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When a flammable liquid (e.g.. gasoline) ignites, the substance actually buming is vapor generated from the liquid. If the concentration of the vapor in the air above the liquid exceeds a certain level (the lower flammability limit), the vapor will ignite if it is exposed to a spark or another ignition source. Once ignited, the heat released is likely to cause additional vaporization of the liquid, and the resulting fire may continue until all combustible material has been consumed.(a) The flash point is defined as the minimum temperature at which a flammable liquid or volatile solid gives off sufficient vapor to form an ignitable mixture with air near the surface of the liquid or within a vessel (page \(2-515,\) Perry's Chemical Engineers' Handbook, see Footnote 1 ). For example, the flash point of \(n\) -octane at 1.0 atm is \(13^{\circ} \mathrm{C}\left(55^{\circ} \mathrm{F}\right)\), which means that dropping a match into an open container of octane is likely to start a fire in a laboratory, but not outside on a cold winter day. (Do not try it! One reference- -L. Bretherick, Bretherick's Handbook of Reactive Chemical Hazards, 4th Edition, Butterworths, London, 1990, p. 1596 - points out there is "usually a fair [our emphasis] correlation between flash point and probability of involvement in fire.")Suppose you are keeping two solvents in your laboratory, one with a flash point of \(15^{\circ} \mathrm{C}\) and the other with a flash point of \(75^{\circ} \mathrm{C}\). How do these solvents differ from the standpoint of safety? What differences, if any, should there be in how you treat them?(b) The lower flammability limit (LFL) of methanol in air is 6.0 mole \(\%\). Calculate the temperature at which a saturated methanol-air mixture at 1 atm would have a composition corresponding to the LFL. What is the relationship of this value to the flash point, and what value would you assign the flash point of methanol?(c) Give reasons why it would be unsafe to maintain an open container of methanol in an environment below the LFL (i.e., the value calculated in Part (b)) if there are ignition sources nearby. List common ignition sources that may be found in a laboratory.

Short Answer

Expert verified
The solvent with a flash point of 15°C is riskier than the 75°C solvent because it takes a lower temperature to emit sufficient vapors that could ignite. It thus requires more careful handling. The lower flammability limit (LFL) of methanol at specific temperature implies that at this temperature methanol emits sufficient vapors that can be ignited. The flash point is lower than the LFL temperature which makes it unsafe to store methanol in open containers at a temperature below LFL if there are ignition sources nearby. Typical ignition sources in a laboratory include electrical appliances, open flames, static electricity and hot surfaces.

Step by step solution

01

Compare solvent safety based on flash point

The solvent with a flash point of 15°C is more risky than the one with a 75°C flash point. The risk comes from the fact that a lower flash point means that it takes a lower temperature for the solvent to emit sufficient vapors that can be easily ignited by a spark or another ignition source. As such, the solvent with a flash point of 15°C takes a lower temperature to ignite than the one at 75°C, thus making it more prone to start a fire. The treatment for each of these solvents should therefore be different with the one with the lower flash point requiring more careful handling like avoiding sparks or flames.
02

Calculate the LFL of a methanol-air mixture

Methanol’s LFL in air is 6.0 mole%. This denotes the minimum concentration at which methanol vapors in the air can ignite. From the Antoine equation, we can determine the vapor pressure of methanol at different temperatures then convert that vapor pressure into mole fraction in air. The Antoine constants for methanol are: A=7.89750, B=1473.11, C=-15. For an LFL of 6.0 mole%, this corresponds to a vapor pressure of 0.06 atm (as the total pressure is 1 atm). Solving the Antoine equation for temperature will provide the temperature that corresponds to the LFL.
03

Discuss the relationship between LFL and flash point

The flash point of a substance is generally lower than the temperature at which the LFL is reached. The flash point of methanol is about 11°C but the temperature that corresponds to the LFL from the calculations is less. It means methanol will start producing flammable vapors at a lower temperature than it will ignite.
04

Reasons to avoid keeping open container of methanol in environment below LFL

Keeping an open container in an environment below the LFL means the methanol is under a temperature at which it is producing enough vapors that can ignite upon the presence of a spark. Therefore, if there are ignition sources nearby, it can easily result in a fire or explosion. Ignition sources in a laboratory can be numerous: electrical appliances, open flames, static electricity, hot surfaces, among others.

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Key Concepts

These are the key concepts you need to understand to accurately answer the question.

Flash Point
Understanding the flash point of a substance plays a crucial role in evaluating potential fire hazards. It is defined as the minimum temperature at which a flammable liquid or volatile solid can generate enough vapor to form an ignitable mixture with air near the surface of the substance. This concept directly correlates with fire safety, particularly in environments like laboratories where flammable materials are common. For instance, considering the different flash points of two solvents – one with a flash point of \(15^\circ \mathrm{C}\) and another at \(75^\circ \mathrm{C}\) – significantly impacts their safety handling protocols. The lower the flash point, the greater the risk of ignition at a lower temperature. Therefore, the solvent with the \(15^\circ \mathrm{C}\) flash point is more susceptible to catching fire and requires more stringent safety measures to prevent accidents, such as thorough ventilation and avoiding any heat sources or open flames.

Particularly in a laboratory setting, distinguishing between chemicals based on flash point can inform the way they are stored and handled. Chemicals with lower flash points should not only be kept in well-ventilated areas but may also require refrigeration to maintain temperatures below the flash point, thus reducing the risk of a vapor-related fire.
Methanol Safety
Methanol is a commonly used solvent and fuel, which, due to its properties, necessitates specific safety precautions. These safety measures stem from understanding methanol's lower flammability limit (LFL), which is the minimum concentration of vapor in the air that can propagate flame when an ignition source is present. Methanol's LFL is 6.0 mole%, a critical value to consider when working with it to prevent fire or explosion hazards.

With this in mind, safety protocols for methanol include proper labeling and storage, as well as the use of flame arrester-equipped containers to prevent vapor ignition. Workers should use personal protective equipment, such as safety goggles and gloves, when handling methanol to prevent skin and eye contact. Additionally, in the case of a spill, immediate action should be taken to clean it up, and proper disposal procedures should be followed to prevent environmental contamination or further safety risks. Understanding and adhering to these safety measures are key to preventing accidents and ensuring a safe working environment.
Laboratory Fire Prevention
Fire prevention in a laboratory involves a combination of practices, equipment, and knowledge designed to reduce the risk of accidental fires. Common ignition sources in a laboratory setting include electrical equipment that might malfunction, open flames from Bunsen burners, static discharge which can spark unexpectedly, and hot surfaces like heating plates. To avoid fires, it's essential to maintain proper separation between flammable materials and ignition sources.

Regular safety audits and training are vital to ensure all laboratory personnel are aware of how to handle flammable substances safely, including understanding the importance of flash points and LFLs. Additionally, installing safety equipment such as fire extinguishers, fire blankets, and having an accessible emergency shower and eyewash station are critical components of a comprehensive fire safety plan. Most importantly, however, is cultivating a culture of safety where all lab workers know to prioritize safe handling practices, including the proper storage of chemicals in flameproof cabinets and routine checks for leaks or any other potential hazards.

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Most popular questions from this chapter

The pressure in a vessel containing methane and water at \(70^{\circ} \mathrm{C}\) is 10 atm. At the given temperature, the Henry's law constant for methane is \(6.66 \times 10^{4}\) atm/mole fraction. Estimate the mole fraction of methane in the liquid.

When fermentation units are operated with high aeration rates, significant amounts of water can be evaporated into the air passing through the fermentation broth. since fermentation can be adversely affected if water loss is significant, the air is humidified before being fed to the fermenter. Sterilized ambient air is combined with steam to form a saturated air-water mixture at 1 atm and \(90^{\circ} \mathrm{C}\). The mixture is cooled to the temperature of the fermenter \(\left(35^{\circ} \mathrm{C}\right),\) condensing some of the water, and the saturated air is fed to the bottom of the fermenter. For an air flow rate to the fermenter of \(10 \mathrm{L} / \mathrm{min}\) at \(35^{\circ} \mathrm{C}\) and \(1 \mathrm{atm},\) estimate the rate at which steam must be added to the sterilized air and the rate (kg/min) at which condensate is collected upon cooling the air-steam mixture.

Air at \(25^{\circ} \mathrm{C}\) and 1 atm with a relative humidity of \(25 \%\) is to be dehumidified in an adsorption column packed with silica gel. The equilibrium adsorptivity of water on silica gel is given by the expression \(^{19}\).$$X^{*}(\mathrm{kg} \text { water/ } 100 \mathrm{kg} \text { silica gel })=12.5 \frac{p_{\mathrm{H}_{2} \mathrm{O}}}{p_{\mathrm{H}_{2} \mathrm{O}}^{*}}$$ where \(p_{\mathrm{H}_{2} \mathrm{O}}\) is the partial pressure of water in the gas contacting the silica gel and \(p_{\mathrm{H}, \mathrm{O}}^{*}\) is the vapor pressure of water at the system temperature. Air is fed to the column at a rate of 1.50 L/min until the silica gel is saturated (i.e., until it reaches equilibrium with the feed air), at which point the flow is stopped and the silica gel regenerated. (a) Calculate the minimum amount of silica gel needed in the column if regeneration is to take place no more frequently than every two hours. State any assumptions you make. (b) Briefly describe this process in terms that a high school student would have no trouble understanding. (What is the process designed to do, what happens within the column, and why is regeneration of the column packing necessary?)

The feed to a distillation column (sketched below) is a 45.0 mole\% \(n\) -pentane- 55.0 mole\% n-hexane liquid mixture. The vapor stream leaving the top of the column, which contains 98.0 mole\% pentane and the balance hexane, goes to a total condenser (which means all the vapor is condensed). Half of the liquid condensate is returned to the top of the column as reflux and the rest is withdrawn as overhead product (distillate) at a rate of \(85.0 \mathrm{kmol} / \mathrm{h}\). The distillate contains \(95.0 \%\) of the pentane fed to the column. The liquid stream leaving the bottom of the column goes to a reboiler. Part of the stream is vaporized; the vapor is returned to the bottom of the column as boilup, and the residual liquid is withdrawn as bottoms product.(a) Calculate the molar flow rate of the feed stream and the molar flow rate and composition of the bottoms product stream. (b) Estimate the temperature of the vapor entering the condenser, assuming that it is saturated (at its dew point) at an absolute pressure of 1 atm and that Raoult's law applies to both pentane and hexane. Then estimate the volumetric flow rates of the vapor stream leaving the column and of the liquid distillate product. State any assumptions you make. (c) Estimate the temperature of the reboiler and the composition of the vapor boilup, again assuming operation at 1 atm.(d) Calculate the minimum diameter of the pipe connecting the column and the condenser if the maximum allowable vapor velocity in the pipe is \(10 \mathrm{m} / \mathrm{s}\). Then list all the assumptions underlying the calculation of that number.

An important parameter in the design of gas absorbers is the ratio of the flow rate of the feed liquid to that of the feed gas. The lower the value of this ratio, the lower the cost of the solvent required to process a given quantity of gas but the taller the absorber must be to achieve a specified separation.Propane is recovered from a 7 mole \(\%\) propane \(-93 \%\) nitrogen mixture by contacting the mixture with liquid \(n\) -decane. An insignificant amount of decane is vaporized in the process, and \(98.5 \%\) of the propane entering the unit is absorbed.(a) The highest possible propane mole fraction in the exiting liquid is that in equilibrium with the propane mole fraction in the feed gas (a condition requiring an infinitely tall column). Using Raoult's law to relate the mole fractions of propane in the feed gas and liquid, calculate the ratio \(\left(\dot{n}_{L_{1}} / \dot{n}_{G_{2}}\right)\) corresponding to this limiting condition.(b) Suppose the actual feed ratio \(\left(\dot{n}_{L_{1}} / \dot{n}_{G_{2}}\right)\) is 1.2 times the value calculated in Part (a) and the percentage of the entering propane absorbed is the same (98.5\%). Calculate the mole fraction of propane in the exiting liquid.(c) What are the costs and benefits associated with increasing \(\left(\dot{n}_{L_{1}} / \dot{n}_{G_{2}}\right)\) from its minimum value [the value calculated in Part (a)]? What would you have to know to determine the most cost-effective value of this ratio?

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