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Transport of fuels

The pour point represents the lowest temperature at which the liquid fuel will pour. This is a useful consideration in the transport of fuels through pipelines. To determine the pour point, an oil sample contained in a test tube is heated up to 115°F (46°C) until the paraffin waxes have melted. The tube is then cooled in a bath kept at about 20°F (11°C) below the estimated pour point. The temperature at which the oil does not flow when the tube is horizontally positioned is termed the pour point. [Pg.324]

Regulation of the rate of transport of fuels, according to the requirements of the cell or extracellular signals (e.g. hormones). [Pg.85]

The fluidity of a membrane is difficult to define but it is known to increase the rate of lateral movement of proteins in the membrane and the activity of some membrane proteins, such as ion channels and transporters of fuels (Chapter 5). Fluidity depends, in part, upon the amount and the degree of unsaturation of the fatty acids that are present... [Pg.236]

The government has developed regulations and guidelines for fuel oils and some of the chemicals in them. These are designed to protect the public from the possible harmful health effects of these chemicals. The Department of Transportation also regulates the transportation of fuel oils, because they are classified as hazardous materials that are considered to pose a risk to health, safety, or property when transported. [Pg.24]

ANFO can be mixed directly in the shot-hole by first pouring the ammonium nitrate into the shot-hole followed by the fuel oil. The main advantage of mixing on site is that no safety procedures are required for the transportation of fuel oil and ammonium nitrate, since fuel oil and ammonium nitrate are not classed as explosives. It is only when they are mixed together that the composition becomes an explosive substance. [Pg.141]

In Diesel fuel combustion, the physical processes include metering and transportation of fuel and air into the combustion chamber, vaporization of fuel, mixing fuel vapor with air, and provision of an environment favorable for rapid chemical reaction. The chemical processes include self-ignition or autoignition of the fuel-air mixture, and extensive chemical reaction to liberate the potential energy in the fuel. The accomplishment of these processes is the basic consideration in the design of the Diesel engine. [Pg.281]

Information on phosphorus retention (Table V) is less abundant than that on lead. The presence of lead phosphates in used catalysts has been noted (26, 35). The retention and possibly its ability to poison a catalyst, as well, of phosphorus originating from fuel, will depend on the presence of lead. The work of McArthur (26) shows very low P retention from the fuel as compared with that from oil. The ad hoc explanation offered is that whereas P205 is the most likely form for the transport of fuel phosphorus, other forms may prevail for the oil phosphorus. This, indeed, may be so if one realizes that the oil contains species such as Zn and alkaline earth metals which form very stable phosphates. The harmful effects and the distribution of phosphorus might well be influenced by such differences, as will be discussed subsequently. [Pg.324]

Fire is referred to as a combustion process in which the fuel and oxidant are transported separately to the reaction zone during the combustion. Because the rate of combustion in fires is limited by the rate of transportation of fuel and oxidant molecules, which are usually slower than the rate of oxidation, fires do not cause rapid pressure buildup. Gas explosions are combustions of premixed fuel-oxidant mixtures in confined spaces. [Pg.1109]

Comparison of current densities, and the potenhal for onset and for maximum current, is hampered when attempts are made, as will be undertaken in the following sechons, to report on results from diverse sources, as there is as yet poor adherence to normalization of such data to standard or accepted conditions. The variability in experimental approaches includes differences, often unspecified, in specific surface areas of the elechodes used, the control of mass transport of fuel/ oxygen to the surface, the coverage and activity of the enzyme on the surface, the stabihty of the system, the operational (and ophmal) condihons (pH, ionic strength. [Pg.234]

The steady state temperature of the catalyst surface under mass-transport-limited conditions can exceed the adiabatic flame temperature if the rate of mass transport of fuel to the surface is faster than the rate of heat transport from the surfaee. The ratio of mass diffusivity to heat dilTusivity in a gas is known as the Lewis number. Reactor models [9] show that for gases with a Lewis number close to unity, such as carbon monoxide and methane, the catalyst surface temperature jumps to the adiabatic flame temperature of the fuel/air mixture on ignition. However, for gases with a Lewis number significantly larger than unity the rate of mass transport to the surface is much faster than the rate of heat transport from the surface, and so the wall temperature can exceed the adiabatic gas temperature. The extreme case is... [Pg.186]

The Vision 21 Program [73] is promoting research and innovation to maintain cost-competitive options for using a diverse mix of fossil fuels for power generation. A key element of this program is the effective removal of current environmental concerns and impediments associated with producing electricity and transportation of fuels from fossil fuels, including natural gas, petroleum, and coal. [Pg.628]

An allocation of emissions to Parties followed by differential regulation of the emissions attributed to Annex I and non-Annex I Parties will induce behaviour that reduces the effectiveness of the regulations. Under option 2, for example, bunker fuel sold in Annex I Parties would be more costly than fuel sold in non-Annex I Parties, because Annex I Parties would need to regulate the emissions associated with the fuel use. This would shift fuel purchases to non-Annex I Parties and lead to increased transport of fuel purchased there - tankering - thus reducing the effectiveness of the Annex I regulations to limit emissions. [Pg.82]

At the moment, there are no transport packages in Russia that are suitable for the transportation of fuel elements and fuel bundles of reactor VVER-1000 with fresh mixed fuel. VNIPIET has performed design studies for such packages and appropriate auxiliaries. The work was conducted in two directions ... [Pg.74]

Transportation of fuel elements in both types of packages is carried out in a technological canister. Structure, size, and design of the canister are analogous to that of the fuel bundle. Capacity of the canister is up to 180 fuel elements or rods. [Pg.75]

NAGAKURA, T, MAKI, Y, TANAKA, N., Safety evaluation on transport of fuel at sea and test program on full scale cask in Japan , Packaging and Transportation of Radioactive Materials, PATRAM 78 (Proc. Symp. New Orleans, 1978), Sandia Laboratories, Albuquerque, NM (1978). [Pg.150]

The pores are for the transport of fuel cell reactants and product(s). Optimal porosity and pore size distribution can facilitate the mass transport process to minimize the fuel cell performance loss due to concentration overpotential. If some pores are more hydrophobic than others, what is the relative distribution Is the distribution of pore sizes and hydrophobicity within the allowable range ... [Pg.4]

The design of metal casks for storage has been derived from existing casks for transportation of fuel assemblies. The cask design in most cases takes into account the conditions for storage as well as for transportation. There is a large variety of casks available commercially for many different types of spent fuel assemblies (PWR, BWR, HTR, WER, RBMK, FBR). Steel or nodular cast iron casks... [Pg.125]

This group of characteristics specifies on-site facilities designed to contain the spent fuel assemblies discharged from the reactor. Basically, there can be two types of spent fuel storage facilities available on site to the unit a spent fuel pool and an interim spent fuel storage facility. The spent fuel pool is usually located in the containment or in the reactor building next to the reactor to facilitate the transport of fuel from the reactor to the pool by a refuelling machine. The spent fuel pool is partially filled with water and the assemblies are left in the... [Pg.24]

The packaging and transport of fuel assemblies with fresh and irradiated fuel shall be carried out in accordance with national and international requirements and, as appropriate, in accordance with Ret [18]. [Pg.84]


See other pages where Transport of fuels is mentioned: [Pg.243]    [Pg.85]    [Pg.93]    [Pg.190]    [Pg.286]    [Pg.141]    [Pg.104]    [Pg.28]    [Pg.54]    [Pg.171]    [Pg.544]    [Pg.45]    [Pg.46]    [Pg.160]    [Pg.362]    [Pg.157]    [Pg.45]    [Pg.46]    [Pg.100]    [Pg.149]    [Pg.188]    [Pg.24]    [Pg.238]    [Pg.385]    [Pg.53]    [Pg.409]    [Pg.703]    [Pg.156]   
See also in sourсe #XX -- [ Pg.238 ]




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