US2029301A - Process of preparing tetra alkyl lead - Google Patents

Process of preparing tetra alkyl lead Download PDF

Info

Publication number
US2029301A
US2029301A US675089A US67508933A US2029301A US 2029301 A US2029301 A US 2029301A US 675089 A US675089 A US 675089A US 67508933 A US67508933 A US 67508933A US 2029301 A US2029301 A US 2029301A
Authority
US
United States
Prior art keywords
alloy
lead
particles
preparing
stirring
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
US675089A
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 US675089A priority Critical patent/US2029301A/en
Application granted granted Critical
Publication of US2029301A publication Critical patent/US2029301A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

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

Definitions

  • analkyl 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 amountsof the alloy inthe form of dust.
  • the object of this invention is to provide a process for preparing tetra alkyl lead 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 inch and also preferably larger than about inch in diameter.
  • substantially dust-free particles preferably not larger than about 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 ofthe largest particle.
  • Such alloy may be obtained by various methods.
  • 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'eiilciency of contact between the larger particlesand 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.
  • 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 30 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 resleved.
  • 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.
  • the alloy assumes the form of uniformly sized crystals of octahedral structure or the form of well polished particles.
  • the yield of the alkyl lead compound is materially increased.
  • 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 to times as rapid as the slow stirring previously referred to.
  • the rate at which an agitator can be run when working with 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 Since the hot alloy has a great affinity 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 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 advantage but merely results in rounding the edges of the crystals to a. greater extent.
  • This 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 difllcult to prevent .exposure of the alloy to the atmosphere durin 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 different forms as follows:
  • My alloy has the advantages of increasing the 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.
  • the process for preparing tetra alkyl lead which comprises contacting under reacting conditions, an organic halide with a lead monosodium alloy in the form of small substantially dust-free particles of a uniform size.
  • the process for preparing tetra alkyl lead which comprises contacting, under reacting conditions, an organic halide with a lead monosodium alloy in the form of small substantially dust-free crystals of octahedral structure of a uniform size and having their edges rounded off and their surfaces well polished.
  • the process for preparing tetraethyl lead which comprises contacting, under reacting conditions, ethyl chloride with a lead mono-sodium alloy in the form of small substantially dustfree crystals of octahedral structure of a uniform size 10.
  • the process for preparing tetraethyl lead which comprises contacting, under reacting conditions, ethyl chloride witha lead mono-sodium alloy in the form oi small substantially dustfree crystals of octahedral structure of a uniform size of about to about $4; inch in diameter.
  • the process for preparing tetraethyl lead which comprises contacting, under reacting conditions, ethyl chloride with a lead mono-sodium alloy in the form of small substantially dustfree crystals of octahedral structure of a uniform size and having their edges rounded off and their surfaces well polished.
  • the process for preparing tetraethyl lead which comprises contacting, under reacting con-- ditions, ethyl chloride with a lead mono-sodium alloy in the form of small substantially dust-free crystals of octahedral structure of a'uniiorm size of about to about M; inch in diameter and having their edges rounded oil and their surfaces well polished.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Manufacture Of Metal Powder And Suspensions Thereof (AREA)

Description

Patented Feb. 4, 1936 PROCESS or ranmamo mm mm. mm
Louis S. Bake, Penns grove, N. J., assignor to E. L du' Pont de Nemours & Company, Wilmington, Del., a corporation of Delaware No Drawing. Application June 9, 1933,
' Serial N0.'675,089
12 Claims.
In the present commercial manufacture of organic lead compounds and particularly of alkyl lead compounds, analkyl 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 amountsof the alloy inthe 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.
The object of this invention is to provide a process for preparing tetra alkyl lead 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 maybe 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 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 ofthe largest particle. Such alloy may be obtained by various methods.
Inthe 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 caustice 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'eiilciency of contact between the larger particlesand 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 3 1 inch to about inch in diameter and V which are substantially free from dust are far of alloy and prevent the introduction of impuri- 26 ties 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 30 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 resleved.
free 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. duced, 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.
I have also discovered a method whereby dust- When alloy, thus pro- It would ordinarily be expected that, if a lead it 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 to 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 working with 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 affinity 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 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 advantage but merely results in rounding the edges of the crystals to a. greater extent.
This 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 difllcult to prevent .exposure of the alloy to the atmosphere durin 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 different forms as follows:
(C) A single solid piece of alloy.
(D) Grainod alloy of uniform size off: to ,3g' inch particle size obtained by rapidly stirring molten alloy until .cooled to about 275 C.
100 grams of each of the above alloys A, B, C and D were reacted with 50 cc. of ethyl chloride in an autoclave under identical conditions such as are ordinarily employed for this reaction. The alloy and ethyl chloride were maintained in contact until reactionwas complete. tetraethyl lead obtained with alloy D, was several percent higher than that obtained with any of the other alloys.
My alloy has the advantages of increasing the 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 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 of the prior art.
Iclaim:
1. The process for preparing tetra alkyl lead which comprises contacting under reacting conditions, an organic halide with a lead monosodium alloy in the form of small substantially dust-free particles of a uniform size.
2. The process for preparing tetra alkyl lead which comprises contacting under reacting condltions, an organic halide with a lead mono.- sodium alloy in the form of small substantially dust-free particles of a uniform size of about to about $4; inch in diameter.
3. The process for preparing tetraethyl lead which comprises contacting, under reacting conditions, ethyl chloride with a lead mono-sodium alloy in the form of small substantially dustfree particles of a uniform size.
4. The process for preparing tetraethyl lead which comprises contacting, under reacting conditions, ethyl chloride with a lead mono-sodium The yield in alloy in the form of small substantially dust-free particles of a uniform size of about a; to about V inch in diameter.
5. The process for preparing tetra alkyl lead which comprises contacting, under reacting conditions, an organic halide with a lead monosodium alloy in-the form of small uniformly sized crystals of octahedral structure."
6. The process-for preparing tetra alkayl lead which comprises contacting, under reacting conditions, an organic halide with a lead monosodium alloy in the form-of small substantially dust-free crystals of octahedral structure of a uniform size of about to about 56inch in I diameter. d
7. The process for preparing tetra alkyl lead which comprises contacting, under reacting conditions, an organic halide with a lead monosodium alloy in the form of small substantially dust-free crystals of octahedral structure of a uniform size and having their edges rounded off and their surfaces well polished.
8. The process for preparing tetra alkyl lead which comprises contacting, under reacting conditions, an organic halide with a lead monosodium alloy in the form of small substantially dust-free crystals of octahedral structure of a uniform size of about a; to about inch in diameter and having their edges rounded ofi and their surfaces well polished.
9; The process for preparing tetraethyl lead which comprises contacting, under reacting conditions, ethyl chloride with a lead mono-sodium alloy in the form of small substantially dustfree crystals of octahedral structure of a uniform size 10. The process for preparing tetraethyl lead which comprises contacting, under reacting conditions, ethyl chloride witha lead mono-sodium alloy in the form oi small substantially dustfree crystals of octahedral structure of a uniform size of about to about $4; inch in diameter.
11. The process for preparing tetraethyl lead which comprises contacting, under reacting conditions, ethyl chloride with a lead mono-sodium alloy in the form of small substantially dustfree crystals of octahedral structure of a uniform size and having their edges rounded off and their surfaces well polished.
12. The process for preparing tetraethyl lead which comprises contacting, under reacting con-- ditions, ethyl chloride with a lead mono-sodium alloy in the form of small substantially dust-free crystals of octahedral structure of a'uniiorm size of about to about M; inch in diameter and having their edges rounded oil and their surfaces well polished.
LOUIS S. BAKE.
US675089A 1933-06-09 1933-06-09 Process of preparing tetra alkyl lead Expired - Lifetime US2029301A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US675089A US2029301A (en) 1933-06-09 1933-06-09 Process of preparing tetra alkyl lead

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US675089A US2029301A (en) 1933-06-09 1933-06-09 Process of preparing tetra alkyl lead

Publications (1)

Publication Number Publication Date
US2029301A true US2029301A (en) 1936-02-04

Family

ID=24709008

Family Applications (1)

Application Number Title Priority Date Filing Date
US675089A Expired - Lifetime US2029301A (en) 1933-06-09 1933-06-09 Process of preparing tetra alkyl lead

Country Status (1)

Country Link
US (1) US2029301A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2572887A (en) * 1948-05-29 1951-10-30 Stanton Robert Solid-liquid reaction processes
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

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2572887A (en) * 1948-05-29 1951-10-30 Stanton Robert Solid-liquid reaction processes
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

Similar Documents

Publication Publication Date Title
US2745735A (en) Method of producing titanium
US2109005A (en) Preparation of lead-sodium alloys
US2989376A (en) Method of producing pure silicon
US2029301A (en) Process of preparing tetra alkyl lead
US2214211A (en) Process for producing zirconium metal
US2866685A (en) Preparation of lithium nitride
US2378053A (en) Production of iron carbonyl
US2765328A (en) Metals recovery
US3012878A (en) Titanium metal production process
US2816020A (en) Method of producing titanium
US2166917A (en) Process of producing alkoxyl de
US2387203A (en) Method of making beryllium fluoride
US1923570A (en) Production of sodium cyanide
US3006726A (en) Process for upgrading crude alkali metal sulfates
US2768064A (en) Preparation of alkali metal hydrides
US2635107A (en) Manufacture of tetraalkyllead compounds
US2311307A (en) Production of metal carbonyls
US1664021A (en) Process of manufacturing tetra-ethyl lead
US2897056A (en) Production of elemental boron by magnesium reduction
US2069262A (en) Manufacture of chlorinated rubber
US2744003A (en) Process of producing cobalt in fine powder form
GB883721A (en) Improvements in or relating to titanium production
US1929014A (en) Recovery of metallic oxides from ores
US2807539A (en) Process for refining titanium
US1474479A (en) Manufacture of metal chlorides