US2581238A - Vaporizing vertical pot type oil burner - Google Patents

Description

Jan. 1, 1952 s. P. cAULEY vAPoRIzING VERTICAL POT TYPE OIL BURNER 2 SHEETS-SHEET l Filed Aug. 8, 1946 0 M 3. M M

m 8. fu e 4 rv. Z w 0. ru 8 ra. W M M w w 0 S. P. CAULEY VAPORIZING VERTICAL POT TYPE OIL BURNER Jan. 1, 1952 2 SHEETS- SHEET 2 Filed Aug. 8, 1946 00oopo o l 1 INVENTOR Patented Jan. 1, 1952 ICE,

vAPoluziNG VERTICAL on. BURNER Garden City, N. Y., asignor Stephen/P. Cauley,

POT TYPE to Souany-Vacuum Oil Company, Incorporated; a corporation of New York Application August 8, 1946, Serial No. 689,240

The present invention relates to vaporizing type liquid hydrocarbon fuel burners and, more particularly, to burners of this class which depend entirely upon the heat of combustion of the oil being burned for vaporizing the oil to be burned. These burners may be conveniently classified into the following general types:

l. Vertical pot type 2. Horizontal type a. Retort b. Pot 3. Sleeve type The present commercially available vaporizing type burners are of all-metal construction and have common operating characteristics in that they normally require virgin distillate fuels in order to give satisfatocry performance, satisfactory performance being judged by their ability to deliver rated heat output without the formation of objectionable amounts of soot or hard carbonaceous deposits.

AS previously mentioned, all of these commercially available burners have combustion characteristics which make it necessary to use distillate fuel oils that are essentially parafllnic in their composition. Attempts to use less parailinic oils, such as those derived from commerical cracking operations for the production of motor fuels, result in the production of excessive soot and hard carbonaceous deposits in the burner. These deposits interfere with the entrance of primary air required for vcombustion and the flow of oil into the burner.

The above mentioned critical nature of the vaporizing burner in regard to the type of fuel required presents a serious problem in connection with the conservation of natural petroleum resources. There are several millions of this type of burner in use within the United States of America and approximately 500,000 to 700,000 additional new units are normally manufactured each year. The problem of continuing the supply ofparamnic distillate oils for these burners/.iis recognized as being quite serious. Studies to determine the amounts of by-product distillate fuel oils from motor fuel cracking processes, that might be blended with parainic stocks for their use, have emphasized the critical nat 1re of this type of burner. An example of this is illustrated in the Figures 1 and 2. In these figures the relative paramnicity of the-fuels tested is shown by the property of carbon-hydrogen ratio. This property gives the weight ratio of the carbon and hydrogen contents of a fuel. The lowest carbon/hydrogen ratio represents the most paraffnic type fuel. Reduced parafllnicity is characterized by increasing C/H ratios. The test data were obtained using a conventional vertical vaporizing type burner under the same draft conditions.

Figure l shows that the rateat which oils may 4 Claims. (Cl. 158-91) be burned (indicating the relative amounts of heat released) at the maximum tolerable soot or smoke concentration is quite sensitive to the carbon-hydrogen ratios of fuels tested. The ICHAM smoke point referred to in the drawing is a measurement of the amount of light transmission that may be obtained, under specified conditions of test, through a glass rod that has been inserted in the flue gas passageway of the burner. A 6 per cent ICHAM smoke point indicates only a 6l per cent light transmission under the test .conditions and roughly corresponds to the concentration at which smoke becomes visible to the human eye.

Figure 2 shows the weights of hard carbonaceous deposits produced when burning the same volume of fuels having different carbon-hydrogen ratios under the same conditions of test. As in Figure l, it may be noted that the 'carbonaceous depositing tendencies of fuels, when used in this commercially available vaporizing type of burner. are also critical to carbon-hydrogen ratio.

It has been recognized by the manufacturers of this type of burner that the present commercially available designs must be modified to permit the use of catalytically cracked fuel. This is evident from a report of an address given at a recent meeting of the Cleveland Engineering Society and published in the February 6, 1946, issue of National Petroleum News (page 34).

During a discussion following presentation of the paper it was brought out that whatever course the future deisgn of pot type burners may take, no concern need be felt over the supply of thermal cracked fuel. But it was conceded that the day will come when cat crackers will crowd out the old thermal cracking plants, and a point will be reached where it will be necessary to switch over to the cat cracked product entirely, rather than attempt to sell two kinds of fuel oil.

For all of these reasons the oil burner designers were urged to develop equipment to use the cat" cracked fuel. The speaker hoped that some clue to the right solution might arise out of -a recent series of burning tests conducted by the American Society for Testing Materials.

While previous attempts to improve burners of this type to reduce or eliminate excessive deposition of carbon in the air inlets and elsewhere have been based upon the assumption that the presence of excessive deposits of carbon was' evidence of insufficient air for complete combustion or inadequate mixing of sufficient air with the oil lvapors, it has now been found that the unsatisfactory excessive deposits of carbon when burning fuels of reduced paraffinicity in this type of burner is not correlated as closely with the adequacy of the air supply as with other phenomena. It has been found that burners of the vaporizing type which when operating on fuels of reduced parafiinicity may be modified in structure in a manner which in no way ap-A pears to affect the amount of air supplied to the burner but does result in the reduction of the amount of carbon deposited from 'fuels of reduced parainieity to a remarkable extent. Thus, the problem of providing an adequate supply of fuel for this class of liquid hydrocarbon burner in the face of decreasing supplies of fuel of high paramnicity has been solved. The burners of modified structure operate on fuels of low parainicity under substantially the same draft usually with less smoke and at at least as high a capacity as that with which the unmodined burner operates on fuel of high parainicity.

It is an object of the present invention to provide a modified vaporizing type burner in which liquid hydrocarbon fuels of relatively low parafiinicity or relatively high carbon to hydrogen ratio can be burned under conditions which would produce excessive deposits of carbon were the fuel to be burned in a conventional burner of this class. It is another object of the present invention to provide movable elements which may be inserted in appropriate positions in the conventional structure of a manufactured burner to modify the structure thereof in accordance with the principles of the present invention to provide improved operating conditions resulting in the reduction of the amount of carbon deposited lwhen burning fuels of low paraninicity, i. e. of relatively high C/H ratios.

It is a further object of the present invention to provide a vaporizing type burner having a vaporizing chamber in which the liquid fuel is vaporized in whichthose portions of the vaporizing chamber which are in contact with the liquid fuel or vapors thereof before ignition are provided with non-metallic surfaces.

The'present invention also has as an object to provide a vaporizing type burner having a shield interposed between the source of radiant energy and the oil to be vaporized, said shield to be of such size and so constructed and arranged as to reduce the amount of heat absorbed by the fuel to be vaporized and the vapors produced that cracking of the oil is reduced to a substantial degree before ignition and burning of the oil occurs.

It is also within the scope of.' the objects of this invention to provide an improvement in the operation of burners of this class whereby liquid hydrocarbon fuels of relatively low parainicity can be burned without the production of excessive amounts ofv carbon and obstruction thereby of air inlets.

Other objects and `advantages will become apparent from 'the following description taken in conjunction with the drawings in which Figure lA is a graph showing the relation between the carbon-hydrogen ratio of fuels and the rate at which liquid hydrocarbon fuels may be burned at maximum tolerable soot or smoke concentration,

Figure 2 is a graph showing the relation between the weights oi' hard carbonaceous deposits produced and the carbon-hydrogen ratio of fuels when the same volume of each of several fuels is burned in the same burner under substantially the same test conditions,

Figure 3 is a vertical section through the lower portion of a conventional pot type vaporizing burner modied in accordance with the principles of the present invention,

Figure 4 is a more or less diagrammatic representation of a vertical cross-section through the lower portion of a conventional pot type vaporizing burner modified in accordance with the principles of the present invention, in which the non-catalytic coating of the inner surface of the bottom of the pot is built up around the fuel. inlet means to insure drainage of the fuel away from the fuel inlet,

Figure 5 is a more or less diagrammatic representation of a vertical cross-section through the lower portion of a conventional pot type vaporizing burner modified in accordance with the principles of the present invention wherein the upper surface of the baille or shield is provided with a coating of insulating material,

Figure 6 is a more or less diagrammatic representation of a vertical cross-section through the lower portion of a conventional pot type vapor- Laing-burner modified in accordance with the principles of the present invention in which the conventional low-flame ring has been replaced with a low-flame ring all parts of which are in the same plane,

Figure 7 -is a more or less diagrammatic representation of a vertical cross-section through the lower portion of a conventional pot type vaporizng burner modified in accordance with the principles of the present invention in which the fiat shield or balile of the modifications depicted in Figures 3 through 6 is replaced by a conical shield, and

Figures 8 and 9 are illustrative of further modifications of the conical shield illustrated in Figure 7.

4It has been found that substantial improvement in combustion characteristics of commercially available vaporizing types of burners, which results in their ability to satisfactorily burn fuels having increased carbon-hydrogen ratios, may be obtained through two factors. The first is that if distillate fuel oils are vaporized while in contact with a non-catalytic non-metallic, instead of a metallic catalytic, surface, less soot and hard carbonaceous deposits will be obtained during combustion. This is due to the elimination of the catalytic effect of metals upon the carbonization of hydrocarbons.

The second is elimination or control of direct radiant heat absorption from the burner flame by the oil at the point of vaporization. The effect of this is to reduce excessive heat absorption by the oil being vaporized which may cause excessive thermal decomposition or carbonization of the fuel during vaporization.

It is proposed that the metallic surface in contact with oil during vaporization in vaporizing types of burners be eliminated by covering or replacing this area with a suitable refractory type of material. An alternative is to provide the metallic surface with a non-metallic heat resistant non-catalytic coating, for example, by siliconizing the metal surface. This improvement applies to all of the vaporizing types of burners A discussed.

Other types of vaporizing burners may have materially improved combustion by elimination of direct radiant heat absorption by the oil during vaporization. l

It is proposed to control the amount of radiant heat absorption, by the oil while being vaporized, by a shield orbafile interposed between the source of radiant heat and the oil at the point of vaporization. The method of shielding used in each type of burner will vary because of their differences in construction but, in general, the shield should cover 60 per cent of the total surface area of the pool of oil to be burned.

In the vertical type of vaporizing oil burner the shield may be a circular disc or discs. It may have a fiat surface or may be concave or convex depending upon the type of oil which is to be used. If highly aromatic fuels are to be used, the shield should preferably be in t` shape of a cone without a bottom. This shape will allow for a longer period of interaction between the hydrocarbon vapors and oxygen prior to subjection of the mixture to absorption of direct radiant heat from the flame. An illustration of this shield shape is shown in Figure 7. For less aromatic types of fuels the cone apex angle may increase or may become inverted as shown in Figures 8 and9.

'Ihe height of the shield or its distance from the point of vaporization will also depend upon the construction of the burner in which it is used and the type of fuel being burned. Generally with aromatic fuels the shield should be placed at a greater distance from the point of vaporization than when using less aromatic fuels. This in effect provides a control over the amount of radiant heat absorption, by the oil. The edge of the shield preferably should be below the lowest primary air inlet holes in the vertical type of vaporizing burner. This allows the mixing of oil vapors and air prior to absorption of radiant heat and combustion.

In order that those skilled 1n the art may ap-` preciate the magnitude of the change in the capability of a burner of the class described, the data of two comparative tests on a relatively high carbon-hydrogen ratio fuel are tabulated hereinafter.

The fuel had the following characteristics:

Gravity, API 32.5 Distillation- I. B. P., F 376 10% 428 20% 441 30% 452 40% 460 50% 467 60% 477 70% 488 80% 501 90 520 E. P. "F 576 Recovery, percent 99.0 Residue, percent 1.0 Aniline point, F 122.4 Carbon residue on 10% bottoms, percent 0.11 Sulfur, percent 0.07 Carbon-hydrogen ratio (estimated) 6.48

A conventional vertical vaporizing type 10 inch burner rated at 50,000 B. t. u. per hour available heat output was used. The burner was operated at a draft of 0.08 inch of water to determine if the burner would deliver the rated heat output under ratingr conditions required by the Bureau of Fire Underwriters. The rating conditions of the Bureau are that the smoke rating at a draft of 0.08 inch water shall not be lower than 6 per cent as measured by the ICHAM glass rod procedure. It was found upon burning approximately 50 gallons of oil that the maximum heat output under these conditions was 45,600 B. t. u. per hour. Furthermore, it was found that it was necessary to reduce the oil input at intervals to retain the 6 per cent smoke limit. 'I'his is an indication that the excessive soot (carbon) formed 1was interfering with the entrance of primary air to the burner.

A comparative test was then run using the same burner after improving it in accordance with the principles of the present invention. That is to say. a steel disc, 0.125 inch thick, eight inches in diameter and having its surface sloping radially at an angle of about 5 percent from the horizontal was mounted on three supports equally spaced near the edge of the disc. The height of the supports was 2.5 inches. The height of the disc or baille was such that, when the supports rested on the bottom of the vaporizing chamber of the burner, the edge of the baiiie was below the lowest row of primary air inlet holes. The metal surface of the bottom of the vaporizing chamber was covered with a common refractory type of material such as reclay in such a manner that the oil would be in contact only with the refractory during vaporization.

After improvement of the burner in the above manner a test run was made using the same oil and the same draft as was used in testing the unmodified burner. However, it was possible to maintain an ICHAM smoke measurement of 87 to 100 per cent. In other words, with the improved burner there was almost perfect elimination of smoke as determined by this method. Furthermore, in a continuous burning test it was not necessary to reduce the fuel input rate during the entire test period as was necessary when operating the prior art burner on the same fuel under the same draft conditions.

Prior art Improved vaporlzing vaporizing type burner type burner Oil rate pounds per hour 3.11 3. 4 Total burning time (hours) 103. 109. 2 Grams of Carbon Deposit per pound of oil burned 0. 23 0. l5 Bottom Carbon 0. 18 Side Carbon 0.05 Draft, inch of water 0. 08 0. 08 Carbon Dioxide per cent of Flue 68s.... l2. l 13. 0 Per cent Excess Air 23.0 14.0 Flue Gas Temperature, F 830 845 Elciency, Per Cent 76 76 Smoke rate (ICHI "l) as per cent light transmitted 5+ 27 Heat output, B. t. u./hour 45. 600 50,000

Certain of the foregoing data should be emphasized. For example, in the modified burner only about 65 per cent as much carbon was deposited per pound of oil input as was deposited in the unmodified burner. In other words, the total amount of carbon deposited was about 35 per cent less than that deposited in the unmodied burner. The reduced carbon deposit was obtained with conditions under which the excess air was reduced 40 per cent and the smoke rating was improved by about 540 per cent. All of these improved results were obtained without the sacrifice of any efliciency or output of heat.

Other tests were conducted using other oils typical of whichis one having the following characteristics:

Gravity, A1 r 29.4 Distillation- I. B. P., F 423 10% 447 50% 479 528 E. P., "F 584 Carbon residue 10% bottoms, per cent 0.07

Carbon-hydrogen ratio 7.24

- ashpoint is delivered to the periphery This oil wals burned in the burner improved as described hereinbefore under the conditions and with the results tabulated hereinafter:

Oil rate pounds per hour 3.4

It will be noted that the foregoing data were obtained on a relatively heavy oil usually considered as unsuitable fuel for this class of burner. Nevertheless, the burner improved in accordance with the principles of this invention operated in a highly satisfactory manner.

'l'hel foregoing discussion of the highly satisfactory results obtained when burning fuels usually considered unsatisfactory for use in this class of burners leads to a description of the improved burner in conjunction with the drawings. As noted hereinbefore, the drawings of Figure 3 illustrates that type of the class of vaporizing liquid fuel burners which depend entirely upon the heat of combustion of the oil being burned to vaporize the oil to be burned which is known as the vertical pot type modified in accordancel with the principles of the present invention to provide a non-catalytic surface ,on those por tions of the pot the surfaces of which are in contact with unvaporized oil or unignited -oil vapors, a bailie or shield between the pool of un, burned oil and the source of radiant heat and to provide a fuel inlet means located at the ap;- proximate center of the bottom of the pot in place of an inlet at the periphery of the pot. The general construction of this type of the general class of vaporizing burners is too well known to require detailed description herein. It is considered sufficient to state that the commercially available vertical pot type burner comprises in general a cylindrical metal vessel with an oil inlet at the periphery of the bottom and a plurality of spaced apart air ports or inlets in the vertical portion of the poi?. These ports or inlets are usually present as rows of which the lowest is spaced a short distance above the bottom of the pot. An annular ange rigidly or removably mounted on the upper part of the wall oflthe pot serves as a iiame ring at which point the flue burns with a visible ame. This structure is illustrated in its fundamental elements in U. S. Patents Nos. 1,660,857 and 2,393,233.

The firebox or pot I is constructed of suitable sheet metal such as iron or steel and issurrounded by and enclosed within a drum l2" of similar material suitably ornamented. Drum 2 usually extends beyond the upper edge of pot I to provide heat exchange between the products of combustion and the air surrounding the heater. Liquid fuel such as kerosene or relatively light distillates having distillation end points below about 650 degrees Fahrenheit and of suitable of pot I through inlet 3. The fuel spreads upon the base l of pot I and forms a pool which covers an area of base I dependent upon the difference between the rate at which the fuel is burned and the rate at which the fuel is fed to pot I. Since the pot I is of generally'well known construction. enumeration of the parts need only be sufficiently detailed to permit appreciation of the modifications comprehended. by the principles of the present invention. Therefore, it will suffice to point out that the walls 5 of the pot usually are inclined from the vertical and provided with air inlets 6 through which the primary air is admitted to support the initial combustion of the fuel. In order to provide better operational conditions. a low flame ring or center baille 1 is provided. Above the uppermost row of primary air inlets a high amerin'g or top bale 8 is provided. In order to ensure better mixing of secondary air entering the pot through ports 9 a secondary air mixing baille III is located immediately above and contiguous to baille B. The chimney effect of the pot I draws air into the air space II through main base inlet I2. From air space Il the air is drawn into Athe interior of pot I through primary inlets 6 and secondary inlets 9. The conventional, unmodified vertical pot type burner, the essential parts of which have been enumerated in the foregoing, can be modified in accordance with the principles of the present invention by providing a bottom shield or baille Il supported by legs I5 or in any other suitable manner to place the baille or shield I4 between the first row of primary air inlets 5 and the unburned oil. In addition walls of pot I are provided with a non-metallic. non-catalytic coating I6, illustrated as being of a refractory material such as fire-clay or the like, although a siliconized surface is satisfactory.

When fuel such as that for which certain physical and chemical characteristics have been given hereinbefore is burned in a conventional, unmodified burner about 0.23 gram total carbon is deposited per pound of oil burned. About '78 per cent of the total carbon depositssettles on the bottom of the pot and about 22 per cent on the walls.

The eiect of heavy ends on the deposition of carbon in the unmodified burner can be determined by comparison of pertinent values for Y different oils. The fuels described in the following table were burned as indicated 'in a conventional, unmodified vertical pot type burner of the vaporlzing type, a modification in accordance with the principles of the present invention is illustrated in Figure 3.

Table I Fuel A B C D 449 423 376 435 5l7:bl1 F per cent l0 90 90 50 EP. .4-- 833 584 576 636 Aniline Pt., F 155.5 116.2 122.4 115.0 Corrected CJH Ratio. 6.62 7. 2i 6.94 7. 56 Diesel Index.- 52. 4 34.2 41. l 20.8 Mole Wt 225 180 200 Run No D-l D-S D19 F ue] Rate, iba/hr 2. 72 2.15 0.050 3.11 2,16 Stack Draft; Inches Water. 0. 044 0.031 0.055 0.080 0.063 Pot Draft, Inches Water 0.059 0.031 0. 055 0.097 0.078 Per cent CO1 in dry flue ga 12.0 9. 4 Por cent Excess Air 27 67 ICHAM, Per Cent Trans 5l 2l 5 5 34 Total Carbon Deposit, g./lb. oil 0.23 1.90 Bottom Carbon, gJlb. oil 0. 18 0. 45 Bottom Carbon, Per Cent Total. 78 23 Side Carbon, glib. oil 0.05 1.45 Side Carbon, Per Cent Total 22 77 the base 4 and the Those `skilled in the art will recognize that l fuel A is a fuel of relatively high -parafliniclty.v

Fahrenheitand that the carbon-hydrogen ratio is the lowest of the four fuels.

For the purposes of the comparative tests to be discussed hereinafter, the attention of those skilled in the art is directed to fuels C and D. It will be observed that at 517 i 11 degrees Fahrenheit, 90 per cent of fuel C has distilled whereas only 50 per cent of fuel D has distilled at that temperature range. It will also be noted the carbon-hydrogen ratio for fuel D is appreciably higher than that of fuel C.

Turning to the characteristics of these fuels, it will be noted (1) that although approximately eight times as much carbon was deposited by fuel D, the percentage rf light transmission in the ICHAM test was much higher; (2) that with fuel C most of the carbon was deposited on the bottom of pot I, whereas with fuel D most of the carbon was deposited on the sides.y This is an important characteristic since the carbon deposited on the side walls (side carbon) tends to obstruct the primaryl air inlets and increase the amount of carbon and smoke. Thus, Ait would appear that when a more aromatic fuel with heavier ends is burned in an unmodified conventional vertical pot type burner, the total carbon deposited per pound of oil burned is increased labout eight-fold and that most of'the carbon is deposited on the side walls of the pot i.

A further modification of' the conventional vertical pot type burner provides theA following changes of the structure illustrated in Figure 3. A sealing ring is superposed on the secondary air mixing baille i0. The sealing ring is in the form of an annulus and serves to confine the secondary air, to increase the velocity of' the secondary air and -to concentrate the secondary air at the base of the fiame formed at the inner periphery of top bafiie 8.

Illustrative of the effect of these modifications are the comparative data on fuel C provided in Table II.

Table Il Run Nom-.

Pot Draft, Inches Water..

Per Cent CO: dry flue gas 12.0 12. 8

Per Cent Excess Air 27 20 18 ICHAM, Per Cent Trans 32 6 Total Carbon, g.llb. oil 0. 23 f 0.15

1 Maximum. i Average.

Table III Run No D-Q D- 60 9o 676 584 122.4 116.2 8.94 7.24 Fuel Rate, iba/hr 13. 28 l 3. 34 l 3. 25 I 3. 50 Stack Draft, inches water- 0. 080 0.080 0. 080 0. (B0 Pot Draft, inches water; 0. 097 0.097 0.097 0. 097 Per Cent CO: dry flue gris 12.8 13.0 12.8 14. 1 Per, Cent Excess Air 27 18 22 ll ICHAM, Per Cent Trans. 32 6 72 6 Total Carbon, g./1b.oil. 0. l5 0. 33 Bottom Carbon, g./lb. oil 0. 14 Bottom Carbon/Total Carbon 42 side carbon, g./1b.oi 0.19 :III Sido Carbon/Total Carbomper cent.. 68

l Average. i Maximum.

Since with fuel C burned in an unmodified burner havin-g a center baille only 0.15 gram of total carbon was deposited per pound of oil burned, it would appear that elimination ofthe center baffle increases the total amountof carbon deposited probably due to poor burner characteristics of low fuel input. However, this comparison does provide a means for comparing the effect of a fuel such as fuel D having a heavy end. i

When fuel D is burned in a pot modified in the manner illustrated in Figure 4 the following comparable data are obtained:

Table 1V Run No ICHAM, Per Cent Trans Total Carbon, g./lb. oil... Bottom Carbon, g./lb. oil Bottom Carbon] Total Carbon per cent.. Side Carbon, g.llb. oil Side Carbon/Total Carbomper cent..

1 Average. i Maximum.

D-19 is compared in Table V:

Table V Run No D--19l D-ll Fuel D D Fuel Rate, lbs./hr 2.16 3.33 Stack Draft, inches Water. 0.063 0. 080 Pot Draft, inches Water 0. 078 0. 097 Per cent CO2 in dry flue gas 9. 4 13. 1 Per Cent Excess Air 67 20 ICHAM Per Cent Trans 34 25 Total Carbon Deposit, g./Ib. 1. 0.71 Bottom Carbon, g./Ib. oil 0. 45 0. l Bottoni Carbon/Total Carbon.. per cent.. 24 72 Side Carbon, g./1b. oil 1. 45 0.20 Side Carbon/Total Carbon per cent.. 76 28 l Unmodied.

Those skilled in the 'art will observe that not only has the total amount o1' carbon been reduced by about 63 per cent but, inaddltion, in the modified form of the burner three-quarters oi the carbon is deposited on the bottom whereas in the unmodiiied form three-quarters of the carbon is deposited on the side walls. It will also be noted that the improved conditions were obtained at a fuel rate 1.5 times that of the control (D-19).

Changing the bottom shield from a plane to a cone but making no other changes in the modification illustrated in Figure 4 produces the results indicated by the following comparable data.

Changing the uninsulated cone-shaped bottom shield of run D-12 to an insulated cone-shaped bottom shield produces the results indicated by the comparable data of Table VII.

Table V11 Run No D-l21 I D-i3 D D ICHAM Per Cent Trans ll 26 Total Carbon, g /lb oil..- 0. 45 0.88 Bottom Carbon, gJlb. oil 0. 2f.) 0. 20 Bottom CarbonlTotai Carbon. per cent 64 23 Side Carbon, g./lb. oil 0.16 0. 68 Side Carbon/Total Carbon per cent 36 77 lCone. 2 Insulated cone.

It is manifest that while the total amount of carbon deposited has increased about 100 per cent, the distribution of the deposit has been changed radically. Thus, the bottom carbon of D-l3 (insulated hollow cone) represents 23 per cent of the total carbon in contrast to 64 per cent in D-12 (non-insulated hollow cone) and the side carbon represents a proportional increase.

Changing the bottom shield from an insulated hollow cone-shaped structure to an insulated plane producesv a reduction in total carbon of about 75 per cent but the carbon distribution is substantially the same, as the data in Table VIII show.

Table VIII Bun No i D-13 i Fuel ICHAM, Per Cent Trans Total Carbon, g./lb. oil Bottom Carbon, glib. oil Bottom Carbon/Total `Carbon Side Coi-bon, gJlb. oil Side Carbon/Total Carbon per cent..

l2 and the distribution of the deposit changed to an appreciable degree as the data. in TableIX illustrate.

Table IX Run No D-H l D-ll i Fuel D D ICHAM, Per Cent Trans i7 98 Total Carbon, g.llb. oil 0.25 0.95 Bottom Carbon, glib. oil. 0.05 0. 43 Bottom Carbon/Total Carbo per cent.. 20 45 Side Carbon, g./lb. oil 0. 20 0. 52 Side Carbon/Total Carbon .per cent. 80 55 1 Insulated plane; no center bame. 2 Insulated plane; center baule.

' proved operational characteristics from all viewpoints the embodiment illustrated by Figure 6 is preferred.

In all of the Figures 3 to 'I the same or similar parts are designated by the same numeral. Thus, for example, the fire pot is designated as I, the base thereof as 4, the walls as 5 and the oil inlet as 3. The primary air inlets are designated as 6, the center baille as 1, the secondary air mixing baille as 8 and the secondary air inlets as 9. The top shield is numbered Il and the sealing ring as I3. Each bottom shield comprises the shield I4 and the supports or legs I5. The non-metallic, non-catalytic coating is designated i6 as is the similar coating of the shield when so coated.

While the present invention has been illustrated in terms oi` new construction. the provision of bottom shields and re pot linings per se are also contemplated, Thus, while new burners may be constructed along the lines illustrated hereinbefore, the present invention also includes the construction of refractory linings and bottom shields for insertion in presently existing and operating burners either to improve the prior art burners or as replacement parts.

Figures 8 and 9 are illustrative of variations of the type of bottom shield. The major difference between each of these and the others and that illustrated in Figures 4 to 7, both inclusive. is the width of the apex angle of the shield. 0f course, it will be observed that in Figure 9 the cone is inverted. It also is to be noted that the shields may be insulated or provided with a noncatalytic surface on the under-side.

I claim:

1. In a vaporizing type oil burner of the vertical pot type wherein vaporization of the oil to be burned is dependent substantially wholly upon heat derived from the combustion of oil being burned comprising a burner pot having a plurality of air inlet apertures located at various levels in the wall thereof, a low flame ring positioned above the lowermost of said air inlet apertures, a high ilame ring positioned below the uppermost of said air inlet iapertures, a notchedvbaiiie ring positioned above the uppermost of said air inlet apertures, and means for supplying a liquid fuel to the lower portion of the pot, the improvement which comprises n.

sealing ring positioned immediately above said notched baille ring, a non-catalytic, refractory coating on the surfaces of said pot with which unvaporized oil is in contact, liquid fuel inlet means positioned substantially at the center of the bottom of said pot, a horizontally disposed shield having its center in the projected vertical axis of said fuel inlet means, and means for supporting said shield in spaced relation with the bottom of said pot and below the lowermost of said air inlet apertures.

2. In a vaporizing type oil burner of the vertical pot type wherein vaporization of the oil to be burned is dependent substantially wholly upon heat derived from the combustion of oil being burned comprising a burner pot having a plurality of air inlet apertures located at various levels in the wall thereof, and means for supplying a liquid fuel to the lower portion of the pot, the improvement which comprises the combination of a non-catalytic, refractory coating on the surfaces of said pot with which unvaporized oil is in contact, liquid fuel inlet means positioned substantially at the center of the bottom of said pot, a horizontally disposed shield having its center in the projected vertical axis of said fuel inlet means, and means for supporting said shield in spaced relation with the bottom of said pot and below the lowermost of said air inlet apertures.

3. In a vaporizing type oil burner of the vertical potv type wherein vaporization of the oil to be burned is dependent substantially wholly upon heat derived from the combustion of oil being burned comprising a burner pot having a plurality of air inlet apertures located at various levels in the wall thereof, and means for supplying a liquid fuel to the lower portion of the pot, the improvement which comprises the combination of a non-catalytic, refractory coating on the surfaces of said pot with which unvaporized oil is in contact, liquid fuel inlet means positioned substantially at the center of the bottom of said pot, a horizontally disposed shield having its center in the projected vertical axis of said fuel inlet means, said shield comprising a disk of refractory material, and means for supporting said shield in spaced relation with the bottom of said pot and below the lowermost of said air inlet apertures.

4. In a, vaporizing type oil burner of the vertical pot type wherein vaporization of the oil to be burned is dependent substantially wholly upon heat derived from the combustion of oil being burned comprising a burner pot having a plurality of air inlet apertures located at various levels in the wall thereof, and means for supplying a liquid fuel to the lower portion of the pot, the improvement which comprises the combination of a non-catalytic, refractory coating on the surfaces of said pot with which unvaporized oil is in contact, liquid fuel inlet means positioned substantially at the center of the bottom of said pot, a conical shield having its center in the projected vertical axis of said fuelinlet means. and means for supporting said shield in spaced relation with the bottom of said ot and with the base of said cone below the lowermost of said air inlet apertures.

STEPHEN P. CAULEY.

REFERENCES CITED The following references are of record in the le of this patent:

UNITED STATES PATENTS Number Name Date 623,012 Grimm Apr. 11, 1899 892,706 Blubaugh July 7, 1908 1,633,549 Little June 21, 1927 1,840,137 Sturgis Jan. 5, 1932 1,848,206 ySherman Mar. 8, 1932 1,927,434 Cole et al Sept. 19, 1933 1,950,161 Bock Mar. 6, 1934 2,065,265 Bock Dec. 22, 1936 2,218,154 Ramsey Oct. 15, 1940 2,311,469 Pruitt Feb. 16, 1943 2,326,221 Hill Aug. 10, 1943 2,361,912 Breese Nov. 7, 1944 2,363,192 Miller Nov, 21, 1944 2,375,347 Castle et al. May 8, 1945 FOREIGN PATENTS Number Country Date 816,124 France Apr. 26, 1937

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