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Pour point liquid fuels

At lower temperatures, the crystals increase in size, and form networks that trap the liquid and hinder its ability to flow. The pour point is attained which can, depending on the diesel fuel, vary between -15 and -30°C. This characteristic (NF T 60-105) is determined, like the cloud point, with a very rudimentary device (maintaining a test tube in the horizontal position without apparent movement of the diesel fuel inside). [Pg.215]

Table 12-4 is a summary of liquid fuel speeifieations set by manufaeturers for effieient maehine operations. The water and sediment limit is set at 1% by maximum volume to prevent fouling of the fuel system and obstruetion of the fuel filters. Viseosity is limited to 20 eentistokes at the fuel nozzles to prevent elogging of the fuel lines. Also, it is advisable that the pour point be 20 °F (11 °C) below the minimum ambient temperature. Failure to meet this speeifieation ean be eorreeted by heating the fuel lines. Carbon residue should be less than 1% by weight based on 100% of the sample. The hydrogen eontent is related to the smoking tendeney of a fuel. Lower... [Pg.442]

Certain properties of a liquid fuel are measured routinely in a laboratory for characterization purposes. Besides density and viscosity, these properties include the pour point, the cloud point, and the flash point. Standard ASTM (American Society for Testing Materials) procedures are available for their determination. [Pg.324]

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]

Further cooling of the fuel leads to wax crystal formation throughout the fuel matrix. The growing wax crystals develop into a larger latticelike network encompassing the bulk fuel volume. This latticelike network eventually causes the fuel to become highly viscous and to eventually gel into a semisolid mass. The lowest temperature at which fuel remains in the liquid state just prior to gellation is called the pour point. [Pg.87]

Pour point ranges from 213 K (-80°F) for some kerosene-type jet fuels to 319 K (115°F) for waxy No. 6 fuel oils. Cloud point (which is not measured on opaque fuels) is typically 3 to 8 K higher than pour point unless the pour has been depressed by additives. Typical petroleum fuels are practically newtonian liquids between the cloud point and the boiling point and at pressures below 6.9 MPa (1000 psia). [Pg.2119]

The optimum pyrolysis temperature is 395°C to give a recovery ratio of 0.97 (i.e. 1000 kg polystyrene will yield 970 L liquid monomer) and 5 to 10% char residue. Fuel made from polystyrene feedstock will be high in aromatic character and have an energy content of 50 MJ/kg and a pour point of —67°C. However the flash point is only 26°C and the cetane rating only 12.6. The fuel needs to be blended with polyolefin-derived diesel or regular diesel in order to upgrade the flash point and cetane rating to within specification. [Pg.388]

U.S. Environmental Protection Agency (1975). The pour point, flash point, and viscosity determinations of the liquid fuel from RDF were made on the product containing 14 wt % water as produced. [Pg.251]

The hydrocracking process often produces relatively large amounts of iso-butane that can be used in alkylation units to prepare alkylate for gasoline blending. Hydrocracking, depending on the catalyst, can also cause isomerization of the paraffinic products that benefit liquid fuels in terms of pour point control and smoke point. [Pg.1282]

The pour point (ASTM D-97, IP 15) is the lowest temperature at which the fuel oil will flow under specified conditions. The maximum and minimum pour point temperatures provide a temperature window where a petroleum product, depending on its thermal history, might appear in the liquid as well as the solid state. Pour point data can be used to supplement other measurements of cold flow behavior, and the data are particularly useful for the screening of the effect of wax interaction modifiers on the flow behavior of petroleum. The pour point should not be confused with the freezing point, which is an index of the lowest temperature at which the crude oil will flow under specified conditions. Test methods (ASTM D-2386, ASTM D-5901, ASTM D-5972, IP 434, IP 435) for the freezing point are not usually applicable to fuel oil but are more applicable to diesel fuel and aviation fuel. [Pg.208]

Waten The standard method is to pour water onto the fire. This reduces the heat, hopefully to the point that the fire can no longer burn. However, water is not suitable for liquid fuel fires, because it is likely to spread the fuel and make the fire larger, nor for electrical fires because of the risk of electric shock. [Pg.193]

Crude oil is a substance which emerges from the ground as a thick, viscous, brown or dark green liquid. Some types like the deposits of Venezuela, contain primarily gasolines. Others, like those of Texas, are richer in fuel-oil while others like those of Mexico contain more bitumen for asphalt. The specific gravity varies and provides an indication of quality. Other criteria include pour- and cold-points, viscosity, optical properties, odor flash- and burning-points, color and coefficient of expansion. [Pg.41]


See other pages where Pour point liquid fuels is mentioned: [Pg.203]    [Pg.690]    [Pg.104]    [Pg.40]    [Pg.305]    [Pg.684]    [Pg.99]    [Pg.335]    [Pg.1518]    [Pg.237]    [Pg.316]    [Pg.587]    [Pg.815]    [Pg.85]    [Pg.36]    [Pg.158]    [Pg.247]   
See also in sourсe #XX -- [ Pg.155 , Pg.156 , Pg.305 , Pg.399 , Pg.401 ]




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