US2109005A - Preparation of lead-sodium alloys - Google Patents
Preparation of lead-sodium alloys Download PDFInfo
- Publication number
- US2109005A US2109005A US19148A US1914835A US2109005A US 2109005 A US2109005 A US 2109005A US 19148 A US19148 A US 19148A US 1914835 A US1914835 A US 1914835A US 2109005 A US2109005 A US 2109005A
- Authority
- US
- United States
- Prior art keywords
- alloy
- lead
- stirring
- particles
- sodium
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 229910000528 Na alloy Inorganic materials 0.000 title description 16
- 238000002360 preparation method Methods 0.000 title description 5
- 229910045601 alloy Inorganic materials 0.000 description 50
- 239000000956 alloy Substances 0.000 description 50
- 239000002245 particle Substances 0.000 description 25
- 238000003756 stirring Methods 0.000 description 19
- 238000000034 method Methods 0.000 description 16
- KEAYESYHFKHZAL-UHFFFAOYSA-N Sodium Chemical compound [Na] KEAYESYHFKHZAL-UHFFFAOYSA-N 0.000 description 15
- 238000001816 cooling Methods 0.000 description 10
- -1 alkyl lead compounds Chemical class 0.000 description 9
- 239000013078 crystal Substances 0.000 description 9
- 239000000428 dust Substances 0.000 description 7
- 238000000227 grinding Methods 0.000 description 7
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 6
- HRYZWHHZPQKTII-UHFFFAOYSA-N chloroethane Chemical compound CCCl HRYZWHHZPQKTII-UHFFFAOYSA-N 0.000 description 6
- 229960003750 ethyl chloride Drugs 0.000 description 6
- 238000007873 sieving Methods 0.000 description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 238000000354 decomposition reaction Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- MRMOZBOQVYRSEM-UHFFFAOYSA-N tetraethyllead Chemical compound CC[Pb](CC)(CC)CC MRMOZBOQVYRSEM-UHFFFAOYSA-N 0.000 description 4
- 150000002611 lead compounds Chemical class 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000007710 freezing Methods 0.000 description 2
- 230000008014 freezing Effects 0.000 description 2
- 239000011261 inert gas Substances 0.000 description 2
- 235000011121 sodium hydroxide Nutrition 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- 150000001350 alkyl halides Chemical class 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 238000010961 commercial manufacture process Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000002939 deleterious effect Effects 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000009877 rendering Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
- C07F7/00—Compounds containing elements of Groups 4 or 14 of the Periodic Table
- C07F7/24—Lead compounds
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C11/00—Alloys based on lead
- C22C11/02—Alloys based on lead with an alkali or an alkaline earth metal as the next major constituent
Definitions
- This invention relates to lead-sodium alloys and processes for preparing the same and more particularly to such alloys employed in the manufacture of organic lead compounds.
- an alkyl halide is contacted with a lead mono-sodium alloy in an autoclave at temperatures starting at about 30 to 40 C.
- the lead mono-sodium alloy employed in this process has ordinarily been prepared by melting together the lead and sodium, then pouring into molds, cooling, and then grinding.
- the particle size of alloy thus prepared varies from about 40 mesh and smaller, to pieces of about inch or more in diameter admixed with considerable amounts of the alloy in the form of dust.
- An object of the present invention is to prepare a lead mono-sodium alloy in a form which has not been employed heretofore.
- a further object is to prepare a lead mono-sodium alloy in a form such as will permit higher yields of alkyl lead compounds to be produced.
- a still further object is to provide a process for preparing alkyl lead compounds whereby higher yields of the compound may be produced.
- Other objects are to provide new compositions of matter and to advance the art. Still other objects will appear hereinafter.
- a lead mono-sodium alloy in the form of small uniformly sized substantially dust-free particles preferably not larger than about A; inch and also preferably larger than about inch in diameter.
- substantially dust-free particles preferably not larger than about A; inch and also preferably larger than about inch in diameter.
- uniform I mean that the smallest particle must not be less than about the size of the largest particle.
- Such alloy may be obtained by various methods.
- Dust that has not been exposed and become coated with decomposition products is abnormally reactive and, as a result, the reaction with ethyl chloride is so rapid that it is very diflicult to control the temperature of the reaction mass.
- Large pieces of alloy present only a small surface area for contact with ethyl chloride and hence react very slowly and inefficiently.
- Such uniformly sized particles may be obtained by sieving ordinary ground alloy.
- this method is expensive and diflicult to operate as it involves the steps of casting, grinding and sieving. It is practically impossible to prevent access of air in the grinding and sieving operations and consequent loss of alloy due to decomposition. Also a large proportion of the alloy must be remelted, reground and resieved.
- This new method comprises cooling a molten lead mono-sodium alloy, with stirring,
- the alloy assumes the form of uniformly sized crystals of octahedral structure or the form of well polished particles.
- grained alloy Alloy prepared by this more rapid stirring of the molten alloy will be hereinafter termed grained alloy.
- rapid stirring I mean something on the order of '10 to 30 times as rapid as the slow stirring previously referred to.
- rate at which an agitator can be run when workingwith materials of this kind which limit varies with the type of vessel or agitator employed and the size of charge treated.
- the agitator will generally run at about 15 revolutions per minute. This, I have found, is very satisfactory for my purpose in preparing the grained alloy.
- the hot alloy has a great aflinity for moisture it should be maintained in an atmosphere of a dry oxygen free inert gas during the cooling and stirring operation. From a safety and economic standpoint, nitrogen is to be preferred for this purpose. However, if desired, other inert gases such as hydrogen, helium and r the like may be employed.
- the alloy freezes at about 371 C. Crystals are formed upon cooling to only a few degrees below the freezing point with stirring. These crystals have a wet appearance and, if the stirring is discontinued at this point, the particles of alloy tend to adhere to each other and are difficult, if not impossible, to separate, resulting in a conglomerate mass that offers no advantage over ordinary large lumps of alloy. However, if the stirring is continued until the temperature of the alloy reaches about 300 0., or less, the particles have a dry appearance and do not tend to adhere together. Thus the stirring may be stopped when the alloy reaches about 300 0.; or when it has this dry appearance. However I preferably continue the stirring until the alloy reaches a temperature of 275 C. or less, as a safety factor. Continued stirring below this point does not result in any material advantages but merely results in rounding the edges of the crystals to a greater extent.-
- T'his last method of obtaining uniformly sized particles of the alloy is generally to be preferred over the process of grinding and sieving as it is cheaper to operate and there is less loss in material. It is also much more difficult to' prevent exposure of the alloy to the atmosphere during grinding and sieving operations, hence a purer and more satisfactory alloy may be obtained according to my preferred method.
- Example Lead mono-sodium alloy was prepared in four diflerent forms as follows:
- a lead mono-sodium alloy in the form of small uniformly sized discrete crystals of octahedral structure and having their edges rounded off and their surfaces well polished.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
Patented Feb. 22, 1938 UNITED STATES PATENT OFFICE PREPARATION OF LEAD-SODIUM ALLOYS No Drawing. Application May 1, 1935, Serial No. 19,148
5 Claims.
This invention relates to lead-sodium alloys and processes for preparing the same and more particularly to such alloys employed in the manufacture of organic lead compounds.
In the present commercial manufacture of organic lead compounds and particularly of alkyl lead compounds, an alkyl halide is contacted with a lead mono-sodium alloy in an autoclave at temperatures starting at about 30 to 40 C. The lead mono-sodium alloy employed in this process, up to the present time, has ordinarily been prepared by melting together the lead and sodium, then pouring into molds, cooling, and then grinding. The particle size of alloy thus prepared varies from about 40 mesh and smaller, to pieces of about inch or more in diameter admixed with considerable amounts of the alloy in the form of dust.
While high yields of alkyl lead compounds have been obtained by this process, the yields have not proved to be entirely satisfactory and the reaction has not proceeded as smoothly as desired. I have found that the yield of alkyl lead compound varies in accordance with the particle size and physical condition of the alloy and the presence or absence of appreciable amounts of alloy in the form of dust.
An object of the present invention is to prepare a lead mono-sodium alloy in a form which has not been employed heretofore. A further object is to prepare a lead mono-sodium alloy in a form such as will permit higher yields of alkyl lead compounds to be produced. A still further object is to provide a process for preparing alkyl lead compounds whereby higher yields of the compound may be produced. Other objects are to provide new compositions of matter and to advance the art. Still other objects will appear hereinafter.
These objects may be accomplished in accordance with my invention which comprises preparing and employing a lead mono-sodium alloy in the form of small uniformly sized substantially dust-free particles preferably not larger than about A; inch and also preferably larger than about inch in diameter. By uniform, I mean that the smallest particle must not be less than about the size of the largest particle. Such alloy may be obtained by various methods.
In the grinding of lead mono-sodium alloy, as in other materials, a considerable proportion is reduced to dust which, on account of the enormously increased surface area, is extremely sensitive to the action of oxygen and moisture in the air forming, among other things, caustic soda.
As a result, a considerable proportion of the very finely divided alloy is decomposed and lost, and, at the same time, the caustic soda introduced into the reaction mass of lead sodium alloy and ethyl chloride has a marked deleterious effect on the reaction. Fine alloy or dust that has been exposed to the atmosphere appears to become coated with the decomposition products, which products prevent ready contact of the ethyl chloride with the pure alloy within the particles. Accordingly, these coated particles react very slowly,-if at all. It is also probable that the larger particles become coated with the decomposition products of the smaller particles thereby decreasing the efficiency of contact between the larger particles and the ethyl chloride. Dust that has not been exposed and become coated with decomposition products is abnormally reactive and, as a result, the reaction with ethyl chloride is so rapid that it is very diflicult to control the temperature of the reaction mass. Large pieces of alloy, on the other hand, present only a small surface area for contact with ethyl chloride and hence react very slowly and inefficiently.
I have found that uniformly sized particles of about inch to about inch in diameter and which are substantially free from dust are far more stable against slight exposure to air than is dust and will react with ethyl chloride and the like in a smooth manner with increase in the production of alkyl lead compounds and permit ready control of the temperatures. These uniformly sized particles greatly decrease the loss of alloy and prevent the introduction of impurities into the alkyl lead autoclave.
Such uniformly sized particles may be obtained by sieving ordinary ground alloy. However, this method is expensive and diflicult to operate as it involves the steps of casting, grinding and sieving. It is practically impossible to prevent access of air in the grinding and sieving operations and consequent loss of alloy due to decomposition. Also a large proportion of the alloy must be remelted, reground and resieved.
I have also discovered a, method whereby dustfree uniformly sized particles may be more readily obtained without the disadvantages attending the grinding and sieving as above described. This new method comprises cooling a molten lead mono-sodium alloy, with stirring,
to a temperature below that at which particles of the alloy tend to adhere to each other. By this process, the alloy assumes the form of uniformly sized crystals of octahedral structure or the form of well polished particles. When alloy, thus produced, is employed in the'preparation of alkyl lead compounds, particularly in the preparation of tetraethyl lead, the yield of the alkyl lead compound is materially increased.
It would ordinarily be expected that, if a lead mono-sodium alloy is prepared in a molten state and stirred until it cools well below its freezing point, the alloy would freeze the agitator. I have found this not to be the case. I have found that, if molten lead mono-sodium alloy is stirred at a very slow rate of speed until the alloy is cooled to below 300 C., the alloy forms particles of almost perfect uniformly sized crystals of octahedral structure. By stirring at a very slow rate of speed, I mean stirring at a rate such that the agitator is barely moving. Such stirring may be done by hand or by mechanical means, if desired.
If rapid stirring is employed, the edges of the crystals, as they are formed, are rounded off by the friction of agitation with the result that, instead of crystals of octahedral structure being obtained, the alloy is formed as well polished particles. Alloy prepared by this more rapid stirring of the molten alloy will be hereinafter termed grained alloy. By rapid stirring I mean something on the order of '10 to 30 times as rapid as the slow stirring previously referred to. There is necessarily a definite mechanical limit to the rate at which an agitator can be run when workingwith materials of this kind, which limit varies with the type of vessel or agitator employed and the size of charge treated. In a conventional crystallizing kettle, for example, the agitator will generally run at about 15 revolutions per minute. This, I have found, is very satisfactory for my purpose in preparing the grained alloy.
Since the hot alloy has a great aflinity for moisture it should be maintained in an atmosphere of a dry oxygen free inert gas during the cooling and stirring operation. From a safety and economic standpoint, nitrogen is to be preferred for this purpose. However, if desired, other inert gases such as hydrogen, helium and r the like may be employed.
The alloy freezes at about 371 C. Crystals are formed upon cooling to only a few degrees below the freezing point with stirring. These crystals have a wet appearance and, if the stirring is discontinued at this point, the particles of alloy tend to adhere to each other and are difficult, if not impossible, to separate, resulting in a conglomerate mass that offers no advantage over ordinary large lumps of alloy. However, if the stirring is continued until the temperature of the alloy reaches about 300 0., or less, the particles have a dry appearance and do not tend to adhere together. Thus the stirring may be stopped when the alloy reaches about 300 0.; or when it has this dry appearance. However I preferably continue the stirring until the alloy reaches a temperature of 275 C. or less, as a safety factor. Continued stirring below this point does not result in any material advantages but merely results in rounding the edges of the crystals to a greater extent.-
T'his last method of obtaining uniformly sized particles of the alloy is generally to be preferred over the process of grinding and sieving as it is cheaper to operate and there is less loss in material. It is also much more difficult to' prevent exposure of the alloy to the atmosphere during grinding and sieving operations, hence a purer and more satisfactory alloy may be obtained according to my preferred method.
In order to more clearly illustrate my invention and the advantages thereof the following example is given:'
Example Lead mono-sodium alloy was prepared in four diflerent forms as follows:
(A) Cast alloy, ground to irregular particle size of M inch and less.
(B) Ground alloy passed through a 40 mesh screen.
(C) A single solid piece of alloy (D) Grained alloy of uniform size of a; to 3';
inch particle size obtained by rapidly stirring yield of alkyl lead compound, rendering the operation much smoother, making it easier to control the temperature'of the reaction, is easier to handle and has a less tendency to oxidize in the atmosphere than alloy prepared in any other manner.
While I have disclosed specific methods for preparing my new alloy and its use in the preparation of tetraethyl lead it will be readily understood by those skilled in the art that variations and modifications may be made in such processes and the alloy may be employed for preparing other organic lead compounds without departing from the spirit of my invention. Accordingly, the scope of my invention is to be limited solely by the appended claims, construed as broadly as is permissible in view 01' the prior art.
I claim:
1. The process of preparing a lead monosodium alloy which comprises cooling the molten alloy to a temperature below that at which particles of the alloy tend to adhere to each other and stirring the mass during such cooling, the entire operation being carried out in the absence of moisture and oxygen.
2. The process of preparing a lead monosodium alloy which comprises cooling the molten alloy to a temperature of about 275 C. and stirring the mass during such cooling, the entire operation being carried out in the absence of moisture and oxygen.
3. The process of preparing a lead monosodium alloy which comprises cooling the molten alloy to a temperature below that at which particles of the alloy tend to adhereto each other and rapidly stirring the mass during such cooling, the entire operation being carried out in the absence of moisture and oxygen.
4. A lead mono-sodium alloy in the form of small uniformly sized discrete crystals of octahedral structure.
5. A lead mono-sodium alloy in the form of small uniformly sized discrete crystals of octahedral structure and having their edges rounded off and their surfaces well polished.
LOUIS S. BAKE.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US19148A US2109005A (en) | 1935-05-01 | 1935-05-01 | Preparation of lead-sodium alloys |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US19148A US2109005A (en) | 1935-05-01 | 1935-05-01 | Preparation of lead-sodium alloys |
Publications (1)
Publication Number | Publication Date |
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US2109005A true US2109005A (en) | 1938-02-22 |
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US19148A Expired - Lifetime US2109005A (en) | 1935-05-01 | 1935-05-01 | Preparation of lead-sodium alloys |
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Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2425725A (en) * | 1941-08-26 | 1947-08-19 | Bell Telephone Labor Inc | Method of casting and rapid analysis of alloys |
US2572887A (en) * | 1948-05-29 | 1951-10-30 | Stanton Robert | Solid-liquid reaction processes |
US2577289A (en) * | 1950-06-05 | 1951-12-04 | Tiganik Leonhard | Method of activating alkali metals |
US2619496A (en) * | 1951-08-07 | 1952-11-25 | Stanton Robert | Solid-liquid reaction processes |
US2635107A (en) * | 1952-11-10 | 1953-04-14 | Ethyl Corp | Manufacture of tetraalkyllead compounds |
US2717206A (en) * | 1951-11-27 | 1955-09-06 | Ethyl Corp | Method for preparation of lead-sodium alloys |
US2744126A (en) * | 1950-05-02 | 1956-05-01 | Du Pont | Preparation of lead-sodium alloy and tetraethyllead |
US3472637A (en) * | 1968-06-05 | 1969-10-14 | Ppg Industries Inc | Lead-alkali metal particles |
US3881953A (en) * | 1973-11-26 | 1975-05-06 | St Joe Minerals Corp | Battery electrode grids and method of making same from a lead-calcium-lithium-tin alloy |
-
1935
- 1935-05-01 US US19148A patent/US2109005A/en not_active Expired - Lifetime
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2425725A (en) * | 1941-08-26 | 1947-08-19 | Bell Telephone Labor Inc | Method of casting and rapid analysis of alloys |
US2572887A (en) * | 1948-05-29 | 1951-10-30 | Stanton Robert | Solid-liquid reaction processes |
US2744126A (en) * | 1950-05-02 | 1956-05-01 | Du Pont | Preparation of lead-sodium alloy and tetraethyllead |
US2577289A (en) * | 1950-06-05 | 1951-12-04 | Tiganik Leonhard | Method of activating alkali metals |
US2619496A (en) * | 1951-08-07 | 1952-11-25 | Stanton Robert | Solid-liquid reaction processes |
US2717206A (en) * | 1951-11-27 | 1955-09-06 | Ethyl Corp | Method for preparation of lead-sodium alloys |
US2635107A (en) * | 1952-11-10 | 1953-04-14 | Ethyl Corp | Manufacture of tetraalkyllead compounds |
US3472637A (en) * | 1968-06-05 | 1969-10-14 | Ppg Industries Inc | Lead-alkali metal particles |
US3881953A (en) * | 1973-11-26 | 1975-05-06 | St Joe Minerals Corp | Battery electrode grids and method of making same from a lead-calcium-lithium-tin alloy |
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