WWE Flashcards

1
Q

Purpose of Ridge regression

A

Reduce variance

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2
Q

Purpose of Lasso regression

A

Encourage sparsity

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3
Q

Sequence of SCP

A
  1. Define trust region.
  2. Solve approximation.
  3. Check and update trust region.
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4
Q

A11(Q)

A

Head loss relationship

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5
Q

A12

A

Link-junction incidence matrix

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6
Q

A21

A

Junction-link incidence matrix

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7
Q

A10

A

Link-known head node incidence matrix

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8
Q

MPC optimisation formulation

A

Objective function: min. average zonal pressure
Subject to:
- Energy conservation
- Mass conservation
- Minimum regulatory pressure
- Control valve operations

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9
Q

Benefits of pressure management

A
  • Frequency and flow rates of reported leaks reduced
  • Rate of rise of unreported leakage reduces
  • Frequency and cost of economic intervention reduces
  • Background leakage reduces
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10
Q

Leak general equation

A

L = CdA(2gP)^0.5

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11
Q

Leak power equation

A

L = CP^N1

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12
Q

Effect of increasing sludge age

A

More efficient process, but increased Xv (which has a practical limit)

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13
Q

Effect of increasing tank volume

A

Increased hydraulic retention time, but fewer organisms

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14
Q

Nitrification

A
  1. Oxidation of ammonia –> nitrite
  2. Oxidation of nitrite –> nitrate
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15
Q

Denitrification

A

Nitrate + organic matter –> nitrogen gas (under anoxic conditions)

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16
Q

Anammox

A

Ammonia + nitrite –> nitrogen gas
Under anoxic conditions

17
Q

Process of phosphorus removal

A
  • Fatty acids taken by the PAOs and stored as PHA
  • Energy required to store PHA is supplied by breaking down the poly-P into ortho-phosphate
  • Ortho-phosphate released increasing soluble P concentration
  • P uptake to produce poly-P in new cells
  • More P uptake in aerobic reactor than release in anaerobic reactor –> net removal
  • P transfer from liquid to solid
  • P removal via wastage of excess sludge
18
Q

Favorable Conditions Stimulating PolyP

A
  • Anaerobic - aerobic sequence
  • VFAs in the influent
  • No oxygen and nitrate recycling to anaerobic zone
19
Q

P removal configurations

A
  • 3-stage PHOREDOX
  • 5-stage PHOREDOX
  • UCT system
  • Modified UCT system
20
Q

What is the limitation of the PhoRedox systems?

A

Performance is affected if the underflow contains high level of nitrate. Hence, if ammonium/COD ratio is high, there is little flexibility.
N-removal limited by internal recycle ratio.

21
Q

UCT system

A
  • Additional recycle from anoxic to anaerobic.
  • Settling tank underflow recycle to anoxic reactor
22
Q

MUCT system

A
  • Anoxic reactor subdivided into two anoxic reactors
  • First anoxic reactor receives underflow and recycles to anaerobic reactor.
  • Second reactor receives recycling from the aerobic tank.
  • Benefit is no need to control of recycle from aeration tank.
23
Q

Advantage of anammox

A
  • No organics carbon needed
  • No free oxygen needed
  • Less sludge yield (90% less)
24
Q

Globe valve

A

Consists of:
- movable disk-type element
- stationary ring seat in a generally spherical body

25
Diaphragm valve
- flexible diaphragm to control, obstruct, isolate flow
26
Automatic valve control operations
- Pressure from inlet applied to cover chamber --> valve closes. - Pressure in cover chamber relieved --> pressure inlet opens valve.
27
Benefits and limitations of MPC
Benefits: - well-suited for multi-feed DMAs - can adapt to changing critical points - can incorporate other operational objectives Limitations: - needs accurate hydraulic model - computationally expensive
28
Network Models diagram
Steady state simulation ---------------------Extended period simulation Low detail | Strategic planning Pump scheduling | Design Contingency planning | | | | Main rehabilitation Water quality | Minor reinforcements Pressure control High detail
29
Obtaining flow modulation curve
- Monitor flow and pressure at control valve - Monitor pressure at critical point - Record elevation at control valve and critical point head loss between control valve and critical point: hL = (p + z)outlet - (p + z)critical define flow modulation curve by setting pmin = pcritical: poutlet = hL + pmin + (zcritical - zoutlet)
30
Solving hydraulic equations steps
1. Formulate system using hydraulic principles 2. Estimate initial flows and heads, apply Newton-Raphson and derive linear system corresponding to the NR-update. 3. Introduce Schur complement to simplify computations. 4. Solve for h_k+1 first, then get q_k+1.
31
Energy conservation
A11(q)q + A12h + A10h0 = 0
32
Mass conservation
A21q - d = 0
33
Preserving convexity
- Multiplication by non-negative constant - Sum of convex functions - Combination with affine function (f(affine function)) - pointwise maximums
34
Control valve operations constraint
A13T q_t >= 0 eta_t >= 0
35
e- donors and acceptors in nitrogen cycle
Nitrification: e-donor = ammonia; e-acceptor = O2 Denitrification: e-donor = organic matter; e-acceptor: nitrate/nitrite Anammox: e-donor = ammonia; e-acceptor: nitrite
36
Nitrogen cycle diagram
See drawing
37
Sharon & Annamox
Step 1: Partial nitrification (Sharon) convert 50% of ammonium to nitrite Step 2: annamox Result: 70-95% N removal
38
P removal diagram
See drawing
39
3 stage-PhoRedox diagram
see drawing