Month: November 2017

CHE 320 Safety, Engineering Ethics and Professionalism
Fall 2017
CHE 320 Homework #5


Answer each question in 2-3 sentences or a short paragraph. Your responses must be neatly typed, and free of major grammatical and spelling errors. Be specific – points will be deducted for vague or incoherent answers, as well as spelling and grammar problems.

1. Review the details of the Deepwater Horizon disaster on the Wikipedia article titled “Deepwater Horizon explosion” (http://en.wikipedia.org/wiki/Deepwater_Horizon_explosion).

a) Many warning signs and incidents occurred before the explosion, but engineers and management chose to ignore them. List three of these near-misses, and explain why each should have been viewed as a warning of the impending disaster (i.e. what specifically did they suggest might go badly wrong?)

b) Why were operational problems and concerns about safety not reported to (or acted on) by the upper management who were ultimately responsible for the Deepwater Horizon?

2. Read the article titled “Blowup” by Malcolm Gladwell (posted on Canvas).

a) Explain what is meant by the term “normal accident”.

b) Why does our ever-growing reliance on complex safety systems in many aspects of our lives (e.g. antilock braking systems, network firewalls, smoke detectors, etc.) actually encourage people to take more risks than they would have otherwise?

3. Read the article titled “No One Knew He Was There” on the EHS Today website:

http://ehstoday.com/safety/confined-spaces/ehs_imp_35065

a) How was Garcia killed? What was the official cause of death? Who was ultimately responsible for Garcia’s death?

b) List at least four general behaviors or actions that Garcia took, which violated accepted industry safe practices for work in confined spaces. (do not simply list four missing items of PPE, etc.)

c) Explain what was meant by “near-miss confined space fatality” in the article.

d) What is the main subject of the legal dispute between Garcia’s family and Reynolds?



4. Consider the process flowsheet above. In this process, hot gasoline containing methane gas is pumped by a positive-displacement pump (P-1) into a separator drum (D-1). The methane gas and the liquid gasoline are separated in the drum, D-1. A heat exchanger (E-1) cools the hot liquid gasoline stream, to limit the loss of gasoline by evaporation in the drum. Valves V-4 and V-6 automatically maintain the liquid level in the drum, between set high and low limits. See the Crowl text for details of the symbols on the flowsheet diagram. ( You are encouraged to discuss this problem in “what-if” teams ) Signals (dashed lines) to and from the other valves and the pump allow remote manual control by an operator in the main control room. There are no people working near the equipment (good plant design). During a startup, the pump P-1 suddenly exploded in a large ball of fire. Although the pump and the connected piping are destroyed, the drum itself was only slightly damaged by the fire.

a. What is the most likely sequence of events that led to the destruction of the pump? List them in order of their occurrence. Hint: Use a “What-If?” analysis to consider what would happen if each of the labeled pieces of equipment did not operate as expected (either singly or together). What would cause that to happen? Safe assumptions: Pipes carrying hot gasoline would be made from metal (conductive), so static electricity is not a concern. There is no oxygen/air in the gasoline/CH4 mixture, so it cannot burn/explode unless released to the atmosphere. The pump is rated for continuous operation at the maximum temperature of the hot gasoline feed. No open flames are present.

b. Draw appropriate reliefs on the diagram, wherever they are required to prevent catastrophic failure. Err on the side of safety in your final design, but please do not simply put a relief on every pipe or piece of equipment. Copy and paste this symbol where required on the figure:



Relief symbol:

c. Describe a simple change that could be made to the piping or signal/control lines, which would completely and automatically eliminate the main cause of this explosion. Hint: Signals can be made to control equipment other than valves. Just adding a relief or two is not sufficient.

5. The photographs below show a typical underground pump vault in a petroleum refinery. The pump is used to feed a liquid hydrocarbon stream (e.g. gasoline) to a nearby distillation tower.

a) Is the pump vault a permit-required confined space? Explain in terms of the formal definitions of confined spaces. What signage would be required for this area?

b) Using the Hazard Identification Tool which was distributed in class, identify at least three potential life-threatening hazards which might exist in the pump vault.

c) List the specific items of safety equipment that are required before anyone enters the vault to perform maintenance on the pump head.

d) List and describe the role of each person who is required to be involved in the maintenance operation.





6. Refer to the process flow diagram above: Propane vapor is compressed in the turbine compressor C-1 to a final pressure of 7 atm. The boiling point of propane at 7 atm is 12 °C. The compressed vapor is then cooled with 4 °C water in the heat exchanger E-1. The cold propane vapor condenses into liquid propane, which is held in the large refrigerated tank T-1 until it is fed to a reactor. The process is controlled from a remote control room, and an overfill sensor sends an alarm signal to the operators if the liquid rises above a set level. The tank can be inerted by closing all valves except V-5 and V-7; the N2/propane vapor goes to a flare, where it is safely burnt. Valves V-7 and V-8 are normally closed. ( You are encouraged to discuss this problem in “what-if” teams)

DIRECTLY ON THE DIAGRAM ABOVE, mark any location where pressure/vacuum reliefs would be necessary. Please use this symbol to indicate the location of a relief valve (use Word to copy and paste the symbol on figure):



Relief symbol:

Your arrows must be clearly drawn and must point to the part of the equipment/pipe/etc. where the relief should be installed and whether it is a vacuum or pressure relief. Points will be deducted for reliefs that are placed where they are not needed. Do not simply place a relief on every pipe and every piece of equipment!

7. Extra Credit (20pts). Read the article “Learning from UCLA” by J. N. Kemsley (https://cen.acs.org/articles/87/i31/Learning-UCLA.html). Then answer the following:

a. In 2008, a graduate student died during a “routine” organic synthesis step using a very hazardous chemical. What was this chemical and what was the primary hazard?

b. Summarize the suspected sequence of events that lead to the incident and eventual death of Sheharbano “Sheri” Sangji, the 23 year old graduate student.

c. Describe the “proper” technique to transfer the dangerous chemical. Was this technique followed exactly? Describe any differences. What was the proper PPE? Was it being worn?

d. Did regulators (Cal/OSHA) cite violations to UCLA? Why?

e. What larger, systemic, problem did this incident bring to light? Be sure your answer involves a discussion of “safety culture.”

You must use complete and grammatically correct sentences in your writing. Answers must be typed and full credit will only be granted if an in-depth answer is provided.

To operator control board

Propanevapor

C-1V-6V-7V-8T-1Overfillsensor

Cold water

V-3E-1

Warm water

V-2V-4

To reactorNitrogen

V-5

To flare

Liquid propanein refrigerated tankV-1

Hot gasolineand methaneP-1V-3V-4V-5V-6Methane gasLiquid gasolineTo operator control boardD-1LC-1Level sensorCooling water inV-1V-2E-1LC-2Cooling water out

R

VAULT ACCESS HATCHPUMP HEAD