Title: When Things Go Wrong
1When Things Go Wrong
- William Josephson A.U. Chem. Eng.
- Jaya Krishnagopalan T.U. Chem. Eng.
- Dave Mills A.U. Chem. Eng.
- 2007 AIChE Annual Meeting
- Salt Lake City, Utah
2Outline
- 4 Experiments
- Conduction
- Reynolds Number
- Friction factor
- Viscosity
- For Each Experiment
- What should occur
- What did occur
- Why it happened
- What was learned
3Motivation
4Conduction Heat Transfer
- Objectives
- To investigate Fouriers Law for the linear
conduction of heat along a simple brass bar - To determine the average thermal conductivity of
brass in the temperature range studied - To observe the effect of temperature on the
thermal conductivity of brass in the range studied
5Conduction Heat Transfer Apparatus
6Conduction Heat Transfer
7Conduction Heat Transfer
8Conduction Heat Transfer
9Conduction Heat Transfer
10Conduction Heat Transfer
- Told students of problem
- Let them devise workaround
- Most students made use of knowledge of sample
material calculated 3 conductivities
eliminated bad thermocouple
11Reynolds Number
- Objectives
- Compute Reynolds number
- Observe and quantify transitional flow
12Reynolds Number Apparatus
13Reynolds Number - Ideal Results
Re Observations
500 Parallel streamlines laminar flow
1000 Laminar
1500 Laminar
2000 Laminar
2500 Parallel interacting streamlines transient flow
3000 Interacting streamlines - turbulent flow
3500 Turbulent
4000 Turbulent
4500 Turbulent
5000 Turbulent
14Reynolds Number
- The Problem
- Mixing of streamlines at Re 700
- Occurred for all groups
15Reynolds Number Expected Reported Results
Re Observations
500 Parallel streamlines laminar flow
600 Laminar
650 Parallel interacting streamlines transient flow
700 Turbulent flow
800 Turbulent
1000 Turbulent
2000 Turbulent
3000 Turbulent
4000 Turbulent
5000 Turbulent
16Reynolds Number Actual Reported Results
Re Observations
500 Parallel streamlines laminar flow
600 Laminar
650 Parallel interacting streamlines laminar flow
700 Interacting streamlines - laminar flow
800 Interacting streamlines - laminar flow
1000 Interacting streamlines - laminar flow
2000 Interacting streamlines - laminar flow
3000 Interacting streamlines - transient flow
4000 Interacting streamlines - turbulent flow
5000 Turbulent
17Reynolds Number
- Cause of the Problem (physical)
- Nozzle at end of dye introduction pipe
18Reynolds Number
- Cause of the Problem (mental)
- Poor wording in handout If the Reynolds number
is less than 2100, the flow is considered
laminar. If the Reynolds number is greater than
4000, the flow is considered turbulent.
19Piping
- Objectives
- To determine relationship between friction factor
and Reynolds Number roughness - Friction losses in fittings (globe valve, elbows)
- Orifice meter
20Piping Apparatus
Direction of Flow
Pipe A
Pipe B
Pipe C
Pipe D
Pipe E
21Piping What we want them to do
22Piping What we get (sometimes)
- Important! This is not the problem
23Piping What we get (other times)
Important! This is the problem
24Piping
- The Problem friction factors for SS Pipe below
those of PVC - Consideration of the Problem
- Recheck the numbers
- A Lie in the handout?? (e.g., wrong info re pipe
size) - Deeper Thoughts is this an issue w/ the SS pipe
or the PVC pipes? Or both?
25Viscosity
- Objectives
- To investigate rheology of several liquids
- Confirm Newtonian fluids
- Determine if shear-thickening, shear-thinning or
something else - Temperature effect on a Newtonian fluid
26Viscosity
27Viscosity Apparatus
28Viscosity Ketchup Results
29Viscosity Corn Starch Results
30Corn Starch Viscosity
- The Problem data indicates shear thinning
- Consideration of the Problem
- Recheck the numbers
- Try different concentrations
- Is corn starch really shear thickening?
31Corn Starch Viscosity
- Is it really shear thickening??
32Corn Starch Viscosity
- Consideration of the Problem (cont.)
- Observe operation of viscometer esp. spindle
interactions w/ fluid closely read literature - The Answer ( the solution)
33Viscosity Corn Starch Results w/ Vane
34What Went Wrong What Happened
- Conductivity
- Bad Sensor, students were told a priori
- Students derived workaround
- Reynolds Number
- Physical Setup
- Students re-examined their thinking (as did the
instructor!) - Piping
- Arguably, nothing went wrong
- Students have to think
- Viscosity
- Improper equipment
- Students had to think observe
35A Sincere Thank You
To the students in CENG 320 Unit Operations
Laboratory I T.U. CHEN 3820 Chemical
Engineering Laboratory I A.U.