Posts Tagged ‘ plant explosion ’

Understanding LEL of Common Combustible Gases

by Lukman Nulhakiem

LEL-of-common-combustible-gasesThere are many common combustible gases found in chemical plant. These combustible gases have one similarity. They can be ignited when their concentration in air are within their flammability limits.

What are flammability limits? Flammability limits or commonly known as explosive limits are defined as concentration of combustible gas in mixture with air in which they can be ignited and exploded in the presence of source of ignition.

The lowest concentration of a combustible gas in mixture with air where it still can be ignited is called by Lower Explosive Limit (LEL) or Lower Flammable Limit (LFL). Whereas, the highest concentration of a combustible gas in mixture with air where it still can be ignited is called by Upper Explosive Limit (UEL) or Upper Flammable Limit (UFL). (more…)

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Potential Hazards in Chemical Industries

The Most Common Potential Hazards in Chemical Industries

By Lukman Nulhakiem

 If we talk about potential hazards in chemical industries, there will be long discussion about that matter. Although one chemical plant has similar nature with one another, but each plant comes with its unique hazards.

potential hazards in chemical industriesIn this article, I will write about potential hazards in chemical industries in general which is in turn it can be used as inputs for preparing hazard identification work for your own plant site. This is very important mainly for companies which have not determined hazards list within their plant sites yet.

As a reminder, I recommend you to read my previous article about hazard identification study as well as hazard control methods if you have never experienced in making hazard list for your plant. (more…)

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Taking Notes From Middletown Power Plant Explosion

Middletown power plant exploded on last 7 February, when natural gas vent operation was being done. The accident caused at least 6 people died and several others injured. Several similar accidents had also occurred in the past.

In the Middletown power plant explosion, there were some important notes that we could take whenever we do similar operation. Chemical Safety Board said Middletown explosion was due to lack of safety measures. (more…)

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Static Spark and Non-Conductive Flammable Liquid

A plant accident video that was released by U.S Chemical Safety Board shows how static spark could cause fire explosion involving non-conductive flammable liquid. This video shows you that it is very important to understand property of handled flammable liquid, install inert gas purging system and prevent appearance of static electric spark in the flammable liquid tank. This accident occurred at Barton Solvents facilities in Valley Center, Kansas, on July 17, 2007. (more…)

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Chemical Plant Accident in October 2009

chemical-plant-accident-statisticIt is my strong intention to always present chemical plant accident stories in order to give you more inputs for safety improvements. I believe that many similar accidents had happened recurrently. But most of us do not aware about this.

According to OSHA report regarding top 10 workplace safety violations for 2009, violation number increases by 30% compared with last year data.

Read the story below carefully. Take important notes from these stories. And improve your safety system accordingly. (more…)

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A Brief Introduction to Combustible Dust Explosion

In the previous post, I have posted about Chemical Safety Board report on explosion at Imperial Sugar Company, USA. Combustible dust sugar was related to that accident. Then, what does a dust explosion mean actually? According to wikipedia, a dust explosion is the combustion of a particle(s) of dust suspended in the air in an enclosed location, resulting in overpressure, thermal radiation, and ensuing projectiles.

From the basic point of view, a fire can only exist whenever an oxidant (oxygen), a combustible material and a source of ignition come together. The three components are famously called by the fire triangle. Meanwhile, in the case of dust explosion, it requires not only the fire triangle components but also combustible dust material must be in an enclosed space or confined space and suspended in the air at the certain concentration.  (more…)

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Taking Notes from T2 Plant Explosion

t2-plant-explosionA runaway reaction that caused explosion at T2 plant on 19 December 2007 had caused four persons died. Cooling pipe blockage or failed valve probably caused the temperature and pressure inside the batch reactor to become uncontrolled and the relief system could not work to save the system.

I am very interested to what Robert Hall, CSB investigation supervisor, said about T2 plant accident as reported by tce recently. It directly deals with how hazard identification or HAZOP study holds a vital role in recognizing uncontrolled reaction risk since process designing phase. (more…)

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