INTRODUCTION TO BIOENGINEERING II Bio E 411 AECEBRT

INTRODUCTION TO BIOENGINEERING II Bio. E 411, AE/CE/BRT 511 J. (Hans) van Leeuwen T. H. Kim

Instructor (33%) Professor J. (Hans) van Leeuwen from/of the Lions • • Born in Gouda, Netherlands Grew up in South Africa Lived in Australia for 7 years Lived in Ames for 11 years Specialty: Environmental and Bioengineering Industrial wastewater treatment and product development based on waste materials

Research activities Beneficiation of biofuel coproducts by cultivating fungi

Ozonation applications Selective disinfection Selective oxidation Alcohol purification

Keeping exotic aliens out of our ports ET Zebra mussels

Human technological development From scavengers…

…to use of fire… Use of fire was the turning point in the technological development of humans q leading to extended diet q food preservation q better hunting q agriculture q industry Top of the food chain! but, this ultimately led to…

…Overpopulation…

P o l l u t i o n. .

Pollution of a small stream

Consequence of pollution

…and ecological disasters

…and more disasters

Distribution of Earth’s water

Dangers lurking in water

Pollution from informal housing

Waterborne diseases Map by Lord John Snow of the cholera outbreak in London in 1854 – the Broad Street Epidemic. This is considered the root of epidemiology.

Spread of Cholera in London 1854 1 -3 September: 127 dead By 10 September: 500 Ultimately: 616 dead

Cholera – the rapid killer SEM micrograph of Vibrio cholerae, a Gram-negative bacterium that produces cholera toxin, an enterotoxin, which acts on the mucosal epithelium lining of the small intestine This is responsible for the disease's most salient characteristic, exhaustive diarrhea. Bottom: cholera toxin

Examples of organisms secreting enterotoxins Bacterial Escherichia coli O 157: H 7 Clostridium perfringens Vibrio cholerae Yersinia enterocolitica Shigella dysenteriae Staphylococcus aureus ( pictured) Viral Rotavirus (NSP 4) (Institute for Molecular Virology. WI)

Dissolved oxygen Importance Why is oxygen in water important? Dissolved oxygen (DO) analysis measures the amount of gaseous oxygen (O 2) dissolved in an aqueous solution. Oxygen gets into water by diffusion from the surrounding air, by aeration (rapid movement), and as a product of photosynthesis. DO is measured in standard solution units such as milligrams O 2 per liter (mg/L), millilitres O 2 per liter (ml/L), millimoles O 2 per liter (mmol/L), and moles O 2 per cubic meter (mol/m 3). DO is measured by way of its oxidation potential with a probe that allows diffusion of oxygen into it. The saturation solubility of oxygen in wastewater can be expressed as Cs = (0. 99)h/88 x 482. 5/(T + 32. 6) For example, in freshwater in Ames at 350 m and 20°C, O 2 saturation is 8. 8 mg/L. (Check for yourself, with = 1)

BOD Biochemical oxygen demand or BOD is a procedure for determining the rate of uptake of dissolved oxygen by the organisms in a body of water BOD measures the oxygen uptake by bacteria in a water sample at a temperature of 20°C over a period of 5 d in the dark. The sample is diluted with oxygen saturated de-ionized water, inoculating it with a fixed aliquot of microbial seed, measuring the (DO) and then sealing the sample to prevent further oxygen addition. The sample is kept at 20 °C for five days, in the dark to prevent addition of oxygen by photo-synthesis, and the dissolved oxygen is measured again. The difference between the final DO and initial DO is the BOD or, BOD 5. Once we have a BOD 5 value, it is treated as just a concentration in mg/L BOD can be calculated by: Diluted: ((Initial DO - Final DO + BOD of Seed) x Dilution Factor BOD of seed (diluted activated sludge) is measured in a control: just deionized water without wastewater sample. Significance: BOD is a measure of organic content and gives an indication on how much oxygen would be required for microbial degradation.

Oxygen depletion in streams

DO sag definitions

Cumulative oxygen supply + demand Plotting the two kinetic equations separately on a cumulative basis and adding these graphically produce the DO sag curve

Streeter-Phelps Model* Mass Balance for the Model Not a Steady-state situation rate O 2 accum. = rate O 2 in – rate O 2 out + produced – consumed rate O 2 accum. = rate O 2 in – 0 + 0 – rate O 2 consumed Kinetics Both reoxygenation and deoxygenation are 1 st order * Streeter, H. W. and Phelps, E. B. Bulletin #146, USPHS (1925)

Kinetics* for Streeter-Phelps Model • Deoxygenation L = BOD remaining at any time d. L/dt = Rate of deoxygenation equivalent to rate of BOD removal d. L/dt = -k 1 L for a first order reaction k 1 = deoxygenation constant, f’n of waste type and temp. *See Kinetics presentation if unfamiliar with the mathematical processing

Developing the Streeter-Phelps Rate of reoxygenation = k 2 D D = deficit in D. O. k 2 = reoxygenation constant* Where – T = temperature of water, ºC – H = average depth of flow, m – ν = mean stream velocity, m/s D. O. deficit = saturation D. O. – D. O. in the water There are many correlations for this. The simplest one, used here, is from O’Connor and Dobbins, 1958 Typical values for k 2 at 20 °C, 1/d (base e) are as follows: small ponds and back water 0. 10 - 0. 23 sluggish streams and large lakes 0. 23 - 0. 35 large streams with low velocity 0. 35 - 0. 46 large streams at normal velocity 0. 46 - 0. 69 swift streams 0. 69 - 1. 15 rapids and waterfalls > 1. 15

Combining the kinetics Net rate of change of oxygen deficiency, d. D/dt = k 1 L - k 2 D where L = L 0 e-k 1 t OR d. D/dt = k 1 L 0 e-k 1 t - k 2 D

Integration and substitution The last differential equation can be integrated to: It can be observed that the minimum value, Dc is achieved when d. D/dt = 0: , since D is then Dc Substituting this last equation in the first, when D = Dc and solving for t = tc:

Example: Streeter-Phelps Wastewater mixes with a river resulting in a BOD = 10. 9 mg/L, DO = 7. 6 mg/L The mixture has a temp. = 20 C Deoxygenation const. = 0. 2 day-1 Average flow = 0. 3 m/s, Average depth = 3. 0 m DO saturated = 9. 1 mg/L • Find the time and distance downstream at which the oxygen deficit is a maximum • Find the minimum value of DO

Solution…some values needed • Initial Deficit Do = 9. 1 – 7. 6 = 1. 5 mg/L (Now given, but could be calculated from proportional mix of river DO, presumably saturated, and DO of wastewater, presumably zero) • Estimate the reaeration constant: k 2 = 3. 9 v½ (1. 025 T-20)½ H 3/2 k 2 = 3. 9 x (0. 3 m/s)½ (1. 02520 -20)½ = 0. 41 d-1 (3. 0 m)3/2

Solution…time and distance Note that the effects will be maximized almost 70 km downstream

Solution…maximum DO deficiency Note that this BOD could have been calculated from mixing high-BOD wastewater with zero or near-zero BOD The minimum DO value is 9. 1 -3. 1 = 6 mg/L Implication: DO probably not low enough for a fishkill, but if continued could lead to species differentiation and discourage sensitives species like trout.