DUST EXPLOSION HAZARDS

 https://bulkinside.com/bulk-solids-handling/explosion-protection-process-safety/dust-explosion-hazards/

IS TRUCK GROUNDING NECESSARY?

 https://bulkinside.com/bulk-solids-handling/explosion-protection-process-safety/is-truck-grounding-necessary/

How to Avoid Common Genset Room Design Mistakes

How to Avoid Common Genset Room Design Mistakes: The room and building that a power generating set will be located in must comply with all genset room design requirements to ensure reliable operation.

Protecting Battery Energy Storage Systems from Fire and Explosion Hazards

Protecting Battery Energy Storage Systems from Fire and Explosion Hazards: There are serious risks associated with lithium-ion battery energy storage systems. Thermal runaway can release toxic and explosive gases, and the problem can spread from one malfunctioning cell to neighboring cells, resulting in catastrophe.

How to Prevent Fire Hazards Associated with Static Electricity

How to Prevent Fire Hazards Associated with Static Electricity: When combustible materials are handled, static electricity can be dangerous as the work environment then becomes at risk for fires and explosions.

 A game-changing approach to furnace safeguarding

This work is a follow-up article to “Automate furnace controls to improve safety and energy efficiency,” which was published in the June 2014 edition of Hydrocarbon Processing.

Mickity, D., Phillips 66

 

https://www.hydrocarbonprocessing.com/magazine/2018/september-2018/special-focus-refining-technology/a-game-changing-approach-to-furnace-safeguarding

 

Role of fired heater safety systems

A fully automated burner management system operating as a SIS for burner control can meet minimum safety targets, improve system availability and lower costs

NIKKI BISHOP and DAVID SHEPPARD
Emerson Process Management

Role of fired heater safety systems

Design Options for Overfill Protection for Aboveground Atmospheric Tanks - Best Practices

"Overfilling of a tank is an important safety hazard.  It may result in loss of tank fluid and potentially severe consequences if the fluid is flammable or environmentally sensitive.   Additionally, it is necessary to preserve the mechanical integrity of a tank.   This article first looks briefly at various ways liquid may overfill a tank, and then describes different design options as best practices to take care of situations where overfilling is a possibility.   The main paper will contain diagrams and appropriate references."

 See this link https://www.aiche.org/academy/videos/conference-presentations/design-options-overfill-protection-aboveground-atmospheric-tanks-best-practices

DONT UNDERESTIMATE OVERFILLING RISKS

 "Loss of level control has contributed to three significant industrial incidents:

 In Australia, the Esso Longford explosion in September 1998 resulted in two fatalities, eight injuries, and A$1.3 billion (more than U.S. $ 1 billion) in losses [1];In the U.S., the BP Texas City explosion in March 2005 caused 15 fatalities and more than 170 injuries, profoundly affected facility production for months afterwards, and incurred losses exceeding $1.6 billion on BP [2]; andIn the U.K., the Buncefield explosion in December 2005 injured 43 people, devastated the Hertfordshire Oil Storage Terminal, and led to total losses of as much as ₤1 billion (about $1.5 billion) [3, 4]."

Read the article at https://www.chemicalprocessing.com/articles/2010/143/

Process safety time for fired heaters

The fired heater is a common unit operation in the refining and petrochemical industries that is used to increase the temperature of a process fluid. Fired heaters are required when a process-to-process heat exchanger or a utility exchanger (steam condenser, hot oil heater) cannot provide sufficient driving force to raise the temperature of a process fluid for downstream processing. There are numerous applications for fired heaters, from preheating feed to process units to reboiling distillation towers.

During the course of normal operation a fired heater will be exposed to disturbances in the supply of fuel, combustion air, or process fluid that may lead to a potentially hazardous condition developing. To manage these disturbances and take appropriate action to safely operate and control the fired heater, several layers of protective systems are normally provided.¹ These protective systems are designed to take independent action that will prevent the fired heater from reaching a hazardous condition.

 Continue reading at Process safety time for fired heaters

OSHA STANDARD FOR BREATHING AIR

OSHA Standard 29 CFR 1910.134(i)(1)
“Compressed breathing air shall meet at least the requirements for Grade D breathing air described in ANSI/Compressed Gas Association Commodity Specification for Air, G-7.1-1989, to include:
Oxygen content (v/v) of 19.5% - 23.5%;
Hydrocarbon (condensed) content of 5 milligrams per cubic meter of air or less;
Carbon monoxide (CO) content of 10 parts per million (ppm) or less;
Carbon dioxide (CO2) content of 1,000 ppm or less; and
Lack of noticeable odor”

OSHA'S RECOMMENDATIONS TO PREVENT INADVERTENT HOOKING UP OF BREATHING AIR INTO NITROGEN SYSTEMS

To help ensure that workers do not inadvertently hook up to inert gas supplies, the following recommendations should be implemented:

•Ensure that all requirements related to respiratory protection as outlined in29 CFR 1910.134 are met. Written standard operating procedures governing the selection and use of respirators must be developed and implemented. Requirements for training and instruction in the proper use of respirators and their limitations must be met at all facilities.

•Ensure (determine) that the couplings of the respirator air lines are incompatible with any other couplings/fittings for non-respirable air or gas delivery systems.Replace couplings on non-breathing air systems with another, incompatible type of coupling.

•Ensure that breathable air systems are not in any way interconnected to non-breathable air systems.

•Develop a maintenance procedure to address supply-line identification (labeling)and painting. Stress the purpose of color coding and the importance of completing detail painting in a timely fashion to ensure that this visual cue is always available to aid workers.

Source: Osha.gov

Is your relief valve sizing method truly rigorous?

Is your relief valve sizing method truly rigorous?

Pressure relief with rupture discs

Pressure relief with rupture discs

Protecting against high pressure rupture (TIA)

Protecting against high pressure rupture (TIA)

Process safety time for fired heaters

Process safety time for fired heaters

How To avoid PRV performance problems

 https://www.valvemagazine.com/magazine/sections/features/4427-how-to-avoid-prv-performance-problems.html

The working of a flame arrester

 

Process safety beacon on flame arrestor

 https://www.aiche.org/sites/default/files/cep/20160420.pdf

Can a flame arrester element be made of a non metallic element?

Flame arresters are often provided on vent lines in atmospheric storage tanks storing flammable materials. The principle of operation is by cooling the flame and extinguishing it before it reached the inside of the tank. As the flame travels through the element, it is exposed to a large area of the element, which can be folded meshes etc. But do you know that the element inside does not necessarily have to be metal? The flame arrester element itself experiences very little warming, because it is subjected to a high temperature for a very short time. Heat transfer is initially due to convection/diffusion and then later due to conduction after flame has been extinguished. Hence non metallic elements like PTFE can be used to avoid plugging. See one vendors catalogue here https://www.protego.com/products/detail/FA-I-PTFE.html

Note: This is for information only.