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Carbon dioxide, toxicity

Carbon dioxide is toxic, can be an asphyxiant by virtue of oxygen displacement (described above), and can cause death due to paralysis of the respiratory centres (Hoather and Wright, 1989). The threshold limit value for CO2 is 0.5% and concentrations above 5% result in laboured breathing, headaches and visual disturbances. The long term occupational exposure limit (OEL) is 5,000 vpm and the short term occupational exposure limit (STEL) is 1.5% by volume. In most situations arising from landfill gas-associated problems, carbon dioxide toxicity will only occur when collection in an enclosed environment occurs. Under these conditions there would also be potential for explosion due to potentially high methane levels and gas control measures would be required to alleviate such a potentially dangerous situation. [Pg.71]

To prepare gas for evacuation it is necessary to separate the gas and liquid phases and extract or inhibit any components in the gas which are likely to cause pipeline corrosion or blockage. Components which can cause difficulties are water vapour (corrosion, hydrates), heavy hydrocarbons (2-phase flow or wax deposition in pipelines), and contaminants such as carbon dioxide (corrosion) and hydrogen sulphide (corrosion, toxicity). In the case of associated gas, if there is no gas market, gas may have to be flared or re-injected. If significant volumes of associated gas are available it may be worthwhile to extract natural gas liquids (NGLs) before flaring or reinjection. Gas may also have to be treated for gas lifting or for use as a fuel. [Pg.249]

The most common contaminants in produced gas are carbon dioxide (COj) and hydrogen sulphide (HjS). Both can combine with free water to cause corrosion and H2S is extremely toxic even in very small amounts (less than 0.01% volume can be fatal if inhaled). Because of the equipment required, extraction is performed onshore whenever possible, and providing gas is dehydrated, most pipeline corrosion problems can be avoided. However, if third party pipelines are used it may be necessary to perform some extraction on site prior to evacuation to meet pipeline owner specifications. Extraction of CO2 and H2S is normally performed by absorption in contact towers like those used for dehydration, though other solvents are used instead of glycol. [Pg.252]

Because PTFE resins decompose slowly, they may be heated to a high temperature. The toxicity of the pyrolysis products warrants care where exposure of personnel is likely to occur (120). Above 230°C decomposition rates become measurable (0.0001% per hour). Small amounts of toxic perfiuoroisobutylene have been isolated at 400°C and above free fluorine has never been found. Above 690°C the decomposition products bum but do not support combustion if the heat is removed. Combustion products consist primarily of carbon dioxide, carbon tetrafluoride, and small quantities of toxic and corrosive hydrogen fluoride. The PTFE resins are nonflammable and do not propagate flame. [Pg.355]

Toxicity. The products of combustioa have beea studied for a number of plastic foams (257). As with other organics the primary products of combustion are most often carbon monoxide and carbon dioxide with smaller amounts of many other species depending on product composition and test conditions. [Pg.421]

Reactions. Heating an aqueous solution of malonic acid above 70°C results in its decomposition to acetic acid and carbon dioxide. Malonic acid is a useful tool for synthesizing a-unsaturated carboxyUc acids because of its abiUty to undergo decarboxylation and condensation with aldehydes or ketones at the methylene group. Cinnamic acids are formed from the reaction of malonic acid and benzaldehyde derivatives (1). If aUphatic aldehydes are used acryhc acids result (2). Similarly this facile decarboxylation combined with the condensation with an activated double bond yields a-substituted acetic acid derivatives. For example, 4-thiazohdine acetic acids (2) are readily prepared from 2,5-dihydro-l,3-thiazoles (3). A further feature of malonic acid is that it does not form an anhydride when heated with phosphorous pentoxide [1314-56-3] but rather carbon suboxide [504-64-3] [0=C=C=0], a toxic gas that reacts with water to reform malonic acid. [Pg.465]

Use of dry chemical, alcohol foam, or carbon dioxide is recommended for cycloahphatic amine fire fighting. Water spray is recommended only to flush spills away to prevent exposures. In the aquatic environment, cyclohexylamine has a high (420 mg/L) toxicity threshold for bacteria (Pseudomonasputida) (68), and is considered biodegradable, that is, rnineralizable to CO2 and H2O, by acclimatized bacteria. [Pg.212]

Butylenes are not toxic. The effect of long-term exposure is not known, hence, they should be handled with care. Reference 96 Hsts air and water pollution factors and biological effects. They are volatile and asphyxiants. Care should be taken to avoid spills because they are extremely flammable. Physical handling requires adequate ventilation to prevent high concentrations of butylenes in the air. Explosive limits in air are 1.6 to 9.7% of butylenes. Their flash points range from —80 to —73° C. Their autoignition is around 324 to 465°C (Table 2). Water and carbon dioxide extinguishers can be used in case of fire. [Pg.369]

When heated to about 60°C, nickel carbonyl explodes. Eor both iron and nickel carbonyl, suitable fire extinguishers are water, foam, carbon dioxide, or dry chemical. Large amounts of iron pentacarbonyl also have been reported to ignite spontaneously (189). Solutions of molybdenum carbonyl have been reported to be capable of spontaneous detonation (190). The toxicity of industrial chemicals including metal carbonyls may be found in references 191-194. [Pg.71]

In 1977, consumption of PET resin in bottie appHcations was dramatically increased when the EDA banned competing acrylonitrile resins owing to toxicity considerations (recentiy rescinded) (69) and when the 2 L bottie was accepted for beverage sales worldwide (70). The carbon dioxide barrier properties of PET are sufficient to provide the six-month shelf life necessary for carbonated beverages (qv) (see also Barrier polymers). [Pg.268]

Products of Combustion Heat, hght, smoke, and asphyxiating and toxic gases are produced by fire. In a hot, well-ventilated fire, combustion is usually nearly complete. Nearly all the carbon is converted to carbon dioxide, all the hydrogen to steam, and oxides of various other elements such as sulfur and nitrogen are produced. [Pg.2314]


See other pages where Carbon dioxide, toxicity is mentioned: [Pg.489]    [Pg.489]    [Pg.182]    [Pg.879]    [Pg.134]    [Pg.226]    [Pg.24]    [Pg.25]    [Pg.130]    [Pg.137]    [Pg.471]    [Pg.172]    [Pg.172]    [Pg.253]    [Pg.267]    [Pg.516]    [Pg.276]    [Pg.492]    [Pg.285]    [Pg.475]    [Pg.197]    [Pg.61]    [Pg.92]    [Pg.226]    [Pg.228]    [Pg.345]    [Pg.165]    [Pg.226]    [Pg.163]    [Pg.332]    [Pg.31]    [Pg.230]    [Pg.403]    [Pg.482]    [Pg.1]    [Pg.35]    [Pg.364]    [Pg.134]    [Pg.1540]   
See also in sourсe #XX -- [ Pg.480 ]

See also in sourсe #XX -- [ Pg.526 ]




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