US2109005A - Preparation of lead-sodium alloys - Google Patents

Preparation of lead-sodium alloys Download PDF

Info

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
Application number
US19148A
Inventor
Louis S Bake
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
EIDP Inc
Original Assignee
EI Du Pont de Nemours and Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by EI Du Pont de Nemours and Co filed Critical EI Du Pont de Nemours and Co
Priority to US19148A priority Critical patent/US2109005A/en
Application granted granted Critical
Publication of US2109005A publication Critical patent/US2109005A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F7/00Compounds containing elements of Groups 4 or 14 of the Periodic Table
    • C07F7/24Lead compounds
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C11/00Alloys based on lead
    • C22C11/02Alloys 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.
US19148A 1935-05-01 1935-05-01 Preparation of lead-sodium alloys Expired - Lifetime US2109005A (en)

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
US2109005A true US2109005A (en) 1938-02-22

Family

ID=21791683

Family Applications (1)

Application Number Title Priority Date Filing Date
US19148A Expired - Lifetime US2109005A (en) 1935-05-01 1935-05-01 Preparation of lead-sodium alloys

Country Status (1)

Country Link
US (1) US2109005A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
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

Cited By (9)

* Cited by examiner, † Cited by third party
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

Similar Documents

Publication Publication Date Title
US3857705A (en) Small grain promoting aluminum-titanium-boron mother alloy
US2109005A (en) Preparation of lead-sodium alloys
JPH04231406A (en) Preparation of metal powder
US2029301A (en) Process of preparing tetra alkyl lead
US2485175A (en) Method of recovering hard metal carbides from sintered masses
US2765328A (en) Metals recovery
US3012878A (en) Titanium metal production process
US2635107A (en) Manufacture of tetraalkyllead compounds
US2453076A (en) Crystallization of ddt
US2897056A (en) Production of elemental boron by magnesium reduction
US2635105A (en) Manufacture of tetrallkyllead compounds
US2880084A (en) Process of preparing massive zirconium particles
US2008731A (en) Treatment of easily oxidizable alloys
US2807539A (en) Process for refining titanium
US2816020A (en) Method of producing titanium
US2861868A (en) Method of producing substantially white, globular sodium bisulfate
US2311307A (en) Production of metal carbonyls
US2994603A (en) Process of preparing columbium and tantalum
US2929678A (en) Method of producing zinc selenide
US2349190A (en) Recovery of finely divided magnesium scrap
US2497529A (en) Process for production of magnesium base alloys containing zirconium
US2202252A (en) Preparation of metallic oxides
GB883721A (en) Improvements in or relating to titanium production
US2886429A (en) Method for the reduction of uranium compounds
US2816021A (en) Method of producing titanium