US2038704A - Recovery of alkyl lead compounds - Google Patents
Recovery of alkyl lead compounds Download PDFInfo
- Publication number
- US2038704A US2038704A US718220A US71822034A US2038704A US 2038704 A US2038704 A US 2038704A US 718220 A US718220 A US 718220A US 71822034 A US71822034 A US 71822034A US 2038704 A US2038704 A US 2038704A
- Authority
- US
- United States
- Prior art keywords
- lead
- mixture
- reaction mass
- steam
- acid
- 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
- -1 alkyl lead compounds Chemical class 0.000 title description 19
- 238000011084 recovery Methods 0.000 title description 6
- 239000000203 mixture Substances 0.000 description 41
- MRMOZBOQVYRSEM-UHFFFAOYSA-N tetraethyllead Chemical compound CC[Pb](CC)(CC)CC MRMOZBOQVYRSEM-UHFFFAOYSA-N 0.000 description 38
- 239000010802 sludge Substances 0.000 description 23
- 239000002253 acid Substances 0.000 description 20
- 238000002156 mixing Methods 0.000 description 20
- 238000004821 distillation Methods 0.000 description 19
- 238000000034 method Methods 0.000 description 19
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 18
- 239000000126 substance Substances 0.000 description 13
- 229910000528 Na alloy Inorganic materials 0.000 description 11
- 238000001256 steam distillation Methods 0.000 description 8
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 6
- 125000000217 alkyl group Chemical group 0.000 description 6
- 150000001875 compounds Chemical class 0.000 description 5
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 4
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 4
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 4
- 235000011130 ammonium sulphate Nutrition 0.000 description 4
- 230000000717 retained effect Effects 0.000 description 4
- 238000009736 wetting Methods 0.000 description 4
- HRYZWHHZPQKTII-UHFFFAOYSA-N chloroethane Chemical compound CCCl HRYZWHHZPQKTII-UHFFFAOYSA-N 0.000 description 3
- 239000002270 dispersing agent Substances 0.000 description 3
- 229960003750 ethyl chloride Drugs 0.000 description 3
- 238000002474 experimental method Methods 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 239000000080 wetting agent Substances 0.000 description 3
- WRIDQFICGBMAFQ-UHFFFAOYSA-N (E)-8-Octadecenoic acid Natural products CCCCCCCCCC=CCCCCCCC(O)=O WRIDQFICGBMAFQ-UHFFFAOYSA-N 0.000 description 2
- LQJBNNIYVWPHFW-UHFFFAOYSA-N 20:1omega9c fatty acid Natural products CCCCCCCCCCC=CCCCCCCCC(O)=O LQJBNNIYVWPHFW-UHFFFAOYSA-N 0.000 description 2
- QSBYPNXLFMSGKH-UHFFFAOYSA-N 9-Heptadecensaeure Natural products CCCCCCCC=CCCCCCCCC(O)=O QSBYPNXLFMSGKH-UHFFFAOYSA-N 0.000 description 2
- FERIUCNNQQJTOY-UHFFFAOYSA-N Butyric acid Chemical compound CCCC(O)=O FERIUCNNQQJTOY-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 239000005642 Oleic acid Substances 0.000 description 2
- ZQPPMHVWECSIRJ-UHFFFAOYSA-N Oleic acid Natural products CCCCCCCCC=CCCCCCCCC(O)=O ZQPPMHVWECSIRJ-UHFFFAOYSA-N 0.000 description 2
- 229910000978 Pb alloy Inorganic materials 0.000 description 2
- WBLCSWMHSXNOPF-UHFFFAOYSA-N [Na].[Pb] Chemical compound [Na].[Pb] WBLCSWMHSXNOPF-UHFFFAOYSA-N 0.000 description 2
- QXJSBBXBKPUZAA-UHFFFAOYSA-N isooleic acid Natural products CCCCCCCC=CCCCCCCCCC(O)=O QXJSBBXBKPUZAA-UHFFFAOYSA-N 0.000 description 2
- 150000002611 lead compounds Chemical class 0.000 description 2
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N oleic acid Chemical compound CCCCCCCC\C=C/CCCCCCCC(O)=O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 description 2
- 229960002969 oleic acid Drugs 0.000 description 2
- 235000021313 oleic acid Nutrition 0.000 description 2
- XNGIFLGASWRNHJ-UHFFFAOYSA-N phthalic acid Chemical compound OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 description 2
- 239000011541 reaction mixture Substances 0.000 description 2
- 239000011780 sodium chloride Substances 0.000 description 2
- USFZMSVCRYTOJT-UHFFFAOYSA-N Ammonium acetate Chemical compound N.CC(O)=O USFZMSVCRYTOJT-UHFFFAOYSA-N 0.000 description 1
- 239000005695 Ammonium acetate Substances 0.000 description 1
- KEAYESYHFKHZAL-UHFFFAOYSA-N Sodium Chemical compound [Na] KEAYESYHFKHZAL-UHFFFAOYSA-N 0.000 description 1
- 235000021355 Stearic acid Nutrition 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- RGCKGOZRHPZPFP-UHFFFAOYSA-N alizarin Chemical compound C1=CC=C2C(=O)C3=C(O)C(O)=CC=C3C(=O)C2=C1 RGCKGOZRHPZPFP-UHFFFAOYSA-N 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 150000001350 alkyl halides Chemical class 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229940043376 ammonium acetate Drugs 0.000 description 1
- 235000019257 ammonium acetate Nutrition 0.000 description 1
- 239000001166 ammonium sulphate Substances 0.000 description 1
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 238000010960 commercial process Methods 0.000 description 1
- 238000010908 decantation Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000011872 intimate mixture Substances 0.000 description 1
- 239000011133 lead Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 1
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000000344 soap Substances 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 239000008117 stearic acid Substances 0.000 description 1
- 150000003460 sulfonic acids Chemical class 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
- a lead monosodium alloy is contacted with an alkyl halide such as ethyl chloride in a reaction chamber.
- the reaction mixture thus obtained comprises an intimate mixture of unreacted lead sodium alloy, sodium chloride, lead and the alkyl lead compound.
- the alkyl lead compound is adsorbed upon the particles of lead. This reaction mixture has the appearance of wet sand from which the alkyl lead compound cannot be removed by any method such as decantation or filtration.
- this reaction mass is introduced into a relatively large volume of water, the mixture agitated and steam passed therethrough to drive off the lead alkyl compounds by steam distillation.
- This method of recovering the alkyl lead from the reaction mass has not proved to be entirely satisfactory for the reason that substantial proportions of the alkyl lead compound remain adsorbed on the lead particles which also tend to agglomerate. This adsorbed and occluded alkyl lead compound cannot be removed by extending the time of the distillation.
- An object of the present invention is to provide a new method for recovering alkyl lead compounds from reaction masses or lead sludges containing the same.
- a still further object is to provide a process whereby almost theoretical recovery of alkyl lead compounds are obtained from Other objects are to advance the art. Still other objects will appear hereinafter.
- the acid reacting substances should be employed in an amount sufiicient to reduce the alkalinity of the reaction mass or sludge to a pH of between 7 and 8.
- smaller amounts of the acid reacting substances may be employed 26 and-we have found that satisfactory results may be obtained when sufiicient of the acid reacting substances is employed to reduce the pH of the reaction mass or sludge to between 7 and 11. It
- the acid reacting substance may be added to the reaction mass at the start of or during the distillation or at the end of a straight steam distillation followed by further distillation to're- 40 move the alkyl lead compound released from the sludge by coagulation of the lead.
- Example 1 100 parts of a reaction mass, obtained by reacting ethyl chloride with monosodium lead alloy, was added to 300 parts of water and the mixture distilled with steam in the usual manner. Upon analysis, it was found that 8.4 parts or 8.4% of tetra ethyl lead remained in the lead sludge. es
- Example 2 100 parts of a reaction mass, similar to that treated in Example 1, was added to 300 parts of water containing 0.2 part of Turkey red oil: This mixture was then subjected to steam distillation in the usual manner. Upon analysis, it was found that 3.2- parts or 3.2% of tetra ethyl lead was retained by the sludge.
- Example 3 100 parts of a reaction mass, similar to that treated in Example 1, was added to 300 parts of water. Dilute sulfuric acid was added to the resulting mixture in an amount suflicient to reduce the pH of the mixture to 7.5. The resulting mixture was subjected to steam distillation in the same manner as in Examples 1 and 2. After distillation, it was found that only 0.16 part or 0.16% of tetra ethyl lead remained in the lead sludge.
- Example 4 100 parts of a reaction mass, similar to that treated in Example 1, was added to 300 parts of water. To the resulting mixture, was added sulfuric acid inan amount sufiicient to reduce the pH to'9.3. 'This mixture was then subjected to steam distillation as in the preceding examples.
- Example5 The experiment of Example 3 was repeated except that ammonium sulfate was employed in place of the sulfuric acid. As a result, 0.19% of 1 tetra ethyl lead was retained in the sludge.
- Example 4 The experiment of Example 4 was repeated employing ammonium sulfate in place of the sulfuric acid.
- Example 8 The experiment of Example 7 was repeated employing a smaller amount of. acetic acid so that the pH of the mixture was reduced to only 9.3. After distillation, 0.42% tetraethyl lead was found to have been retained by the lead sludge.
- Example 9 c A reaction mass, obtained by reacting ethyl chloride with monosodium lead alloy, was subjected to a steam distillation. After distillation, it was, found that the still residue or lead sludge contained 2.9% of tetraethyl lead. 100 parts of this still residue or sludge was redistilled. After such redistillation,'2.7% of tetraethyl lead was found in the sludge. Another 100 parts of the still residue or sludge, containing 2.9% of tetra ethyl lead, was slightly acidified with sulfuric acid and then redistilled with the removal of all but 0.09% of the tetra ethyl lead from the sludge.
- the acid reacting substances may be employed either with or without wetting and dispersing agents.
- 'an alkyl lead reaction mass may be added to water and then the pH of the mixture adjusted by means of the acid substances or the reaction mass may be added to water containing wetting and dispersing agents such as are disclosed in Patent 1,645,375 issued to Daudt et al. and the copending application of Downing,
- the process of recovering tetra alkyl lead from a reaction mass containing the same and unreacted lead-sodium alloy which comprises mixing the reaction mass with water, steam distilling the mixture, mixing with the distillation residue an acid reacting compound sufficient in amount to materially redu'ce the alkalinity of the mixture to a pH of not lower than 7.0 and then'redistilling the partially neutralized mixture with steam.
- the processor recovering tetra ethyl lead from a reaction mass containing the same and mixing the reaction mass with water, steam dis- 'tilling, the mixture, mixing with the distillation residue sulfuric acid sufficient in amount to materially reduce the alkalinity of the mixture to a pH of not lower than 7.0 and then redistilling the partially neutralized mixture with steam.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
the reaction masses.
Patented Apr. 28, 1936 RECOVERY OF ALKYL LEAD COMPOUNDS Louis S. Bake, Pennsgrove, and Alfred E. Parmelee, Carneys Point, N. J., assignors to E. L du Pont de Nemours & Company, Wilmington, DeL, a corporation of Delaware No Drawing. Application March 30, 1934,
- Serial No. 718,220
12 Claims.
manufacturing alkyl lead compounds and par-- ticularly tetra ethyl lead, a lead monosodium alloy is contacted with an alkyl halide such as ethyl chloride in a reaction chamber. The reaction mixture thus obtained comprises an intimate mixture of unreacted lead sodium alloy, sodium chloride, lead and the alkyl lead compound. There is 2 to 3 times as much solid material comprising sodium chloride, lead and unreacted lead-sodium alloy as there are alkyl lead compounds. The alkyl lead compound is adsorbed upon the particles of lead. This reaction mixture has the appearance of wet sand from which the alkyl lead compound cannot be removed by any method such as decantation or filtration.
In the commercial process, this reaction mass is introduced into a relatively large volume of water, the mixture agitated and steam passed therethrough to drive off the lead alkyl compounds by steam distillation. This method of recovering the alkyl lead from the reaction mass has not proved to be entirely satisfactory for the reason that substantial proportions of the alkyl lead compound remain adsorbed on the lead particles which also tend to agglomerate. This adsorbed and occluded alkyl lead compound cannot be removed by extending the time of the distillation.
In order to improve the recovery of the lead alkyl compound from the reaction mass it has been proposed to add, to the reaction mass in the still, wetting and dispersing agents which prevent agglomeration of the lead in the mass and permit a more complete recovery of the alkyl lead compound. While this latter process has proved to be very successful in operation, it has been found that substantial amounts of the alkyl lead compounds are not removed from the reaction mass but remain adsorbed upon the particles of lead. The lead sludge remaining from such a process will normally contain from 1 to 4% of the alkyl lead compound adsorbed on the lead.
An object of the present invention is to provide a new method for recovering alkyl lead compounds from reaction masses or lead sludges containing the same. A still further object is to provide a process whereby almost theoretical recovery of alkyl lead compounds are obtained from Other objects are to advance the art. Still other objects will appear hereinafter.
These objects may be accomplished in accordance with our invention which comprises neutralizing either wholly or partially the alkali in the 5 reaction mass or lead sludge and then distilling by steam in accordance with the usual process.
We have found that, when an acid reacting substance is added to a reaction mass or lead sludge, containing alkyl lead compounds, in such 10 amounts that the alkalinity of the reaction mass or sludge is reduced to a pH of not lower than 7 and then the reaction mass or lead sludge is subjected to steam distillation in accordance with the usual custom, almost theoretical recovery of 15 the organic lead compound is obtained. Among the acid reacting substances which we have found to operate most satisfactory for our purposes are sulfuric acid, acetic acid, phthalic acid, ammonium sulphate, ammonium acetate and the like. 20
Preferably, the acid reacting substances should be employed in an amount sufiicient to reduce the alkalinity of the reaction mass or sludge to a pH of between 7 and 8. However, smaller amounts of the acid reacting substances may be employed 26 and-we have found that satisfactory results may be obtained when sufiicient of the acid reacting substances is employed to reduce the pH of the reaction mass or sludge to between 7 and 11. It
is undesirable to reduce the pH of the reaction 30 mass or sludge to below 7.0 as the excess acid tends to decompose the alkyl lead compounds although complete removal of the alkyl lead compound from the reaction mass or lead sludge may be obtained by employing excess of the acid reacting substance.
The acid reacting substance may be added to the reaction mass at the start of or during the distillation or at the end of a straight steam distillation followed by further distillation to're- 40 move the alkyl lead compound released from the sludge by coagulation of the lead.
In order to more clearly illustrate our invention, the preferred mode of carrying the same into efiectand the advantageous results to be obtained thereby, the following examples are given:
Example 1 100 parts of a reaction mass, obtained by reacting ethyl chloride with monosodium lead alloy, was added to 300 parts of water and the mixture distilled with steam in the usual manner. Upon analysis, it was found that 8.4 parts or 8.4% of tetra ethyl lead remained in the lead sludge. es
Example 2 100 parts of a reaction mass, similar to that treated in Example 1, was added to 300 parts of water containing 0.2 part of Turkey red oil: This mixture was then subjected to steam distillation in the usual manner. Upon analysis, it was found that 3.2- parts or 3.2% of tetra ethyl lead was retained by the sludge.
Example 3 100 parts of a reaction mass, similar to that treated in Example 1, was added to 300 parts of water. Dilute sulfuric acid was added to the resulting mixture in an amount suflicient to reduce the pH of the mixture to 7.5. The resulting mixture was subjected to steam distillation in the same manner as in Examples 1 and 2. After distillation, it was found that only 0.16 part or 0.16% of tetra ethyl lead remained in the lead sludge.
' Example 4 100 parts of a reaction mass, similar to that treated in Example 1, was added to 300 parts of water. To the resulting mixture, was added sulfuric acid inan amount sufiicient to reduce the pH to'9.3. 'This mixture was then subjected to steam distillation as in the preceding examples.
After such distillation, it was found that the lead sludge retained 0.35% of tetra ethyl lead.
Erample5 The experiment of Example 3 was repeated except that ammonium sulfate was employed in place of the sulfuric acid. As a result, 0.19% of 1 tetra ethyl lead was retained in the sludge.
. Egample 6 The experiment of Example 4 was repeated employing ammonium sulfate in place of the sulfuric acid. The lead sludge, remaining after the distillation, contained 0.26% tetraethyl lead.
Example 7 parts of a reaction mass, similar to that treated in Example 1, was added to 300 parts of water. Acetic acidwas then added to the resulting mixture until the pH was reduced to 7.5 and the resulting mixture subjected to steam distillation in the usual manner. After distillation, .it was found that0.17% of tetraethyl'lead remained in the sludge.
Example 8 The experiment of Example 7 was repeated employing a smaller amount of. acetic acid so that the pH of the mixture was reduced to only 9.3. After distillation, 0.42% tetraethyl lead was found to have been retained by the lead sludge.
Example 9 c A reaction mass, obtained by reacting ethyl chloride with monosodium lead alloy, was subjected to a steam distillation. After distillation, it was, found that the still residue or lead sludge contained 2.9% of tetraethyl lead. 100 parts of this still residue or sludge was redistilled. After such redistillation,'2.7% of tetraethyl lead was found in the sludge. Another 100 parts of the still residue or sludge, containing 2.9% of tetra ethyl lead, was slightly acidified with sulfuric acid and then redistilled with the removal of all but 0.09% of the tetra ethyl lead from the sludge.
From the above examples, it will be apparent that the acid reacting substances and the amounts thereof employed may be rather widely varied. Other acid reacting substances which may be mentioned are hydrochloric acid, butyric acid, oleic acid, stearic acid, sulfonic acids and the like.
The acid reacting substances may be employed either with or without wetting and dispersing agents. For example, 'an alkyl lead reaction mass may be added to water and then the pH of the mixture adjusted by means of the acid substances or the reaction mass may be added to water containing wetting and dispersing agents such as are disclosed in Patent 1,645,375 issued to Daudt et al. and the copending application of Downing,
Parmelee, Pedersen and Stecher, Serial No.
597,800 filed on or about March 9,: 1932 and the pH adjusted by adding an acid substance. In
other words, the processes disclosed in the aforesaid patent and application may be employed modifying them by adding acid substances in accordance with our invention. Among the wetting a'nd di'spersingagents disclosed by Daudt of oleicacid and aliphatic diamines, the higher fatty and unsaturated acid and their soaps, resinates, and the like which may be employed in ,our process.
From the foregoing description of our inventionit will be readily apparent to those skilled in the .art that many changes and modifications may be made in the process and the ingredients employed without departing from the spirit of our invention. Accordingly, the scope of our invention is to be limited solely by the appended claims construed as broadly as is permissible in view of the prior art.
We claim:
l. The process of recovering tetra alkyl lead from a reaction mass containing the same and unreacted lead-sodium alloy which comprises mixing the reaction mass with water, steam distilling the mixture, mixing with the distillation residue an acid reacting compound sufficient in amount to materially redu'ce the alkalinity of the mixture to a pH of not lower than 7.0 and then'redistilling the partially neutralized mixture with steam.
2. The process of recovering tetra alkyl lead from a reaction mass containing the same and unreacted lead-sodium alloy which comprises mixing the reaction mass with water, steam distilling the mixture, mixing with the distillation residue an acid reacting compound suflicient in amount to materially reduce the alkalinity of the mixture to a pH of between about 11 and 7.0 and then redistilling the mixture with steam.
3. The process of recovering tetra alkyl lead from a reaction mass containing the same and unreacted lead-sodium alloy which comprises mixing the reaction mass with water, steam distilling the mixture, mixing with the distillation residue an acid reacting compound suflicient in amount to materially reduce the alkalinity of themixtureto apHoibetweenabout8and7.0 and then redistilling the mixture with steam.
4. The process of recovering tetra ethyl lead from a reaction mass containing the same and unreacted lead-sodium alloy which comprises mixing the reaction mass with water, steam distilling the mixture, mixing with the distillation residue an acid reacting compound suilicient in amount to materially reduce the alkalinity of the mixture to a pH of not lower than 7.0 and then redistilling the partially neutralized mixture with steam. Y
5. The process of recovering tetra ethyl lead from a reaction mass containing the same and unreacted lead-sodium alloy which comprises mixing the reaction mass with water, steam distilling the mixture, mixing with the distillation residue an acid reacting compound suiiicient in amount to materially reduce the alkalinityof the mixture to a pH of between about 11 and 7.0 and then redistilling the mixture with steam.
6. The processor recovering tetra ethyl lead from a reaction mass containing the same and mixing the reaction mass with water, steam dis- 'tilling, the mixture, mixing with the distillation residue sulfuric acid sufficient in amount to materially reduce the alkalinity of the mixture to a pH of not lower than 7.0 and then redistilling the partially neutralized mixture with steam.
8. The process of recovering tetra ethyl lead from a reaction mass containing the same and unreacted lead-sodium alloy which comprises mixing the reaction mass with water, steam distilling the mixture, mixing with the distillation residue sulfuric acid suflicient in amount to materially reduce the alkalinity of the mixture to a pH 01' between about 11 and 7.0 and then redistilling the mixture withsteam.
9. The process of recovering tetra ethyl lead from a reaction mass containing the same and unreacted lead-sodium alloy which comprises mixing the reaction mass with water, steam distilling the mixture, mixing with the distillation residue sulfuric acid suihcient in amount to materially reduce the alkalinity of the mixture to a pH of between about 8 and 7.0 and then redistilling the mixture with steam.-
10. The process of recovering tetra ethyl lead from a reaction mass containingthe same and unreacted lead-sodium alloy which comprises mixing the reaction mass with water, steam distilling the mixture, mixing with the distillation residue ammonium sulfate suflicient in amount to materially reduce the alkalinity of the mixture to a pH of between about 11 and 7.0 and then redistilling the mixture with steam.
11. The process of recovering tetra ethyl lead from a reaction mass containing the same and unreacted lead-sodium alloy whichcomprises mixing the reaction masswith water, steam distilling the mixture, mixing with the distillation residue a carboxylic acid sufiicient in amount to materially reduce the alkalinity of the mixture to a pH of between about 11 and 7.0 and then a pH of between about 11 and 7.0 and then re-- distilling the mixture with steam.
1 LOUIS S. BAKE.
ALFRED E. PARMELEE.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US718220A US2038704A (en) | 1934-03-30 | 1934-03-30 | Recovery of alkyl lead compounds |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US718220A US2038704A (en) | 1934-03-30 | 1934-03-30 | Recovery of alkyl lead compounds |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2038704A true US2038704A (en) | 1936-04-28 |
Family
ID=24885266
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US718220A Expired - Lifetime US2038704A (en) | 1934-03-30 | 1934-03-30 | Recovery of alkyl lead compounds |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2038704A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2513659A (en) * | 1948-11-16 | 1950-07-04 | Ethyl Corp | Recovery of alkyllead |
| US2513654A (en) * | 1948-11-16 | 1950-07-04 | Ethyl Corp | Recovery of alkyllead compounds |
| US2622093A (en) * | 1951-05-23 | 1952-12-16 | Ethyl Corp | Recovery of tetraalkyllead compounds |
| US2686799A (en) * | 1952-02-19 | 1954-08-17 | Du Pont | Process for making tetraethyl lead |
| US2777866A (en) * | 1953-08-17 | 1957-01-15 | Ethyl Corp | Recovery of tetraalkyl-lead compounds |
-
1934
- 1934-03-30 US US718220A patent/US2038704A/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2513659A (en) * | 1948-11-16 | 1950-07-04 | Ethyl Corp | Recovery of alkyllead |
| US2513654A (en) * | 1948-11-16 | 1950-07-04 | Ethyl Corp | Recovery of alkyllead compounds |
| US2622093A (en) * | 1951-05-23 | 1952-12-16 | Ethyl Corp | Recovery of tetraalkyllead compounds |
| US2686799A (en) * | 1952-02-19 | 1954-08-17 | Du Pont | Process for making tetraethyl lead |
| US2777866A (en) * | 1953-08-17 | 1957-01-15 | Ethyl Corp | Recovery of tetraalkyl-lead compounds |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US2038704A (en) | Recovery of alkyl lead compounds | |
| US2664437A (en) | O-(2-chloro-4-nitrophenyl) o,o dimethyl thiophosphate | |
| US2038703A (en) | Recovery of alkyl lead compounds from their reaction masses | |
| US2004160A (en) | Tetra alkyl lead | |
| US2046242A (en) | Process for preventing the detrimental formation of lime and magnesia soaps | |
| US3322814A (en) | Purification of nitriles | |
| US3328458A (en) | Purification of nitriles | |
| DE1817918C3 (en) | Ester of 1.7.7-trimethyl-bicyclo- [4.4.0] -decanols- (3) | |
| US2623882A (en) | Process for the manufacture of addition products of hydrocyanic acid and acrylic acid nitrile | |
| US2811549A (en) | Process of preparing high solids beta-alanine detergents | |
| DE3714602A1 (en) | Process for the preparation of 2,3,5,6-tetrafluorobenzyl alcohols | |
| US1975171A (en) | Process of purifying tetra alkyl lead | |
| US3547975A (en) | Process for the hydrodimerization of acrylic acid derivatives | |
| US2405894A (en) | Compounds | |
| US2569425A (en) | Methoxy-ethyl esters of imido acids | |
| US2405842A (en) | Method of making diallyl | |
| US2513654A (en) | Recovery of alkyllead compounds | |
| DE872941C (en) | Process for the production of unsaturated nitriles | |
| US2513659A (en) | Recovery of alkyllead | |
| US2748151A (en) | Purification of acid chlorides | |
| DE633344C (en) | Process for the preparation of diacyldiaminodiphenylselenides | |
| US2266036A (en) | Method of treating oils and product | |
| US2382548A (en) | Esters and method of preparing the same | |
| US1979254A (en) | Lead-sodium alloy | |
| DE1197075B (en) | Process for the production of cyanformamide |