US2029301A - Process of preparing tetra alkyl lead - Google Patents
Process of preparing tetra alkyl lead Download PDFInfo
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- 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
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- United States
- Prior art keywords
- alloy
- lead
- particles
- preparing
- stirring
- Prior art date
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- Expired - Lifetime
Links
- 238000000034 method Methods 0.000 title description 14
- 125000000217 alkyl group Chemical group 0.000 title description 8
- 229910045601 alloy Inorganic materials 0.000 description 49
- 239000000956 alloy Substances 0.000 description 49
- 239000002245 particle Substances 0.000 description 24
- KEAYESYHFKHZAL-UHFFFAOYSA-N Sodium Chemical compound [Na] KEAYESYHFKHZAL-UHFFFAOYSA-N 0.000 description 18
- MRMOZBOQVYRSEM-UHFFFAOYSA-N tetraethyllead Chemical compound CC[Pb](CC)(CC)CC MRMOZBOQVYRSEM-UHFFFAOYSA-N 0.000 description 18
- 238000003756 stirring Methods 0.000 description 16
- 239000013078 crystal Substances 0.000 description 15
- 229910000528 Na alloy Inorganic materials 0.000 description 14
- HRYZWHHZPQKTII-UHFFFAOYSA-N chloroethane Chemical compound CCCl HRYZWHHZPQKTII-UHFFFAOYSA-N 0.000 description 13
- 229960003750 ethyl chloride Drugs 0.000 description 13
- 238000004519 manufacturing process Methods 0.000 description 13
- 238000006243 chemical reaction Methods 0.000 description 7
- 238000000227 grinding Methods 0.000 description 7
- 150000004820 halides Chemical class 0.000 description 7
- -1 alkyl lead compounds Chemical class 0.000 description 6
- 239000000428 dust Substances 0.000 description 6
- 238000007873 sieving Methods 0.000 description 6
- 238000001816 cooling Methods 0.000 description 4
- 238000000354 decomposition reaction Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000011261 inert gas Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 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
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- 238000013019 agitation Methods 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
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing 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
- 150000002611 lead compounds Chemical class 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
- 235000011121 sodium hydroxide Nutrition 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
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.
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- 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.
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)
| 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 |
-
1933
- 1933-06-09 US US675089A patent/US2029301A/en not_active Expired - Lifetime
Cited By (3)
| 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 |
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