Module 3 (I & II) Flashcards

1
Q

T/F: The performance of bioprocesses for the treatment or conversion of organic waste depends on the dyanamic of microbial growth and substrate utilization, which are proportional.

A

False: they are inversely proportional (or INTERCORRELATED)

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2
Q

List the phases of bacterial growth in a batch system in order

A
  1. Lag
  2. Exponential growth
  3. Stationary
  4. Death
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3
Q

_______ _______ _______ is the ratio of biomass produced to the amount of substrate consumed.

A

Biomass synthesis yield

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4
Q

T/F: Biomass synthesis yield is defined relative to the electron acceptor used

A

False: electron DONOR (substrate)

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5
Q

T/F: The biomass synthesis yield can be expressed in measurable quantities - g biomass/g COD consumed, but NOT g biomass/g BOD consumed.

A

False: both g biomass/g COD and g biomass/g BOD can be equated to the biomass synthesis yield.

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6
Q

____ is the parameter used most commonly to follow _______ _______ in full-scale bio wastewater treatment systems because its measurement is _______, and minimal _______ is required for analysis.

A

VSS
biomass growth
simple
time

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7
Q

What is the formula for biomass synthesis yield?

A

VSS (g)/ BOD (g) OR COD (g)

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8
Q

What is the formula for the substrate utilization rate (r_su)?

A

dS/dt = r_su = (kXS) / (K_s + S)

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9
Q

What is “k” and what are its units?

A

maximum specific sub utilization rate (g sub/g microorgg*d)

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10
Q

What is “K_s” and what are its units?

A

half-velocity constant (sub concentration @ 1/2 max specific substrate utilization rate), g/m^3

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11
Q

What does the “b” in bCOD stand for

A

biodegradable COD

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12
Q

T/F: If S is infinitely larger than K_s, then r_su = kX

A

True

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13
Q

T/F: If S «< K_s, r_su = kX/K_s + S

A

False: remove the S from the denominator

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14
Q

What is the formula for bacterial growth rate from substrate utilization (in cases of limiting substrate)?

A

dX/dt = r_g = (mu_max*XS) / (K_s + S)

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15
Q

T/F: The bacterial growth rate and the substrate utilization rate are related by the biomass synthesis yield.

A

True: r_g = Y*r_su

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16
Q

Which case do we deal with the most in biological treatment processes, and why?

  1. K_s&raquo_space;> S
  2. K_s «< S
A

Case 1: the purpose of treatment is to reduce S in the outlet stream

17
Q

What is the formula for net biomass growth rate (r_X)?

A

r_X = (Y*r_su) - bX

*Rate of biomass growth minus the endogenous respiration rate (or dead rate)
b = specific endogenous decay coefficient, g VSS/g VSSd

18
Q

T/F: The biomass synthesis yield for VSS on BOD will be smaller than that for VSS on COD

A

True: COD is a theoretical case, so will always be higher than BOD

19
Q

What is the formula for the rate of O2 uptake in aerobic biological processes?

A

r_o = r_su - (1.42*r_x)

20
Q

What is the significant number 1.42 seen in this course?

A

The COD of biomass: g COD/g VSS

21
Q

Temperature influences not only the _______ _______ of the microorganism, but also a significant impact on performance-related factors such as gas-transfer rates, _______ of biomass, etc.

A

Metabolic activities
settleablity

22
Q

What is the formula for the reaction rate constant?

A

k_T = k_20*(theta^(T-20))

theta = temperature-activity coefficient (can vary from 1.02 to 1.25)

23
Q

T/F: In batch reactors, S is constant, while in CSTRs, S is not constant.

A

False: opposite is true

24
Q

When does “t” start in a batch reactor?

A

t begins at the start of the REACTION

25
Q

What is “t” in the context of a CSTR?

A

t = reaction time; average amount of time that feed particles/molecules spend inside the bioreactor from the time they enter to the time they exit.

26
Q

What is Biomass Retention Time (SRT), why is it important?

A

Average time that biomass stays in the bioreactor; both removal efficiency and biomass/MLVSS concentration are affected by SRT.

27
Q

What is the formula for the hydraulic retention time (HRT)?

A

volume of bioreactor (m3) / volumetric flowrate (m3/d)

28
Q

What is the formula for the solid retention time (SRT)?

A

mass biomass (solids) in bioreactor (g) / biomass removal rate (g/d)

29
Q

Can we control SRT without sludge returning? If so, how?

A

Yes - we can prevent biomass washout by providing a surface for organisms to build a biofilm (ie. biofilm carrier or media)

30
Q

List the main biofilm development phases

A
  1. Attachment [to a surface]
  2. Growth
  3. Detachment
31
Q

What are the two types of biological treatment processes?

A
  1. Suspended-growth processes (maintained in liquid suspension by app. mixing)
  2. Attached-growth processes (attached to an inert packing material)
32
Q

What are the three types of attached growth processes?

A
  1. Non submerged (ie. trickling filter)
  2. Partially submerged (ie. Rotating Biological Contactor)
  3. Fully submerged (ie. Moving-bed biofilm reactor, MBBR)
33
Q

T/F: when using a fully submerged attached growth process, we tend to use packing material with higher density than water so they can collect microorganisms that settle to the bottom of the tank.

A

False: densities similar to water so they move inside the tank/bioreactor. Hence, moving beds

34
Q

What are some benefits to MBBR?

A
  • Higher surface area for org material collection
  • Diff shapes, materials, sizes (economically feasible)
  • Can allow reactor to take on higher org load