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Released vapor

Ammonium cyanide [12211-52-8] NH CN, a colorless crystalline soHd, is relatively unstable, and decomposes into ammonia and hydrogen cyanide at 36°C. Ammonium cyanide reacts with ketones (qv) to yield aminonitriles. Reaction of ammonium cyanide with glyoxal produces glycine. Because of its unstable nature, ammonium cyanide is not shipped or sold commercially. Unless it is kept cool and dry, decomposition releases vapors and forms black hydrogen cyanide polymer. [Pg.386]

Evaporator may refer either to the type of constmction utilized or to the entire assemblage of equipment in a single installation. Thus a single multiple-effect evaporator may contain a number of effects of either the same or different evaporator types. An effect is a section of the evaporator heated by steam at one pressure and releasing vapor (water) at a lower pressure to another section. The term steam generally indicates the heat supply, whereas vapor means the material evaporated. Thus vapor from one effect becomes steam at the next effect. The term prime steam identifies the steam suppHed from an outside source to operate the evaporator (see also Steam). An effect may consist of several bodies, all operating at the same steam and vapor pressures. The purpose of more than one body in an effect may be to handle Hquor at different concentrations, or the result of size limitations or of additions to increase the capacity of an existing evaporator. [Pg.472]

Each PR valve must be installed so that the bonnet vent does not allow released vapors to impinge on lines or equipment, or towards personnel walkways. Where necessary, a short nipple and elbow should be added to direct flow away from such areas. In these cases, the vent piping should discharge horizontally to avoid entry of rainwater and debris, and should terminate in a position which is accessible for leak testing. [Pg.161]

An explosion in the engine room of an LNG carrying ship berthed at the jetty could release vapor cloud, whose explosion would have serious consequences. No amelioration was suggested by the team. Release of cargo, from ship collision was discounted because of the eight knots speed limit. [Pg.435]

The second category includes BLEVE simulation, in which a pressurized, heated flask containing liquid or liquefied fuel is broken after the desired vapor pressure has been reached, and the released vapor is then ignited. Measurement of fireball diameter, liftoff time, combustion duration, and final height is captured by filming with high-speed cameras. Radiometers are used to measure radiation and temperature is measured by thermocouples or by determination of fireball color temperature (Lihou and Maund 1982). [Pg.161]

Vapor pressure, which is the tendency of a liquid to release vapors to the surrounding area, goes down as MW increases but goes up as temperatures rise. By definition, the more volatile a liquid, the higher its vapor pressure and the lower its boiling point. Examples are ... [Pg.533]

Vents, Drains, Sample Ports Failures Small diameter piping or valves may be opened or fail which release vapors or liquids to the environment unexpectedly. [Pg.42]

Operator error released vapors to open vessel under maintenance. [Pg.67]

Level controller allowed cold liquid to enter pipe causing metallurgical failure of 1.57 inch pipe connection to a feed drum released vapors ignited by furnace 14 Fatalities, 22,892,000 loss... [Pg.68]

Failure of piping releasing vapors and causing an explosion... [Pg.71]

Linden, NJ, USA, Refinery, Explosion/Fire Failure of a dead leg piping released vapors 17,500,000... [Pg.71]

Borger, TX, USA, Refinery, Explosion/Fire Pipe or vessel failure released vapor cloud 36,000,000 loss... [Pg.72]

Metallurgical failure of laminated reactor vessel released vapors. [Pg.73]

Leaking heat exchangers released vapors which ignited. [Pg.74]

Pascagoula, MS, USA, Chemical Plant, Explosion/Fire Suspected leaking valves released vapors that were ignited 10,000,000 loss... [Pg.76]

If open sampling is provided, the sampling point should be located where adequate dispersion of released vapors will occur. The sampling point should be located so it is easily accessible so human error factors are reduced. [Pg.155]

Water curtains can also cool or eliminate available ignition source to a released vapor cloud. In this fashion they can also be a mitigating feature to prevent vapor cloud explosions. Hot surfaces, sparking devices and open flames in the immediate area of a vapor release can all be eliminated as a result of a directed water curtain where these sources exist. [Pg.211]

LNAPL recovery projects require careful planning, operation, and management. Some additional factors become important at unforeseen times. Recovery of free product often produces flammable vapors at concentrations that can violate air quality standards if freely released. Vapor treatment should be considered early in the design process. Storage of flammable liquids in appropriate containers is necessary. [Pg.342]

Cast iron casings, where recommended for chemical services, are for nonhazardous locations only. Steel casings (2.11.1.4) should be used for pumps in services located near process plants or in any location where released vapor from a failure could create a hazardous situation or where pumps could be subjected to hydraulic shock, for example, in loading services. [Pg.128]

Figure l Schematic of pre-concentrator designed to trap particulate matter including traces of explosives on a metal mesh screen. After a sample collection step, the apertures are closed, gas is passed at a low flow rate over the mesh which is resistively heated to 200°C or more, releasing vapors into the gas flow and passed to an analyzer, commonly an ion mobility spectrometer. [Pg.174]

At room temperature, 1,4-dichlorobenzene is a white solid with a strong odor that you would probably recognize as the smell of mothballs. When a package of 1,4-di chlorobenzene is opened, it slowly changes from a solid into a vapor and is released into the atmosphere. The released vapor acts as a deodorizer and insect killer. Most of the 1,4-di chlorobenzene that is released to the general environment is present as a vapor. 1,4-Dichlorobenzene can burn, but does not burn easily. Most people begin to smell 1,4-di chlorobenzene when it is present in the air at a concentration of 0.18 parts per million (ppm) and in water at a concentration of 0.011 ppm. [Pg.22]

Fire Point Temperature The temperature a liquid must be before the released vapor is in sufficient quantity to continue to bum, once ignited. [Pg.235]

Figure 28-13 Extraction vessels in a microwave oven that processes up to 12 samples in under 30 min. Each 100-mL vessel has a vent tube that releases vapor if the pressure exceeds 14 bar. Vapors from the chamber are ultimately vented to a fume hood. The femperature inside each vessel can be monitored and used to control the microwave power. [Courtesy CEM Corp.. Matthews. NC.]... Figure 28-13 Extraction vessels in a microwave oven that processes up to 12 samples in under 30 min. Each 100-mL vessel has a vent tube that releases vapor if the pressure exceeds 14 bar. Vapors from the chamber are ultimately vented to a fume hood. The femperature inside each vessel can be monitored and used to control the microwave power. [Courtesy CEM Corp.. Matthews. NC.]...
Atmospheric vapor. Vapor results from pesticide volatilization during spray release, vaporization from leaf deposits, and, over a longer time period, desorption from the soil and litter of the forest floor. Several reviews of this subject appear elsewhere in this Symposium volume. [Pg.228]

Brown, P. M., R. H. Hiltz and J. E. Brugger, 1990. Detoxification of Released Vapors/Par-ticles by Entrapment in Chemically Active Foam. Proceedings SuperFund 1990, pp. 589-594. Washington, D.C. [Pg.88]

A workshop report indicates that building architecture can induce a downwash of vapor clouds, cause channeling between structures, and produce local effects that could bring about mixing and other types of motion (Meroney, 1992). Therefore, emergency response plans for entry into process areas must anticipate the potential encounter of released vapors in high concentrations because of drafts and eddies caused by process equipment and buildings. [Pg.111]

Backstreaming can be one of the main limitations for mechanical pumps to achieve a better vacuum. Because molecular sieve and Micromaze traps are so efficient at capturing (and not releasing) vapors, Strattman experimented with a Micromaze foreline trap to trap the hydrocarbon oils from a mechanical pump. After proper baking and cooling, he was able to achieve pressures of 10 5 torr consistently with only a mechanical vacuum pump. [Pg.390]

Container Cleanliness of Marketing Product The previous cleanliness of containers filled with the product will depend on their transportation exposure, composition, and storage conditions. Glass containers usually carry at least mold spores of different microorganisms, especially if they are transported in cardboard boxes. Other containers and closures made with aluminum, Teflon, metal, or plastic usually have smooth surfaces and are free from microbial contamination but may contain fibers or insects [45], Some manufacturers receive containers individually wrapped to reduce contamination risks and others use compressed air to clean them. However, the cleanliness of wrapped containers will depend on the provider s guarantee of the manufacturing process and compressed-air equipment may release vapors or oils that have to be tested and validated [6],... [Pg.336]


See other pages where Released vapor is mentioned: [Pg.225]    [Pg.70]    [Pg.89]    [Pg.46]    [Pg.125]    [Pg.61]    [Pg.175]    [Pg.175]    [Pg.176]    [Pg.178]    [Pg.179]    [Pg.179]    [Pg.192]    [Pg.181]    [Pg.181]    [Pg.180]    [Pg.74]    [Pg.76]    [Pg.150]    [Pg.4978]    [Pg.148]   
See also in sourсe #XX -- [ Pg.11 , Pg.12 , Pg.13 ]




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Vapor release

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