Document babQEXVLLmNqMJyQLX9nBbGY1

358 CHAPTER 14 1957 Guide A. Indexes based on a single physical test: (1) API\ gravity', (2) Aniline point*, (3) Institute ojPetroleum smoke test, (4) Carbon-Hydrogen ratio based on fluegas analysis or ultimate analysis, and (5) Percent aromatics determined by sulfuric acid absorption tests*. B. Indexes based on two or more physical tests: (1) Diesel index' based on API 'gravity and aniline point, (2) Institute of Petroleum cetane number 10 based on the API gravity and 50 percent distillation point, (3) Universal Oil Products characteri zation factor11 based on specific gravity and average boiling point, (4) Burning index11 based on API gravity and 50 percent distillation point, and (5) Estimated CarbonHydrogen ratio1* based on API gravity aniline point, and boiling point. Various investigators have shown correlation between one or more of these indexes and the performance of fuel oils in oil burners. Experiments o Smoke Spot Reflectance for 60% of Ultimate -GO* a Per Cent of Ultimate CO* for 60% Relotlve Reflectance Fig. 4. Correlation of Burning Qualities of Fuel Oils with Four Combustion Indexes conducted with the Oil Heat Institute Reference Test Unit14 indicated good' correlation between the smoking tendency of fuel oils and API gravity? burning index, Diesel index, and hydrogen-carbon ratio for a limited num? ber of oils in laboratory apparatus simulating a pressure-atomizing burnerl These results are shown graphically in Fig. 4. Smoking tendency is given1 here in terms of smoke spot reflectance, the light reflectance of a smoke-1 soiled filter paper. A high reflectance, relative to a clean filter paper4 indicates low smoking tendency. COi/U is the observed COt divided ;bj the ultimate or maximum theoretical COi expressed as a percentage. , and Hersberger11 have related burning. qualities and burning index, various oils in a wall-flame burner. Cauley and Delgass13 cite test resul"', on combustion indexes obtained with vaporizing burners. The present- experimental data are probably too meager as yet to correlate adequately^: any one of these indexes with burning qualities of oil fuel for all types0!*, burners. Few attempts have been made to suggest limits for any of these^ Fuels and Combustion 359 fuel oil indexes for particular applications, even though correlations be tween them and burning qualities have been observed. In other words, none of the above mentioned indexes has yet gained sufficiently wide usage to replace the grading of oils by Commercial Standard CS12-48. Experiments have shown that thermal decomposition or cracking of hydrocarbons begins at a temperature of approximately 680 F at atmos pheric pressure, although the temperature of cracking varies somewhat above and below this value. Thus pure distillate fuel oils, whose end point does not exceed this temperature, can usually be completely evaporated in vaporizing-type oil burners at atmospheric pressure without leaving a residue or without cracking of the hydrocarbons. Fuel oils that cannot be completely evaporated below 680 F are likely to undergo cracking in vaporizing type burners, with the resulting possibilities of smoky combus tion and residues in the oil burner. A complete distillation curve cannot usually be determined for fuel oils containing fractions that evaporate above 680 F. Since No. 1 grade fuel oil in Commercial Standard CS12-48 has a maxi mum end point of 625 F, it can in most cases be completely evaporated in atmospheric vaporizing burners without cracking, although occasionally an oil is found that undergoes cracking at temperatures below 625 F. By the same criterion, No. 2 grade fuel oil in the Commercial Standard, which can have a maximum distillation temperature of 675 F at the 90 percent point, would frequently be cracked in a vaporizing burner. How ever some No. 2 fuel oils do not crack before complete evaporation takes place. Vaporizing-type burners can generally use only No. 1 fuel oil with assurance that thermal decomposition will not occur during combustion. On the other hand either No. 1 or No. 2 fuel oils may be employed in high or low pressure atomizing burners when the temperatures developed in the combustion chamber are high enough to assure complete combustion, even if the fuel oil is thermally decomposed. . In vaporizing burners, preheating of the combustion air and fuel, com plete evaporation of fuel before it is exposed to. intense heat, and thorough mixing of the air and gasified fuel promote complete combustion without smoke and with a minimum of excess air. In pressure-type burners pre heating of the combustion air, a maximum of air turbulence, good atomiza tion of the fuel, and high combustion chamber temperatures (preferably red hot) promote smokeless combustion with a minimum of excess air. Natural draft burners depend on the motivating force of a chimney to mduce enough air into the burner for complete combustion. Forced draft burners are supplied with combustion air by means of a blower or fan; the chmmey merely conducts the flue gases outdoors and prevents leakage Afr Ue as.es inside the building. More details on the operation of the different kinds of oil burners and on chimneys and draft will be found in Chapters 15 and 17 respectively. A* VUA/ VAUJkU ^Uei gsses employed for various heating and air conditioning processes fiJoughout the United States fall into three broad classifications: natural, n~nufactured, and liquefied petroleum. Natural gas is a mixture of several frii ^'ifie. gases and, usually, a small percentage of inert gases obtained in 2n geologic formations. Natural gas is produced in significant amounts 0u| , sia,i'es- Texas is by far the largest producer, followed by Louisiana, mad kma' California, Kansas, and West Virginia. Manufactured gas is e by the distillation or cracking of oil or coal, by the steam carbon