flow rate of 0.7 m³/min. The filter tare weight was 1.7911 g, and the dried filter weight after sampling was 1.8521 g. Calculate the PM10 concentration in µg/m³.
The bed thickness of a speed sand filter is 1.3 m. A sand with a specific diameter of 0.8 mm and a specific gravity of 2600 kg / m3 will be used as filter material. The shape factor of the sand is 0.9 and the porosity of the clean bed is 0.45. The water layer thickness on the bed is 1.1 m. Average filtration speed is 130 m / day and maximum filtration speed is 180 m / day. The maximum flow rate is 24087 m3 / day and the kinematic viscosity of water is 1.01x10-6 m2 / sec. The maximum head loss in the filter is required to be 1.9 m and negative pressure is not allowed. a) Find the initial head loss of the filter bed. b) Find the required number of filters and the area of each filter in case 3 filters are in reserve. c) Calculate how many meters depth the pollution penetrates at the end of filtration.
Which of the following is not a mode of field flow fractionation? a. Viscosity b. Sedimentation c. Flow d. Thermal
Please design a rapid sand filter that will effectively remove 65% of thesuspended solids in a flow of 10 cubic meters per minute. The suspendedmaterial consists of particles that are perfectly spherical with a diameter of 10microns. Please use sand with an effective size of 1 mm and a porosity of 0.5.You should limit your clean bed head loss to 0.5 meters per meter. (Pease use an attachment efficiency, α of 0.75)Viscosity of water =1.0087x10-3 Ns/m2Density of water =998.23 kg/m3What are the dimensions of this filter (Depth and Surface Area)?

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