US2448235A - Method and apparatus for removing lead containing ingredients from hydrocarbon fuels - Google Patents
Method and apparatus for removing lead containing ingredients from hydrocarbon fuels Download PDFInfo
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- US2448235A US2448235A US537827A US53782744A US2448235A US 2448235 A US2448235 A US 2448235A US 537827 A US537827 A US 537827A US 53782744 A US53782744 A US 53782744A US 2448235 A US2448235 A US 2448235A
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- 239000000446 fuel Substances 0.000 title description 35
- 229930195733 hydrocarbon Natural products 0.000 title description 12
- 150000002430 hydrocarbons Chemical class 0.000 title description 12
- 238000000034 method Methods 0.000 title description 12
- 239000004215 Carbon black (E152) Substances 0.000 title description 10
- 239000004615 ingredient Substances 0.000 title description 6
- MRMOZBOQVYRSEM-UHFFFAOYSA-N tetraethyllead Chemical compound CC[Pb](CC)(CC)CC MRMOZBOQVYRSEM-UHFFFAOYSA-N 0.000 description 44
- 239000002245 particle Substances 0.000 description 26
- 239000003502 gasoline Substances 0.000 description 17
- 229910000831 Steel Inorganic materials 0.000 description 16
- 239000000945 filler Substances 0.000 description 16
- 239000010959 steel Substances 0.000 description 16
- 239000002184 metal Substances 0.000 description 14
- 229910052751 metal Inorganic materials 0.000 description 14
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 12
- 210000002268 wool Anatomy 0.000 description 12
- 230000008016 vaporization Effects 0.000 description 11
- 239000000470 constituent Substances 0.000 description 6
- 238000000354 decomposition reaction Methods 0.000 description 6
- 239000000835 fiber Substances 0.000 description 6
- 239000007789 gas Substances 0.000 description 6
- 229910052742 iron Inorganic materials 0.000 description 6
- 229910000464 lead oxide Inorganic materials 0.000 description 5
- 210000002445 nipple Anatomy 0.000 description 5
- YEXPOXQUZXUXJW-UHFFFAOYSA-N oxolead Chemical compound [Pb]=O YEXPOXQUZXUXJW-UHFFFAOYSA-N 0.000 description 5
- 238000009834 vaporization Methods 0.000 description 5
- 241000288673 Chiroptera Species 0.000 description 4
- 238000005336 cracking Methods 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 229910045601 alloy Inorganic materials 0.000 description 3
- 239000000956 alloy Substances 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 229920000914 Metallic fiber Polymers 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 239000002923 metal particle Substances 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 231100000331 toxic Toxicity 0.000 description 2
- 230000002588 toxic effect Effects 0.000 description 2
- 238000003466 welding Methods 0.000 description 2
- 229910000952 Be alloy Inorganic materials 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229910000640 Fe alloy Inorganic materials 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 230000035508 accumulation Effects 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 239000002657 fibrous material Substances 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 239000002828 fuel tank Substances 0.000 description 1
- 238000005286 illumination Methods 0.000 description 1
- -1 leaded gasoline Chemical compound 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 230000010349 pulsation Effects 0.000 description 1
- 230000000306 recurrent effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G29/00—Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
- C10G29/02—Non-metals
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G29/00—Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
- C10G29/04—Metals, or metals deposited on a carrier
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G31/00—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for
Definitions
- This invention relates to the generating and conditioning of hydrocarbon fuels containing tetra-ethyl lead, such as leaded gasoline, to enable such fuels to be burned successfully in pressure type systems for heating, cooking and illumination.
- a further object is the provision of a simple and highly efficient apparatus for substantially eliminating the objectionable and dangerous constituents of leaded gasoline to enable such fuel to be burned successfully and safely in pressure systems.
- Figure 2 is an end view of the same;
- Figure 3 is a cross section taken on theline 3-3 of Figure 1;
- Figure 4 is a side elevational view illustrating a bat of matted metal filaments, such as steel wool before the same is compressed or condensed;
- Figure 5 is a longitudinal elevation of a somewhat different form of my apparatus.
- the tetra-ethyl lead contained in leaded gasoline or other analogous hydrocarbon fuels is held.
- My method is preferably carried out within the generator or vaporizing tube itself as the leaded,
- hydrocarbon fuel is heated at relatively high temperatures for producing a combustible vapor and gas. It can be carried out, although not as successfully, at points in the pressure burner system immediately after vaporization of the fuel and where the temperature of the mixture is such that the tetra-ethyl lead is still in cracked or decomposed state.
- a relatively large generator tube II which has circumferential rabbeted ends Ila wherein are secured as by- Welding closure discs [2 and I3 respectively, closure disc I2 at the fuel entrance of the generator tube being tapped to receive a straightfitting or plug I4 having an axial passage Ila in the inner end thereof which communicates with a lateral port Pic of a nipple l5 which is connectable with the tank or other source offuel supp
- a short tubular fitting l6 is screwend of the generator tube It,
- the tube H is filled with the exception of its ends with adens'ely compressed or related mass of metal fragments or particles preferably steel wool, the mass of steel wool as utilized being greatly compressed to provide a dense homogenous filler having a minute porosity sufficient, however, to permit passage of vapors and gases. pressed in such manner that its density adjacent the discharge end of the vaporizing tube is materially greater than it, is at the entrance end.
- the cylindrical filler is disposed between two reticulated or relatively rigid concavoconvex screen partitions l1 disposed, at the respective, ends of the, tube.
- the reticulated members may be shell members provided with a multiplicity of very closely spaced small perforations or may be in the form of rigid metal netting of small mesh.
- metal fibers matted together and densely compressed or other forms of metal particles such as compressed metal granules preferably iron or steel having a dense porosity, may be utilized. It is essential that the character of the metal. be such that it will have a relatively high melting point above the temperatures utilized in vaporizing the leaded fuel.
- land 28 may be readily and accurately obtained by successivel inserting uncompressed bats of the proper diameter to fit the fuel entrance end of tube H with disc 12 removed and the disc I3 applied and compressing the first bat of steel wool or fibrous metal.
- which will supply the fuel, such as gasoline containing tetra-ethyl lead, from a source of' supply such as a fuel tank under air
- the filler is very preferably com-- pressure to. the plug M, a coupling 32 being employed for connecting the delivery end of the fuel supply pipe to the plug Id.
- the branch discharge nipple is has quite a small passage therethrougl1 and; it leads into a U-shaped mixing. chamber 33, this chamber having an air opening 33a beyond'the point where nipple Hia delivers into the same.
- the mixing chamber 33 connects with; a manifold 34, which has connected thereto a burner 35 underlying the generator tube H and adapted to deliver heat thereto when in operation.
- leaded hydrocarbon fuel such as gasoline containing tetra-ethylleadis.introduced under pressure through the fuel supply pipe 3
- the generator tube is heated by the burner 35'.
- the gasoline is generated into gas in the generator tube, the generator tube delivering throughthe nipple ifia, into the mixing chamber 33 where the gas mixes with air admitted'through the opening 33a and the mixed air and gas then pass through the manifold 34 to, deliver from the burner 35 where it is burned.
- the heat delivered from the burner 35 intensely heats the generator tube I! together with the steel wool. plugs I8, i9, and Zll to maintain the metal particles or fibers at high temperatures.
- the tube is of such diameter and length that actual passage of the fuel therethrough is slow, the globules of the tetra-ethyl lead passing through the less compressed and less dense pads i8 until cracking or decomposition of the tetraethyl lead takes place in the vaporizing or the gasoline.
- decomposition or cracking of the tetra-ethyl lead commences, liberation of atoms or fine particles of the element lead, is thought to be produced within the tube with some small formation of lead oxide in minute particles be- :cause of the small amounts of air admixed with the leaded gasoline.
- the plugs 28- and I9 are successively denser thereby producing greater impingement ofthe remaining molten particles offree- .lead and serving its substantially eliminate all.
- filler plugs l8, l9 and 20 have been made by opening up a number of my generator tubes after many hours of actual operation of the burner system and have revealed what apears to be alloy coatings upon the particles or fibers of the steel wool.
- particles is used, it is used in its broad sense to indicate elements of very small cross sectional area whether in the shape of filaments, fibers or minute granules.
- FIG. 5 a satisfactory form of apparatus is illustrated wherein the medium for separating off the residue particles from decomposed tetraethyl lead is isolated from the generator tube but closely associated therewith.
- the generator tube 25 is of conventional structure and may or may not have a filling therein to prevent pulsations or choking and has its discharge end connected by a short tube 28 with the intake 21 of a residue removing retort or tube 28.
- Tube 28 is preferably of considerably greater diameter than the vaporizing tube 25 and in general is constructed similarly to the tube H of the form first described, having a discharge tube 29 at one end thereof and being substantially filled throughout its cross sectional area with preferably densely compressed plugs or a plug of metallic fibrous material preferably steel wool or some other fibrous iron containing metal.
- the heavy screens 30 are of similar construction to the retaining screens l1 shown in the form first described, but are related somewhat different as shown both having the concave portions disposed inwardly relatively to the respective ends of the tube.
- the filler F of steel wool or the like is as in the form of the invention first described preferably constructed and compressed in such manner that the plug or portion of the filler at the discharge end of the tube is of greater compressed density than the portion of the filler at the intake end.
- the vaporized fuel with free particles of lead and particles of lead oxide mixed therewith at high temperature pass into the intake end of tube 28 and then are affected by the filler F in the same manner as in the preferred form previously described.
- the volatile material passes through the filler F whereas the lead atoms orparticles and other residue particles impinge against the many matted fibers or particles of steel wool and react therewith and are separated off as described with reference to the form first described. It is, of course, essential that the temperature within the filler F be adequate to retain the fuel in vaporized state, and for thispurpose there is shown a burner 36 underlying both tubes 25 and 28 and playing thereon.
- Apparatus for substantially removing the lead containing ingredients of hydrocarbon fuels containing tetra-ethyl lead comprising a retort adapted to be subjected to high temperatures, said retort having a fuel entrance and a fuel discharge, a filler occupying at least a portion of the interior of said retort between said entrance and said discharge, said filler being composed of a mass of densely related iron containing particles, said particles adjacent the discharge portion of said retort being more densely related than said particles adjacent the fuel intake portion of said retort.
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- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Feeding And Controlling Fuel (AREA)
Description
S- 'RASMUSSEN INGREDIENTS FROM HYDROCARBON FUELS Filed May 29, 1944 INVENTOR. I WV ymm ATTORNEYS METHOD AND APPARATUS FOR REMOVING LEAD CONTAINING ELIIII-II Aug. 31
Patented Aug. 31, 1948 anazzs METHOD AND APPARATUS FOR REMOVIN LEAD CONTAINING INGREDIENTS FROM HYDROCARBON FUELS Sophus Rasmussen, Albert Lea, Minn., 'assignor to American Gas Machine Company, Albert Lea, Minn., a corporation of Minnesota Application May 29, 1944, Serial No. 537,827
:UNITED STATES PATENT OFFICE 2 Claims.
This invention relates to the generating and conditioning of hydrocarbon fuels containing tetra-ethyl lead, such as leaded gasoline, to enable such fuels to be burned successfully in pressure type systems for heating, cooking and illumination.
Heretofore, to applicants knowledge, it has been impractical and commercially impossible to successfully utilizegasoline containing tetraethyl lead in gasoline burner systems of the pressure type. Such systems employ generators whereinthe fuel is introduced, vaporized and passedon by pressure and they also contain small orifices, Valves and other restricted passages which, become easily clogged with accumulations of any deposits or sludge. In the vaporization of the leaded gasoline in the generator tube or other retort, the temperatures are such that a cracking or decomposition of the tetra-ethyl lead occurs resulting in production of atoms .or extremely minute particlesof the element lead as well as some small amount of lead. oxide due to some presence of airin the generator. These atoms and particles, I have discovered, will deposit upon surfaces in small and restricted passages of the system or apparatus, clogging parts of the device ahead of the actual burner jets. The actual burning of the vaporized leaded fuel, of course, produces particles of lead oxide in the burner structure itself where air is admixed with the vaporized fuel, further clogging passages and ports and making such systems inoperative after leaded gasoline has been utilized for a relatively very short period of time.
Furthermore, the production of-minute particles of lead oxide through the burning of gasoline vapor-containing tetra-ethyl lead or constituents thereof is dangerous to human and animal life, such particles being toxic when breathed or swallowed. Various attempts have been made to solve the problems enumerated herein, both for the purpose of enabling pressureburner systems to 'be utilized to successfully burn leaded gasoline and for the further purpose of removing the grave danger to human life.
It is an object of my invention to provide a comparatively simple, but highly successful method whereby the toxic and solid or clogging constituents of tetra-ethyl lead and its oxides formed in vaporizing and burning of the fuel are substantially eliminated from the burner system as the fuel is being vaporized in the generator and prior to entrance of the vapors into the burner proper and, of course, prior to actual burning.
' A further object is the provision of a simple and highly efficient apparatus for substantially eliminating the objectionable and dangerous constituents of leaded gasoline to enable such fuel to be burned successfully and safely in pressure systems.
These and other objects and advantages-of my (01. nae-11' 2 invention will more fully appear from the following description made in connection with the accompanying drawings, wherein like reference characters refer to the same parts throughout the views, and in which Figure 1 is a longitudinal, sectional view of a generator detached from a gasoline burner system constructed to carry out my improved method and embodying the principles of my improved apparatus;
Figure 2 is an end view of the same; Figure 3 is a cross section taken on theline 3-3 of Figure 1;
Figure 4 is a side elevational view illustrating a bat of matted metal filaments, such as steel wool before the same is compressed or condensed; and
Figure 5 is a longitudinal elevation of a somewhat different form of my apparatus. v
The tetra-ethyl lead contained in leaded gasoline or other analogous hydrocarbon fuels is held.
in suspension in the form of very minute globules and remains in such form until it is heated to such temperature either by vaporization ,of the fuel at high temperature or in the subsequent burning, to crack or otherwise decompose the tetra-ethyl lead thereupon liberating free lead atoms or minute particles which in the presence of air readily form particles of lead oxide.
After exhaustive testing of various chemicals,
filters and methods for eliminating the constituents of tetra-ethyl lead both upon burning and prior to burning of the vaporized fuel, I have discovered a method and apparatuswhich by actual long recurrent tests have demonstrated an efliciency for removing as high as of all lead constituents of the prepared leaded gasoline.
My method is preferably carried out within the generator or vaporizing tube itself as the leaded,
hydrocarbon fuel is heated at relatively high temperatures for producing a combustible vapor and gas. It can be carried out, although not as successfully, at points in the pressure burner system immediately after vaporization of the fuel and where the temperature of the mixture is such that the tetra-ethyl lead is still in cracked or decomposed state.
In the form of the apparatus illustrated in the drawings Figs. 1 and 3, there is shown a relatively large generator tube II which has circumferential rabbeted ends Ila wherein are secured as by- Welding closure discs [2 and I3 respectively, closure disc I2 at the fuel entrance of the generator tube being tapped to receive a straightfitting or plug I4 having an axial passage Ila in the inner end thereof which communicates with a lateral port Pic of a nipple l5 which is connectable with the tank or other source offuel supp At the discharge as shown, a short tubular fitting l6 is screwend of the generator tube It,
ed therewith and communicating with the axial,
port in tube IS. The tube H is filled with the exception of its ends with adens'ely compressed or related mass of metal fragments or particles preferably steel wool, the mass of steel wool as utilized being greatly compressed to provide a dense homogenous filler having a minute porosity sufficient, however, to permit passage of vapors and gases. pressed in such manner that its density adjacent the discharge end of the vaporizing tube is materially greater than it, is at the entrance end.
As shown, the cylindrical filler is disposed between two reticulated or relatively rigid concavoconvex screen partitions l1 disposed, at the respective, ends of the, tube. The reticulated members may be shell members provided with a multiplicity of very closely spaced small perforations or may be in the form of rigid metal netting of small mesh.
It will be understoodthat while I prefer densely compressed, steel wool for the filler of my tube,
that other metal fibers matted together and densely compressed or other forms of metal particles, such as compressed metal granules preferably iron or steel having a dense porosity, may be utilized. It is essential that the character of the metal. be such that it will have a relatively high melting point above the temperatures utilized in vaporizing the leaded fuel.
, I prefer'to construct the filler of my generating tube from a plurality of abutting plugs of compressed metallic fibers or particles. As shown eight, of said plugs disposed end to end in tube H are utilized but, of course the number thereof and lengths of the same may be considerably varied. It is important, however, that the density of' the right hand plug as be less than the extreme left hand plug iii and I prefer to utilize a number of plugs E8 of similar compression and density and then utilize one or more intermediate plugs 20 of greater densit than the plugs 18 but of less density than the plug is immediately adjacent the discharge of the tube.
In utilizing the preferred fibrous metal of relatively high melting point, such as steel wool, a proper density of the various plug members it, land 28 may be readily and accurately obtained by successivel inserting uncompressed bats of the proper diameter to fit the fuel entrance end of tube H with disc 12 removed and the disc I3 applied and compressing the first bat of steel wool or fibrous metal. to the desired determined position by a piston inserted through the open end of the tube and then applying a second bat of steel wool or fibrous metal and compressing this bat upon the compressed plug i9 by the same piston action, the inward movement of the piston indicating through predetermined means the compression and density desired and thereafter successively introducing uncompressed bats of fibrous metal and compressing by piston action to the extent gauged to obtain the plugs i8, thereafter the grating or reticulated discs I! with its supporting clip may be inserted and the tube closed at the fuel entrance end by welding or otherwise, securing the disc I2 in the rabbeted end of the tube.
Referring now to Fig. 2, there is there shown a, supply pipe 3|, which will supply the fuel, such as gasoline containing tetra-ethyl lead, from a source of' supply such as a fuel tank under air The filler is very preferably com-- pressure to. the plug M, a coupling 32 being employed for connecting the delivery end of the fuel supply pipe to the plug Id. The branch discharge nipple is has quite a small passage therethrougl1 and; it leads into a U-shaped mixing. chamber 33, this chamber having an air opening 33a beyond'the point where nipple Hia delivers into the same. The mixing chamber 33 connects with; a manifold 34, which has connected thereto a burner 35 underlying the generator tube H and adapted to deliver heat thereto when in operation.
In carrying out my method and in the operation of the apparatus illustrated, when the apparatus is infull operation, leaded hydrocarbon fuel, such as gasoline containing tetra-ethylleadis.introduced under pressure through the fuel supply pipe 3| and nipple l4 into the generator tube H.
The generator tube is heated by the burner 35'.
and. the gasoline is generated into gas in the generator tube, the generator tube delivering throughthe nipple ifia, into the mixing chamber 33 where the gas mixes with air admitted'through the opening 33a and the mixed air and gas then pass through the manifold 34 to, deliver from the burner 35 where it is burned. The heat delivered from the burner 35 intensely heats the generator tube I! together with the steel wool. plugs I8, i9, and Zll to maintain the metal particles or fibers at high temperatures.
The tube is of such diameter and length that actual passage of the fuel therethrough is slow, the globules of the tetra-ethyl lead passing through the less compressed and less dense pads i8 until cracking or decomposition of the tetraethyl lead takes place in the vaporizing or the gasoline. As decomposition or cracking of the tetra-ethyl lead commences, liberation of atoms or fine particles of the element lead, is thought to be produced within the tube with some small formation of lead oxide in minute particles be- :cause of the small amounts of air admixed with the leaded gasoline. These particles impinge against and some are restricted by the fine :porosity of the plugs H but it is believed that thelead atoms or minute particles in molten state, unite with the particles of iron at high temperature usually incandescent to form minute quantitiesof lead-iron alloy. Certain metals have an affinity or ability to form alloys and; this is true of metals, lead" and iron. In any event, in the vaporization of the fuel and in the material decomposition of the tetra-ethyl lead as the mixture passes through the very finely porous plugs [8, the lead constituents of the tetra-ethyl lead are removed and this I am convinced is through. action in addition to mechanical filtering. In the more volatile state and with greater decomposition of the tetra-ethyl lead near the discharge end of tube H, the plugs 28- and I9 are successively denser thereby producing greater impingement ofthe remaining molten particles offree- .lead and serving its substantially eliminate all.
with the proper use of my method and apparatus.
Examination of filler plugs l8, l9 and 20 have been made by opening up a number of my generator tubes after many hours of actual operation of the burner system and have revealed what apears to be alloy coatings upon the particles or fibers of the steel wool.
It will, of course, be understood that the filler bats have to be occasionally renewed, or what is usually simpler, a new generator tube with my improvements therein, installed for replacement. In the apparatus herein described, with the tube and bats of suitable size for'the requirements, several hundred hours of operating use may be obtained where leaded gasoline is burned before replacement is needed. This means that in most commercial devices the system may be operative from six months to over a year without replacement of the filler plugs or generator tube.
I realize that in the high temperature heating action of the leaded gasoline within the generator tube and in the heating of the metallic fibers or particles preferably of steel composition many complicated physical and chemical reactions occur. I cannot positively state what causes the unexpected elimination of substantially all of the lead ingredients during vaporization or immediately thereafter, but I believe there are several factors which may include reactions occurring through carbon in the steel particles; formation of small amounts of alloy with the lead and heated steel, or iron; some other attraction or affinity between the extremely minute lead atoms or particles and certainly decomposition or cracking in the generating tube of the tetraethyl lead globules. In any event, I am positive of the successful results produced by carrying out my method as disclosed herein and by the use of the simple apparatus described.
Where in the appended claims the term "particles is used, it is used in its broad sense to indicate elements of very small cross sectional area whether in the shape of filaments, fibers or minute granules.
Where in the appended claims the term separated 01f is used, it is used in its broad sense to include within its meaning any action whether through attraction, surface tension, alloy ailinity, or pure physical filtering to retain the lead ingredient.
In Figure 5 a satisfactory form of apparatus is illustrated wherein the medium for separating off the residue particles from decomposed tetraethyl lead is isolated from the generator tube but closely associated therewith. In this form of my invention the generator tube 25 is of conventional structure and may or may not have a filling therein to prevent pulsations or choking and has its discharge end connected by a short tube 28 with the intake 21 of a residue removing retort or tube 28. Tube 28 is preferably of considerably greater diameter than the vaporizing tube 25 and in general is constructed similarly to the tube H of the form first described, having a discharge tube 29 at one end thereof and being substantially filled throughout its cross sectional area with preferably densely compressed plugs or a plug of metallic fibrous material preferably steel wool or some other fibrous iron containing metal. In the tube 28 the heavy screens 30 are of similar construction to the retaining screens l1 shown in the form first described, but are related somewhat different as shown both having the concave portions disposed inwardly relatively to the respective ends of the tube. The filler F of steel wool or the like is as in the form of the invention first described preferably constructed and compressed in such manner that the plug or portion of the filler at the discharge end of the tube is of greater compressed density than the portion of the filler at the intake end.
In operation the vaporized fuel with free particles of lead and particles of lead oxide mixed therewith at high temperature pass into the intake end of tube 28 and then are affected by the filler F in the same manner as in the preferred form previously described. The volatile material passes through the filler F whereas the lead atoms orparticles and other residue particles impinge against the many matted fibers or particles of steel wool and react therewith and are separated off as described with reference to the form first described. It is, of course, essential that the temperature within the filler F be adequate to retain the fuel in vaporized state, and for thispurpose there is shown a burner 36 underlying both tubes 25 and 28 and playing thereon.
What I claim is:
1. Apparatus for substantially removing the lead containing ingredients of hydrocarbon fuels containing tetra-ethyl lead, comprising a retort adapted to be subjected to high temperatures, said retort having a fuel entrance and a fuel discharge, a filler occupying at least a portion of the interior of said retort between said entrance and said discharge, said filler being composed of a mass of densely related iron containing particles, said particles adjacent the discharge portion of said retort being more densely related than said particles adjacent the fuel intake portion of said retort.
2. The method of generating hydrocarbon fuels containing tetra-ethyl lead to successfully burn the same in burners of the pressure type, which consists in heating the fuel to vaporize the hydrocarbons and decompose the tetra-ethyl lead and passing the fuel in such condition through a mass of successively more densely compressed and matted metal fibers, which, while permitting passage of the vaporized hydrocarbon elements for burning, will act to catch, retain, and substantially remove from the vaporized hydrocarbons the decomposed elements of the tetra-ethyl lead.
SOPHUS RASMUSSEN.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Number Name Date 646,558 Rey et a1. Apr. 3, 1900 666,785 Williams Jan. 29, 1901 944,456 Miess Dec. 28, 1909 1,594,296 Lee Nov. 9, 1921 1,604,235 Odom Oct. 26, 1926 1,676,724 Pecker July 10, 1928 1,962,153 Peterkin June 12, 1934 2,368,261 Neef Jan. 30, 1945 2,397,142 Howard Mar. 26, 1946 FOREIGN PATENTS Number Country Date 312,200 Great Britain May 21, 1929 728,741 France Apr. 18, 1932 OTHER REFERENCES Toms et al., The Separation of Lead Tetra- Ethyl-Petro1eum Spirit, Analyst 53 (1928), pages 328 to 329.
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US537827A US2448235A (en) | 1944-05-29 | 1944-05-29 | Method and apparatus for removing lead containing ingredients from hydrocarbon fuels |
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US537827A US2448235A (en) | 1944-05-29 | 1944-05-29 | Method and apparatus for removing lead containing ingredients from hydrocarbon fuels |
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Publication Number | Publication Date |
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US2448235A true US2448235A (en) | 1948-08-31 |
Family
ID=24144270
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US537827A Expired - Lifetime US2448235A (en) | 1944-05-29 | 1944-05-29 | Method and apparatus for removing lead containing ingredients from hydrocarbon fuels |
Country Status (1)
Country | Link |
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US (1) | US2448235A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2812017A (en) * | 1953-02-24 | 1957-11-05 | Isadore N Vant | Automatic burner |
US2969320A (en) * | 1959-02-03 | 1961-01-24 | Socony Mobil Oil Co Inc | Removal of tetraethyl lead from hydrocarbon liquids with sulfur dioxide |
US3923643A (en) * | 1974-06-14 | 1975-12-02 | Shell Oil Co | Removal of lead and other suspended solids from used hydrocarbon lubricating oil |
Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US646558A (en) * | 1899-11-01 | 1900-04-03 | Jean Alexandre Rey | Furnace for burning hydrocarbons, &c. |
US666785A (en) * | 1899-06-05 | 1901-01-29 | John F Williams | Generator for hydrocarbon-burners. |
US944456A (en) * | 1907-05-28 | 1909-12-28 | Empire Light Ltd | Vapor-burning apparatus. |
US1594296A (en) * | 1921-11-09 | 1926-07-27 | Louis E Lee | Apparatus for distilling oils |
US1604235A (en) * | 1924-06-13 | 1926-10-26 | M O R Products Company | Process for removing sulphur compounds from petroleum oils |
US1676724A (en) * | 1923-03-06 | 1928-07-10 | Standard Oil Dev Co | Art of distillation |
GB312200A (en) * | 1927-12-19 | 1929-05-21 | Lewis Sidney Fraser | Improved method of and means for treating noxious and other fumes |
FR728741A (en) * | 1931-12-22 | 1932-07-11 | Exhaust purifier | |
US1962153A (en) * | 1931-06-18 | 1934-06-12 | Atlantic Refining Co | Fractional distillation |
US2368261A (en) * | 1943-04-16 | 1945-01-30 | Jr Frederick E Neef | Method of removing dye and tetraethyl lead from gasoline |
US2397142A (en) * | 1941-04-24 | 1946-03-26 | Styles T Howard | Filter |
-
1944
- 1944-05-29 US US537827A patent/US2448235A/en not_active Expired - Lifetime
Patent Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US666785A (en) * | 1899-06-05 | 1901-01-29 | John F Williams | Generator for hydrocarbon-burners. |
US646558A (en) * | 1899-11-01 | 1900-04-03 | Jean Alexandre Rey | Furnace for burning hydrocarbons, &c. |
US944456A (en) * | 1907-05-28 | 1909-12-28 | Empire Light Ltd | Vapor-burning apparatus. |
US1594296A (en) * | 1921-11-09 | 1926-07-27 | Louis E Lee | Apparatus for distilling oils |
US1676724A (en) * | 1923-03-06 | 1928-07-10 | Standard Oil Dev Co | Art of distillation |
US1604235A (en) * | 1924-06-13 | 1926-10-26 | M O R Products Company | Process for removing sulphur compounds from petroleum oils |
GB312200A (en) * | 1927-12-19 | 1929-05-21 | Lewis Sidney Fraser | Improved method of and means for treating noxious and other fumes |
US1962153A (en) * | 1931-06-18 | 1934-06-12 | Atlantic Refining Co | Fractional distillation |
FR728741A (en) * | 1931-12-22 | 1932-07-11 | Exhaust purifier | |
US2397142A (en) * | 1941-04-24 | 1946-03-26 | Styles T Howard | Filter |
US2368261A (en) * | 1943-04-16 | 1945-01-30 | Jr Frederick E Neef | Method of removing dye and tetraethyl lead from gasoline |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2812017A (en) * | 1953-02-24 | 1957-11-05 | Isadore N Vant | Automatic burner |
US2969320A (en) * | 1959-02-03 | 1961-01-24 | Socony Mobil Oil Co Inc | Removal of tetraethyl lead from hydrocarbon liquids with sulfur dioxide |
US3923643A (en) * | 1974-06-14 | 1975-12-02 | Shell Oil Co | Removal of lead and other suspended solids from used hydrocarbon lubricating oil |
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