US2626879A - Process of removing deposits containing lead compounds - Google Patents
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- US2626879A US2626879A US167658A US16765850A US2626879A US 2626879 A US2626879 A US 2626879A US 167658 A US167658 A US 167658A US 16765850 A US16765850 A US 16765850A US 2626879 A US2626879 A US 2626879A
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- ammonium acetate
- lead compounds
- solution
- containing lead
- deposits
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- 238000000034 method Methods 0.000 title claims description 37
- 150000002611 lead compounds Chemical class 0.000 title claims description 28
- USFZMSVCRYTOJT-UHFFFAOYSA-N Ammonium acetate Chemical compound N.CC(O)=O USFZMSVCRYTOJT-UHFFFAOYSA-N 0.000 claims description 31
- 239000005695 Ammonium acetate Substances 0.000 claims description 31
- 229940043376 ammonium acetate Drugs 0.000 claims description 31
- 235000019257 ammonium acetate Nutrition 0.000 claims description 31
- 229910052751 metal Inorganic materials 0.000 claims description 28
- 239000002184 metal Substances 0.000 claims description 28
- 239000007864 aqueous solution Substances 0.000 claims description 7
- 239000000243 solution Substances 0.000 description 29
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 13
- 238000002485 combustion reaction Methods 0.000 description 12
- 239000000446 fuel Substances 0.000 description 12
- 239000003112 inhibitor Substances 0.000 description 11
- 229910021529 ammonia Inorganic materials 0.000 description 6
- 239000012530 fluid Substances 0.000 description 6
- 239000000470 constituent Substances 0.000 description 5
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 4
- 238000001816 cooling Methods 0.000 description 4
- 239000005416 organic matter Substances 0.000 description 4
- 238000010992 reflux Methods 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- 150000001412 amines Chemical class 0.000 description 3
- 238000010494 dissociation reaction Methods 0.000 description 3
- 230000005593 dissociations Effects 0.000 description 3
- 150000002739 metals Chemical class 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 3
- 229910001220 stainless steel Inorganic materials 0.000 description 3
- 239000010935 stainless steel Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 229910019142 PO4 Inorganic materials 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 230000002939 deleterious effect Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 2
- 235000021317 phosphate Nutrition 0.000 description 2
- 229940085991 phosphate ion Drugs 0.000 description 2
- MRMOZBOQVYRSEM-UHFFFAOYSA-N tetraethyllead Chemical compound CC[Pb](CC)(CC)CC MRMOZBOQVYRSEM-UHFFFAOYSA-N 0.000 description 2
- 238000009834 vaporization Methods 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- WSLDOOZREJYCGB-UHFFFAOYSA-N 1,2-Dichloroethane Chemical compound ClCCCl WSLDOOZREJYCGB-UHFFFAOYSA-N 0.000 description 1
- PAAZPARNPHGIKF-UHFFFAOYSA-N 1,2-dibromoethane Chemical compound BrCCBr PAAZPARNPHGIKF-UHFFFAOYSA-N 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- 241000212384 Bifora Species 0.000 description 1
- 229910001018 Cast iron Inorganic materials 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000012752 auxiliary agent Substances 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 230000001186 cumulative effect Effects 0.000 description 1
- MNNHAPBLZZVQHP-UHFFFAOYSA-N diammonium hydrogen phosphate Chemical compound [NH4+].[NH4+].OP([O-])([O-])=O MNNHAPBLZZVQHP-UHFFFAOYSA-N 0.000 description 1
- ZASWJUOMEGBQCQ-UHFFFAOYSA-L dibromolead Chemical compound Br[Pb]Br ZASWJUOMEGBQCQ-UHFFFAOYSA-L 0.000 description 1
- 230000004069 differentiation Effects 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 229910000464 lead oxide Inorganic materials 0.000 description 1
- PIJPYDMVFNTHIP-UHFFFAOYSA-L lead sulfate Chemical compound [PbH4+2].[O-]S([O-])(=O)=O PIJPYDMVFNTHIP-UHFFFAOYSA-L 0.000 description 1
- HWSZZLVAJGOAAY-UHFFFAOYSA-L lead(II) chloride Chemical compound Cl[Pb]Cl HWSZZLVAJGOAAY-UHFFFAOYSA-L 0.000 description 1
- 238000005461 lubrication Methods 0.000 description 1
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 1
- 150000002898 organic sulfur compounds Chemical class 0.000 description 1
- YEXPOXQUZXUXJW-UHFFFAOYSA-N oxolead Chemical compound [Pb]=O YEXPOXQUZXUXJW-UHFFFAOYSA-N 0.000 description 1
- 239000010452 phosphate Substances 0.000 description 1
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 1
- 150000003016 phosphoric acids Chemical class 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000005488 sandblasting Methods 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23G—CLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
- C23G1/00—Cleaning or pickling metallic material with solutions or molten salts
- C23G1/24—Cleaning or pickling metallic material with solutions or molten salts with neutral solutions
- C23G1/26—Cleaning or pickling metallic material with solutions or molten salts with neutral solutions using inhibitors
Definitions
- the invention in general, relates to prime movers of the internal combustion type. More particularly, the invention relates to a novel and useful process and apparatus for improving the performance characteristics of such prime movers.
- the anti-knock fluids hereinafter referred to merely as the ethylfluids which are incorporated into gasolines for improving the octane rating thereof consist of tetra-ethyl-leadand other auxiliary agents, such as ethylene dichloride and ethylene dibromide as well as added organic dyes, the latter merely being included for purposes of differentiation or identification.
- auxiliary agents such as ethylene dichloride and ethylene dibromide
- added organic dyes such as added organic dyes
- the deposits containing lead compounds, as aforesaid, on the various parts of an engine utilizing ethyl-fluids are cumulative and, unless periodically removed, will have a deleterious eifect upon the performance characteristics of the engine not only as to its efiiciency but also as to development of hot spots which, in turn, causes fatigue of the metal.
- the present invention is directed to the provision of means for obviating the above mentioned inherent deleterious efiects of the leaded fuels in the operation of combustion prime movers and, at the same time, of reducing the time and expense heretofore involved in effecting the removal of the aforementioned deposits containing lead compounds.
- One of the primary objects of my present in- V vention is to provide an improved method of effectively and expeditiously removing lead deposits from parts of an engine which has been operating with leaded fuels.
- Another important object of the present invention is to provide a relatively simple process of the indicated nature which is additionally characterized by its appreciably low cost and the minimum of time involved in effecting the removal of deposits containing lead compounds from equipment of the hereinabove mentioned type.
- a still further object of my invention is to provide an improved method of the aforementioned character which can be practiced and handled by the unskilled with the same effectiveness, dispatch and safety as any skilled person.
- the single view is a sectional elevational view of an exemplification of equipment which may be employed in practicing the preferred mode of the invention.
- the improved method of removing deposits containing lead compounds from internal combustion engine parts preferably comprises imrnersing or subjecting the parts of such an engine on which such deposits are found in or to a hot aqueous solution of ammonium acetate.
- I prepare a 30 to 40 per cent concentration of an ammonium acetate solution wherein the ammonium acetate is present in an amount, by weight, of between 30 and 40 per cent of the total solution.
- the solution is an aqueous ammonium acetate solution.
- I add a small amount of a suitable inhibitor, in order to reduce the corrosive action to an absolute minimum.
- a reflux cooling unit and preferably mount the same on the under side of the cover or lid l6-of the tank H which is removably mounted thereon.
- the reflux cooling unit preferably employed consists of a length of stainless steel tubing l'l coiled around the underside of the lid l6 and welded or otherwise permanently secured thereto.
- tubing ll extend through or pierce the cover l6 of tank I I and can be conveniently provided with fittings, not shown, for attaching suitable pipes, not shown, thereto whereby a coolant, such as cold water, can be continuously passed through the coil of stainless steel tubing H from a source, not shown, and thereby the vaporization of the heated solution l3 in the tank is kept to a minimum.
- a coolant such as cold water
- the optimum concentration of the ammonium acetate solution is between approximately 30 and approximately 40 per cent, by weight. I have found that such a concentration of ammonium acetate, when heated to elevated temperature, is capable of dissolving its molecular equivalent of lead compounds and, accordingly, that a single charge of this chemical can be used for the treatment of a considerable number of engine parts.
- a method of removing deposits of lead compounds and carbonaceous organic matter from metal parts of internal combustion engines utilizing ethyl-fluids as the fuel comprising contacting the deposit-carrying parts a loose the carbonaceous organic matter of the lead compounds from metal par-ts, said method comprising contacting the deposit-carrying metal parts with an aqueous. solution of ammonium acetate.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
Description
INVENTOR.
ATTORNEY A. LAZAR Jan. 27, 1953 PROCESS OF REMOVING DEPOSITS CONTAINING LEAD COMPOUNDS Filed June 12, 1950 ARTHUR LA ZAR BY Patented Jan. 27, 1953 PROCESS OF REMOVING DEPOSITS CONTAINING LEAD COMPOUNDS Arthur Lazar, San Francisco, Calif. I
Application June 12, 1950, Serial No. 167,658
11 Claims. I
The invention, in general, relates to prime movers of the internal combustion type. More particularly, the invention relates to a novel and useful process and apparatus for improving the performance characteristics of such prime movers.
As is perhaps well known, the anti-knock fluids hereinafter referred to merely as the ethylfluids, which are incorporated into gasolines for improving the octane rating thereof consist of tetra-ethyl-leadand other auxiliary agents, such as ethylene dichloride and ethylene dibromide as well as added organic dyes, the latter merely being included for purposes of differentiation or identification. During combustion of such leaded gasolines, the organic portions of the ethyl-fluids will bur'n'whereas the lead portion is converted to inorganic lead compounds, such as lead oxide, lead chloride and lead bromide. Since there are minor proportions of organic sulfur compounds present in almost any kind of gasoline, lead sulfate is formed also during the combustion of a leaded fuel. While some of the lead-carrying reaction products of the combustion gases, evolved from the combustion of such fuels may be completely eliminated through the engine exhaust, appreciable quantities thereof are trapped in various parts of an engine and are deposited thereon. It has been found, upon inspection of an engine that has been operated with leaded fuel that a greyish sediment is deposited on the bottom of the engine crankcase or in the oil ducts of the lubrication system. On those parts of the engine which have been exposed to higher temperatures, for example, piston tops, exhaust manifold and exhaust lines, hard carbonaceous deposits of very high lead content were usually found.
The steady trend towards increasingly higher compression ratios in automotive spark ignition engines on one hand, and the high performance requirements of air-craft engines on the other hand are responsible for the steady increase in' the proportion of tetra-ethyl lead fluid of premium and aviation type gasolines. It stands to reason that the higher the lead content of a fuel, the greater will be its tendency to accumulate deposits containing lead compounds in the combustion chamber and exhaust system. Therefore, the cleaning and overhauling of aircraft engines involves a particularly tedious and time consuming operation, inasmuch as the deposits containing lead compounds are so firmly baked on that the engine parts have to be cleaned by mechanical means such as scraping or sand blasting.
It is to be appreciated that the deposits containing lead compounds, as aforesaid, on the various parts of an engine utilizing ethyl-fluids are cumulative and, unless periodically removed, will have a deleterious eifect upon the performance characteristics of the engine not only as to its efiiciency but also as to development of hot spots which, in turn, causes fatigue of the metal. The present invention is directed to the provision of means for obviating the above mentioned inherent deleterious efiects of the leaded fuels in the operation of combustion prime movers and, at the same time, of reducing the time and expense heretofore involved in effecting the removal of the aforementioned deposits containing lead compounds.
It should also -be mentioned here, that deposits containing lead compounds are also found in the burner tubes of the heating units employed on various types of aircraft for maintaining comfortable temperatures plane during high altitude flying or in cold weather. result of the combustion of the same leaded fuel, which is used for feeding the aircraft engines, they resemble in composition quite closely the aforementioned deposits in the exhaust system. Consequently, these deposits, present in the heating units, can be removed just as readily by the process of this invention.
One of the primary objects of my present in- V vention is to provide an improved method of effectively and expeditiously removing lead deposits from parts of an engine which has been operating with leaded fuels.
Another important object of the present invention is to provide a relatively simple process of the indicated nature which is additionally characterized by its appreciably low cost and the minimum of time involved in effecting the removal of deposits containing lead compounds from equipment of the hereinabove mentioned type.
A still further object of my invention is to provide an improved method of the aforementioned character which can be practiced and handled by the unskilled with the same effectiveness, dispatch and safety as any skilled person.
Other objects of the invention, together with some of its advantageous features, will appear from the following description of a preferred mode of practicing the present invention an exemplification of one type of equipment which may be employed in practicing the invention being illustrated in the accompanying drawing. It is to be understood, however, that I am not inside the' Since these deposits are likewise the to be limited to the precise mode of or the order of steps set forth in the description of my process, as the invention, as defined in the appended claims can be practiced in a variety and plurality of ways.
Referring to the drawing:
The single view is a sectional elevational view of an exemplification of equipment which may be employed in practicing the preferred mode of the invention.
In its preferred mode, the improved method of removing deposits containing lead compounds from internal combustion engine parts preferably comprises imrnersing or subjecting the parts of such an engine on which such deposits are found in or to a hot aqueous solution of ammonium acetate.
In accordance with my invention, I prepare a 30 to 40 per cent concentration of an ammonium acetate solution wherein the ammonium acetate is present in an amount, by weight, of between 30 and 40 per cent of the total solution. As indicated above, the solution is an aqueous ammonium acetate solution. In order to avoid possible chemical attack upon the part of the ammonium acetate upon the metal of the engine parts to be treated, I add a small amount of a suitable inhibitor, in order to reduce the corrosive action to an absolute minimum. It is to be observed, in this connection, that in tests that I have conducted for removing deposits containing lead compounds from engine parts of an engine that has operated with leaded fuel, there is only a negligible attack at all events on the metal parts by the ammonium acetate, but very little, if any, attack when the suitable inhibitor is introduced and utilized in the aqueous ammonium acetate, as hereinafter described.
The parts to .be freed from deposits containing lead compounds may consist of a variety of metals; in most cases, they will be cast iron, steel, cast aluminum, or sheet aluminum. I have found the best all around inhibitor for ammonium acetate (de-leading) solution is provided by phosphate ion. The phosphate type inhibitor may be incorporated into the ammonium acetate solution in form of an inorganic or organic salt of phosphoric acid of a pH which matches as closely as possible that of the ammonium acetate solution itself. The pH of freshly prepared ammonium acetate solution may vary between 7.0 and 7.5. I have found that during the de-leading operation while the solution is consistently boiling under reflux, the pH may gradually decrease to as low as 6.0, due to partial dissociation of the ammonium acetate. Therefore, an occasional check up appears advisable so that, if necessary, the pH can be brought back to thenormal range of 7.5 by the addition of the necessary'amount of ammonia. This can be accomplished either by means of concentrated aqueous ammonium solution or by the passing of ammonia gas into the treating tank. Di-ammonium phosphate which has a pH of 7.0 is the most suitable inhibitor. It is effective when added at a ratio as low-as .1%. For practical reasons I prefer to add approximately .5% of this inhibitor. Phosphates of organic amines are equally suitable provided that the pH is adjusted to that of the ammonium acetate solution itself. Depending on the basicity of the amine, the adjustment has to be made by selecting the proper ratio of amine and phosphoric acid. Of course, in metal parts consisting of stainless steel there is no attack at all even without the'use of inhibitors.
It is especially to be observed that in the application of my improved method, the metal parts carrying the deposits containing lead compounds are preferably soaked in the ammonium acetate solution maintained at elevated temperature and it has been demonstrated that the hardest of such deposits will disintegrate in approximately one hour or less and will leave the metal surface bright and clean after rinsing with fresh water. It has been found that in most cases the lead compounds represent the major constituent and the carbonaceous organic binder the minor constituent of such deposits. Consequently, as the ammonium acetate solution gradually dissolves the lead constituents, the deposit as a whole readily breaks loose from the metal parts under treatment.
In order to avoid loss of chemicals during the treatment, I have found it advisable to provide a reflux cooling unit on the container or receptacle in which the treatment is carried out and to this end have devised the apparatus illustrated in the annexed drawings as an exemplification of equipment that may .be employed in practicing the preferred mode of my invention. With reference to the single view, I have provided a suitable metal receptacle or tank I I having a relatively large opening 12 in the top thereof for passing the metal parts of an engine for soaking in the aqueous ammonium acetate 13 contained in the tank. Since the solution is preferably heated to since such solution, under such conditions will give ofi water vapor as well as ammonia and acetic acid due to the dissociation of the ammonium acetate molecule, I also provide in this exemplification a reflux cooling unit and preferably mount the same on the under side of the cover or lid l6-of the tank H which is removably mounted thereon. The reflux cooling unit preferably employed consists of a length of stainless steel tubing l'l coiled around the underside of the lid l6 and welded or otherwise permanently secured thereto. The ends of the tubing ll, indicated'at l8 and IS in the annexed drawings, extend through or pierce the cover l6 of tank I I and can be conveniently provided with fittings, not shown, for attaching suitable pipes, not shown, thereto whereby a coolant, such as cold water, can be continuously passed through the coil of stainless steel tubing H from a source, not shown, and thereby the vaporization of the heated solution l3 in the tank is kept to a minimum. Moreover, the composition of the ammonium acetate solution is thus kept fairly constant under such-conditions.
In addition to causing the lead constituents of the above mentioned deposits on engine parts to enter into the aqueous ammonium acetate under the aforesaid treatment, and the breaking loose of the carbonaceous matter, my improved method of treating such-'lead-carrying metal parts of the aforesaid engines is eflicaceous in the removal of scale and rust which often occurs in the exhaust lines, ball joints and muillers of combustion enginesoperating with leaded fuels. However, the scaleand rust do not dissolve to any great extent in the hot ammonium acetate solution but are to .be found on the'bottom of the treating vessel or receptacle! 1 as a brown sludge.
It .willbe clear'from a review of the foregoing and a consideration of the annexed drawing that I have provided a relatively simple and expeditious method as well as have indicated relatively simple apparatus for effectively removing lead near boiling temperature, and y compounds from deposits on metal parts of a combustion engine operating on leaded fuels. As indicated, the optimum concentration of the ammonium acetate solution is between approximately 30 and approximately 40 per cent, by weight. I have found that such a concentration of ammonium acetate, when heated to elevated temperature, is capable of dissolving its molecular equivalent of lead compounds and, accordingly, that a single charge of this chemical can be used for the treatment of a considerable number of engine parts. In view of the simplicity of the illustrated apparatus and the fact that the solution can be delivered to the premises where the process is to be practiced in sealed containers, it is evident that the entire process can be practiced and the apparatus utilized by unskilled persons with the same efiectiveness and the same dispatch as any skilled person. There are no fire hazards involved in the use of the apparatus and the assembly thereof is relatively simple and the process of treating the lead-compound carrying metal parts likewise is relatively simple. In view of the fact that my improved method can be practiced at a relatively small expense, appreciable savings can be had in efiecting the removal of the deposits containing lead compounds from engines of the type hereinabove mentioned. Moreover, the employment of such mechanical means as scrapers or sand blasters heretofore utilized for removing such deposits are eliminated.
It is to be understood that the appended claims are to be accorded a range of equivalents commensurate in scope with the advance made over the prior art.
I claim:
1. A method of removing deposits containing 5. A method of removing deposits containing lead compounds from metal parts, said method comprising contacting the deposit-carrying parts with an aqueous solution of ammonium acetate at elevated temperature, said solution containing an inhibitor, to prevent corrosive attack of metals, said inhibitor consistin of a phosphoric acid salt of substantially the same pH as ammonium acetate. x.
6. A method of removing deposits containing lead compounds from metal parts in accordance with claim 4; keeping the pH of the solution adjusted to approximately 7.0 by the addition of ammonia in aqueous form.
7. A method of removing deposits containing lead compounds from metal parts in accordance with claim 4; keeping the pH of the solution adjusted to approximately 7.0 by the addition of ammonia in gaseous form.
8. A method of removing deposits of lead compounds and carbonaceous organic matter from metal parts of internal combustion engines utilizing ethyl-fluids as the fuel, said method comprising contacting the deposit-carrying parts a loose the carbonaceous organic matter of the lead compounds from metal par-ts, said method comprising contacting the deposit-carrying metal parts with an aqueous. solution of ammonium acetate.
2. A method of removing deposits containing lead compounds from metal parts, said method comprising contacting the deposit-carrying parts with an aqueous solution of ammonium acetate at elevated temperature.
3. A method of removing deposits containing lead compounds from metal parts, said method comprising contacting the deposit-carrying parts with an aqueous solution of ammonium acetate at elevated temperature, said solution containin an inhibitor, to preventv corrosive attack of metals.
4. A method of removing deposits containing lead compounds from metal parts, said method comprising immersing the deposit-carrying parts in a contained volume of a hot aqueous solution of ammonium acetate in the presence of phosphate ion while simultaneously cooling the container holding the solution to keep vaporization of water and dissociation of the ammonium acetate at a minimum and to maintain the composition of the solution substantially constant while the metal parts are immersed therein.
deposits.
9. A method of removing deposits of lead compounds and carbonaceous organic matter from metal parts of internal combustion engines utilizing ethyl-fluids as the fuel, said method comprising contacting the deposit-carrying parts with an aqueous solution of ammonium acetate containing a metal-protecting inhibitor to disintegrate the lead constituents and to break loos the carbonaceous organic matter of the deposits.
10. A method in accordance with claim 9; keeping the pH of the solution adjusted to approximately 7.0 by the addition of ammonia in aqueous form.
11. A method in accordance with claim 9; keeping the pH of the solution adjusted to approximately 7.0 by the addition of ammonia in gaseous form.
ARTHUR LAZAR.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Number Name Date 1,918,817 Mantell July 18, 1933 2,181,553 Hiller Nov. 28, 1939 2,264,766 Mauersberger Dec. 2, 1941 2,408,931 Heath Oct. 8, 1946 2,465,228 Hein Mar. 22, 1949 2,476,823 ONeil July 19, 1949 2,508,215 Bishop May 16, 1950 ,5 3,956 Kleist Sept. 26, 1950
Claims (1)
1. A METHOD OF REMOVING DEPOSITS CONTAINING LEAD COMPOUNDS FROM METAL PARTS, SAID METHOD COMPRISING CONTACTING THE DEPOSIT-CARRYING METAL PARTS WITH AN AQUEOUS SOLUTION OF AMMONIUM ACETATE.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US167658A US2626879A (en) | 1950-06-12 | 1950-06-12 | Process of removing deposits containing lead compounds |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US167658A US2626879A (en) | 1950-06-12 | 1950-06-12 | Process of removing deposits containing lead compounds |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2626879A true US2626879A (en) | 1953-01-27 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US167658A Expired - Lifetime US2626879A (en) | 1950-06-12 | 1950-06-12 | Process of removing deposits containing lead compounds |
Country Status (1)
| Country | Link |
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| US (1) | US2626879A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2992995A (en) * | 1955-05-25 | 1961-07-18 | Purex Corp Ltd | Alkaline composition for cleaning metal |
| US2992946A (en) * | 1955-05-25 | 1961-07-18 | Purex Corp Ltd | Process for removing leaded deposits from metal |
| US3661643A (en) * | 1971-03-30 | 1972-05-09 | Ppg Industries Inc | Lead ring removal from a steam still |
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| US2465228A (en) * | 1946-05-07 | 1949-03-22 | Westinghouse Electric Corp | Liquid treatment of contact surfaces for copper oxide rectifiers |
| US2476823A (en) * | 1945-12-14 | 1949-07-19 | Firestone Tire & Rubber Co | Method of treating polonium plated metal |
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| US2523956A (en) * | 1947-01-18 | 1950-09-26 | Dole Refrigerating Co | Block freezing unit |
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1950
- 1950-06-12 US US167658A patent/US2626879A/en not_active Expired - Lifetime
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|---|---|---|---|---|
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| US2181553A (en) * | 1937-08-16 | 1939-11-28 | Hiller Vernon William | Milk cooler |
| US2264766A (en) * | 1938-03-01 | 1941-12-02 | Alframine Corp | Detergent and method for producing the same |
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| US2476823A (en) * | 1945-12-14 | 1949-07-19 | Firestone Tire & Rubber Co | Method of treating polonium plated metal |
| US2465228A (en) * | 1946-05-07 | 1949-03-22 | Westinghouse Electric Corp | Liquid treatment of contact surfaces for copper oxide rectifiers |
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| US2508215A (en) * | 1947-04-29 | 1950-05-16 | Socony Vacuum Oil Co Inc | Process of removing protective coating films from surfaces |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2992995A (en) * | 1955-05-25 | 1961-07-18 | Purex Corp Ltd | Alkaline composition for cleaning metal |
| US2992946A (en) * | 1955-05-25 | 1961-07-18 | Purex Corp Ltd | Process for removing leaded deposits from metal |
| US3661643A (en) * | 1971-03-30 | 1972-05-09 | Ppg Industries Inc | Lead ring removal from a steam still |
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