US1723724A - Process of making ketene - Google Patents

Process of making ketene Download PDF

Info

Publication number
US1723724A
US1723724A US269863A US26986328A US1723724A US 1723724 A US1723724 A US 1723724A US 269863 A US269863 A US 269863A US 26986328 A US26986328 A US 26986328A US 1723724 A US1723724 A US 1723724A
Authority
US
United States
Prior art keywords
ketene
temperature
network
chamber
vapors
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
US269863A
Inventor
Hans T Clarke
Charles E Waring
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.)
Eastman Kodak Co
Original Assignee
Eastman Kodak 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 Eastman Kodak Co filed Critical Eastman Kodak Co
Priority to US269863A priority Critical patent/US1723724A/en
Application granted granted Critical
Publication of US1723724A publication Critical patent/US1723724A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C45/00Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
    • C07C45/87Preparation of ketenes or dimeric ketenes
    • C07C45/88Preparation of ketenes or dimeric ketenes from ketones

Definitions

  • This invention relates to processes for the manufacture of ketene.
  • One object of the invention is to provide a process in which compounds convertible into ketene may be so converted without undue decomposition.
  • Another object of the invention is to provide a process in which the heat is efiiciently and economically transferred to the vapors to be converted.
  • a further object is to insure that all particles of the vapor reach the required decomposition temperature.
  • Still another object is to maintain the said vapors of the compound, to be decomposed into ketene, at a specified temperature for the optimum reaction period.
  • the number of metals. that can replace copper are necessarily limited. They should have a higher melting point than the operating temperature used and should be free from iron or other metals that promote the breaking down of the ketene. Metals other than iron and nickel having a melting point. above 700 C. and a coeflicient of heat conductivity of more than .150 C. G. S. system, may be used. We have found that copper, its alloys,
  • the time of contact of the starting material at the operating temperature is offirst importance,over-exposure at this temperature will greatly decrease the useful yield and under-exposure will permit an unnecessarily large proportion of the star-ting material to pass through the combustion chamber unchanged, the optimum time of contact for acetone vapor in the heated zone being not more than five seconds.
  • Acetone is vaporized by boiling at a predetermined rate, and the vapor is passed into the copper reaction tube having a diameter of the order of a half inch or more, filled with copper turnings, and heated to 650670 C.
  • the acetone vapor is conducted into the reaction chamber at such a rate that the acetone is at the optimum temperature, during a period of time less than five seconds.
  • the unchanged acetone is condensed and returned to the boiling vessel, and the gaseous reaction products are condensed or absorbed in any desired manner. After about eight hours operation a yield of approximately 80% is realized.
  • ketene which comprises passing the vapors of organic compounds which are decomposed by ieat into substances including ketene through a chamber having therein a network of metal which is free from iron and nickel, said metal having high thermal conductivity and a melting point above the reaction temperature.
  • ketene which comprises passing the Vapors of organic compounds which are decomposed by heat into substances including ketene through a chamber having therein a network of metal which is free from iron and nickel, said metal having a melting point above 700 C. and a coefiicient of heat conductivity greater than .150, C. G. S. units.
  • ketene which comprises passing the vapors of acetone through a chamber having therein a network of metal which is free from iron and nickel, said metal having a melting point above 700 C. and a cocflicient of heat conductivity greater than .150 C. G. units.
  • ketene which comprises passing the vapors of organic compounds which are decomposed by heat into substances including ketene through a chamber having therein a network of metal which is free from iron and nickel, said metal having a melting point above 700 C. and a coefficient of heat conductivity greater than .150 C. G. S. units, maintaining said chamber at a temperature of 650-670? (1., the period of contact of the vapor with the network being less than five seconds.
  • ketene which comprises passing the vapors of acctone through a chamber containing a network of copper, said chamber and copper being free from iron and nickel.
  • the PlOCeiS of manufacturing ketene which comprises passing the vapors of acetone through a chamber containing a network of copper, at a temperature of 650-670 (1, said chamber and network bein free of nickel and iron.
  • ketene which comprises passing the vapors of acetone through a chamber containing a network of copper, at a temperature of 650-670 0., said chamber and network being free of nickel and iron, the period of contact between the vapors and network being less than five seconds.
  • ketene which comprises passing the vapors of acetone through a copper chamber containing a network of copper, said chamber and network being free of nickel and iron, at a temperature of 650670 C., the period of said passage being less than five seconds.

Description

Patented Aug. 6, 1929.
UNITED STATES 1,723,724 PATENT OFFICE.
HANS T. CLARKE AND CHARLES E. WAIEING, OF ROCHESTER, NEW YORK, ASSIGNORS TO EASTMAN KODAK COMPANY, OF ROCHESTER, NEW YORK, A CORPORATION OF NEW YORK.
PROCESS OF MAKING KETENE.
No Drawing.
' This invention relates to processes for the manufacture of ketene. One object of the invention is to provide a process in which compounds convertible into ketene may be so converted without undue decomposition.
Another object of the invention is to provide a process in which the heat is efiiciently and economically transferred to the vapors to be converted. A further object is to insure that all particles of the vapor reach the required decomposition temperature. Still another object is to maintain the said vapors of the compound, to be decomposed into ketene, at a specified temperature for the optimum reaction period. Other objects will hereinafter appear.
It was shown in 1910 by Schmidlin and Bergmann (Berichte der Deutschen Chemischen Gesellschaft, vol. 43, p. 2821) that acetone vapor, when passed through a combustion tube, reacted to form ketene. Hurd and Cochran, J. Amer. Chem. Soc. 45, page 515, 1923, repeated the work of Schmidlin and Bergmann, using a combustion tube filled with brocken porcelain and obtained, at a temperature of 600 C., slightly less than 11% of available ketene. These and other investigators believed that a much larger amount of ketene had been initially formed and subsequently decomposed, as they found the resulting decomposition products, ethylene and carbon monoxide in considerable quantities.
D. A. Nightingale in U. S. Patent No. 1,602,699, describes the use of a preventive catalyst, which counteracts the degenerative decomposition, noted above. He was enabled by the use of this cataylst and a temperature of between 600 C. and 675 C. to obtain a yield of more than 80% of the theoretical amount of ketene,-while without his catalyst less than 20% was produced.
From the prior work it would, therefore, be supposed that the essential procedure to be followed in order to realize a high yield in manufacturing ketene comprises accurate temperature control, and the use of some preventive catalyst. We have found, on the other hand, that the catalyst is not necessary. The precautionary measures of excluding mote the egenerative decomposition, and also of insuring the optimum time, of contactat the correct operating temperature will resalt in an equally high yield.
Application filed April 13,
from the apparatus certain metals that prov 1928. Serial No. 269,863.
In our investigation of this subject, it was determined that certain metals apparently catalyze an entirely different reaction in which carbon is deposited in large quantities and the yield of ketene is enormously dccreased if not completely inhibited. Certain metals, such as iron or nickel, or their salts. if present even in minute quantities, cause a very marked reduction in the yield.
The previous work on the manufacture of ketene has been carried out on a laboratory scale in which combustion tubes of small diameter have been used. In working on a semi-production basis employing larger tubes we found that the percentage of c'onversion was considerably decreased with a large quantity of the starting material appearing in the final product unchanged. \Ve were then using, as a filling material for the combustion tubes, an inert material which had been leached with nitric and hydrochloric acids to remove all traces of the decomposing catalysts. It was evident that all points within the combustion tube were not at the correct reaction temperature, the center, naturally, being cooler than the wall. 'VVc found that by packing the combustion tube with fragments or turnings of a good heat conductor, such as copper, we were able to bring the efficiency to a much higher value.
The effect of using copper as a filling material does not increase the percentage yield but, because of its excellent heat conductivity, raises the temperature of the vapors quickly to the reaction temperature. This prevents undue degenerative decomposition of the ketene which results when the kctene is retained at the operating heat for any appreciable time. i
The number of metals. that can replace copper are necessarily limited. They should have a higher melting point than the operating temperature used and should be free from iron or other metals that promote the breaking down of the ketene. Metals other than iron and nickel having a melting point. above 700 C. and a coeflicient of heat conductivity of more than .150 C. G. S. system, may be used. We have found that copper, its alloys,
brass, bronze, and the like, and silver, work entirely satisfactorily.
The time of contact of the starting material at the operating temperature is offirst importance,over-exposure at this temperature will greatly decrease the useful yield and under-exposure will permit an unnecessarily large proportion of the star-ting material to pass through the combustion chamber unchanged, the optimum time of contact for acetone vapor in the heated zone being not more than five seconds.
We shall now describe our invention by way of example, but it will be understood that the invention is not limited to the details thus given, except as indicated in the appended claims.
Acetone is vaporized by boiling at a predetermined rate, and the vapor is passed into the copper reaction tube having a diameter of the order of a half inch or more, filled with copper turnings, and heated to 650670 C. The acetone vapor is conducted into the reaction chamber at such a rate that the acetone is at the optimum temperature, during a period of time less than five seconds. The unchanged acetone is condensed and returned to the boiling vessel, and the gaseous reaction products are condensed or absorbed in any desired manner. After about eight hours operation a yield of approximately 80% is realized.
It is to be understood that while we have described the use of metal filings or turnings as our preferred filler, other forms may be used giving an equivalent cellular effect, that is, providing a considerable area of unimpeded air space with comparatively thin walls or masses of heat conductive material in a sponge or network throughout the space.
Having thus described our invention, what we claim as new and desire to secure by Letters Patent is:
1. The method of manufacturing ketene which comprises passing the vapors of organic compounds which are decomposed by ieat into substances including ketene through a chamber having therein a network of metal which is free from iron and nickel, said metal having high thermal conductivity and a melting point above the reaction temperature.
2. The method of manufacturing ketene which comprises passing the Vapors of organic compounds which are decomposed by heat into substances including ketene through a chamber having therein a network of metal which is free from iron and nickel, said metal having a melting point above 700 C. and a coefiicient of heat conductivity greater than .150, C. G. S. units.
3. The method of manufacturing ketene which comprises passing the vapors of acetone through a chamber having therein a network of metal which is free from iron and nickel, said metal having a melting point above 700 C. and a cocflicient of heat conductivity greater than .150 C. G. units.
4. The method of manufacturing ketene which comprises passing the vapors of organic compounds which are decomposed by heat into substances including ketene through a chamber having therein a network of metal which is free from iron and nickel, said metal having a melting point above 700 C. and a coefficient of heat conductivity greater than .150 C. G. S. units, maintaining said chamber at a temperature of 650-670? (1., the period of contact of the vapor with the network being less than five seconds.
5. The process of manufacturing ketene which comprises passing the vapors of acctone through a chamber containing a network of copper, said chamber and copper being free from iron and nickel.
6. The PlOCeiS of manufacturing ketene which comprises passing the vapors of acetone through a chamber containing a network of copper, at a temperature of 650-670 (1, said chamber and network bein free of nickel and iron.
7. The process of manufacturing ketene which comprises passing the vapors of acetone through a chamber containing a network of copper, at a temperature of 650-670 0., said chamber and network being free of nickel and iron, the period of contact between the vapors and network being less than five seconds.
8. The process of manufacturing ketene which comprises passing the vapors of acetone through a copper chamber containing a network of copper, said chamber and network being free of nickel and iron, at a temperature of 650670 C., the period of said passage being less than five seconds.
Signed at Rochester, New York, this 9 day of April, 1928.
HANS T. CLARKE. CHARLES E. VVARING.
US269863A 1928-04-13 1928-04-13 Process of making ketene Expired - Lifetime US1723724A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US269863A US1723724A (en) 1928-04-13 1928-04-13 Process of making ketene

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US269863A US1723724A (en) 1928-04-13 1928-04-13 Process of making ketene

Publications (1)

Publication Number Publication Date
US1723724A true US1723724A (en) 1929-08-06

Family

ID=23028962

Family Applications (1)

Application Number Title Priority Date Filing Date
US269863A Expired - Lifetime US1723724A (en) 1928-04-13 1928-04-13 Process of making ketene

Country Status (1)

Country Link
US (1) US1723724A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5475144A (en) * 1994-06-08 1995-12-12 The University Of Delaware Catalyst and process for synthesis of ketenes from carboxylic acids

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5475144A (en) * 1994-06-08 1995-12-12 The University Of Delaware Catalyst and process for synthesis of ketenes from carboxylic acids

Similar Documents

Publication Publication Date Title
DE842055C (en) Process for the preparation of organic silicon halides
Finch et al. Diboron tetrafluoride
DE1132098B (en) Process for the production of phosphides or arsenides of the elements boron, aluminum, gallium, indium from the ó¾. Group of the periodic table
US2294383A (en) Process for the preparation of
US2300969A (en) Production of alkinols
US2765270A (en) Alkali titanium halide compositions
US1723724A (en) Process of making ketene
Mackay et al. Germyl and digermanyl halides
US2419198A (en) Process for dehydrohalogenating halogenated organic compounds
Belchetz The thermal catalytic decomposition of methane
US1418448A (en) Manufacture of butyric aldehyde
US2381001A (en) Method of preparing tetrachloroethylene and chlorosilanes
Glazebrook et al. 134. The photochemical decomposition of aromatic ketones: the phenyl radical
US3230264A (en) Reaction of carbonyl fluoride with fluorine
Korolkov et al. Metal solid solutions obtained by thermolysis of Pt and Re salts. Crystal structure of [Pt (NH 3) 4](ReO 4) 2
US2080562A (en) Process for the production of ketene
Willhoft The importance of defects in nickel on the catalytic dehydrogenation of formic acid at low pressures
US2036410A (en) Process of making styrene
US3216797A (en) Preparation of boron compounds
US2929678A (en) Method of producing zinc selenide
US3088807A (en) Production of pure phosphorus
US2574077A (en) 4,6-ditertiary-butyl-2-methylcyclohexanol
US1375345A (en) Method of producing catalyzers
US1360312A (en) Process of making carbonyl chlorid
Taylor et al. The adsorption of hydrogen and of carbon monoxide on a surface of zinc and molybdenum oxides