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Publication numberUS2235561 A
Publication typeGrant
Publication dateMar 18, 1941
Filing dateMar 5, 1937
Priority dateMar 5, 1937
Publication numberUS 2235561 A, US 2235561A, US-A-2235561, US2235561 A, US2235561A
InventorsCarl J Malm, Gale F Nadeau
Original AssigneeEastman Kodak Co
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Process for the manufacture of methyl ketene and propionic anhydride
US 2235561 A
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Description  (OCR text may contain errors)

Patented Mar. 18, .1941

UNITED STATES PATENT OFFICE METHYL KETENE ANHYDBIDE MANUFACTURE OF AND rnoriomo Gale r. Nadeau and-Carl r. Malm, Rochester, 1 N. Y., assignors to Eastman Kodak Company, Rochester, N. Y.,a corporation New Jersey Application March 5, 1937, Serial No. 129,242

90laims.

the present time produced from propyl alcohol,

pyroligneous liquor or synthetically and the acids may be subsequently converted to the anhydrides.

We have found a novel method for the manufacture of propionic acid and anhydride which is M highly desirable because of its adaptation to the treatment of readily available commercial ma.- terlals.

This invention has for an object to provide a process for producing organic acids and organic acid anhydrides. A still further object is and proplonic anhydride. A still further object is to provide a process for producing propionic acid and anhydrides involving simple pyrolysis. A still further object is to provide a process for the production of organic acids and organic acid anhydrides utilizing ketonic starting materials. Still another object is to provide a process for converting unstable pyrolysis products into acids- 0 and anhydrides. A still further object is to provide a process for the pyrolysis of the higher ketones suchas methyl ethyl ketone. Still another object is to provide a method for sep arating acids and anhydrides by means of ke- 35 tenes. Other objects will appear hereinafter.

There is available commercially as a solvent an organic chemical material comprising methyl ethyl ketone. We have found that this compound, by means of our novel process, consti- 40 tutes a source of propionic acid and anhydride.

Some work has been done on the pyrolysis of simple ketones' such as the pyrolysis of acetone to ketene. Schmidlin, Berglin, Hurd, Cochrane, Nightingale, Clarke and Waring (see U. S.

45 3. Rice, law and others describe the Pyrolysis of acetone to ketene. Some mention is made in the art relative to the pyrolysis of methyl ethyl ketone but one investigator states to the eifct that when methyl ethyl kctone is pyrolized '50 at 600 C., only ketene is formed in small yields;

to provide a process for producing propionic-acid (or. 260-546) hence, it was concluded that methyl ethyl ketone is not superior to. acetone. Also, the aforementioned investigators and others have de scribed various procedures for treating acetone pyrolysis products. Some condense the products directly, others indicate that condensation should be omitted.

We have found after considerable investigation relative to the treatment of higher ketonic materials, that by our process, methyl ethyl ketone, may be passed through a reaction chamber heated to a temperature of 500-800 C., and under other proper conditions, where it is decomposed to a mixtiu econtaining methyl ketene and certain other gaseous products. When the products of the reaction are passed into warm acetic acid, any ketene forms acetic anhydride with the acetic acid and the methyl ketene forms with the acid, a mixture of propionic anhydride and acetopropionic anhydride. Upon distillation of the mixture, one obtains first, acetic acid, then acetic anhydride andfinally the propionic anhydride,

the aceto-propionic anhydride having re-ar ranged during the distillation to form, acetic anhydride and propionic anhydride. The propionic anhydride may be then converted to propionic acid.

Our novel process may be carried out without pyrolysis. One feature of the process is to obtain as high a yield'of propionic anhydride as possible, but the fact that ketene itself may be formed in the reaction does not represent a loss because it is converted into acetic anhydride as soon as it passes into the acetic acid.

For a more complete understanding of our novel processes, reference is made to the attached the use of catalysts and is, as described, a simple drawing forming a part of the present application. Fig. 1 is a semi-diagrammatic side elevation showing one form of apparatus arrangement for carrying out our process. Fig, 2 is a similar type view of another apparatus arrangement for carrying out our process.

In Fig. 1, 2 is a pre-evaporator or still pot. This device is connected by conduit 3 through the reaction or pyrolysis chamber 4.

The pyrolysis chamber may be of the type such as described in U. 3. 1,723,724 and if desired, contain a metal network, corebuster or other means for heat distribution. Or, a tube having a con-- be utilized for the construction of some of the tinuous passage therethrough may be employed,

parts.

The pyrolysis chamber is connected by conduits 6, 7 through condenser 8 to a reflux apparatus 9, which may comprise a column. This apparatus will include a condenser or dephlegmator 'II for furnishing reflux. A base heater having heating means may be provided at E2. The upper portion of this apparatus is connected by conduit it to a scrubber it or other equivalent device into which reaction medium such as acetic acid may be introduced at it.

The scrubbing device Mi is provided with a draw-oil conduit H which leads to'distillation column I 8 of conventional construction, hence extensive description thereof is unnecessary. This distillation column will include a base heater i9, vapor draw-oi 28 which leads to condenser 22. A reflux line is provided at 23 and a conduit for drawing ofi distilled components at 24%.

In 'Fig. 2, the apparatus disclosed is in some respects similar to Fig. i and includes the vaporizer 32, and the conduit 33 which leads to pyrolysistube 35. In this apparatus arrangement the materials from the pyrolysis chamber are conducted through conduit 36 to the condenserheat exchange arrangement 3?, 38. As will be more apparent hereinafter, this arrangement has a number of advantages. The conduit 38 is connected to a reflux column as, provided with a condenser or dephlegmator ii and a base heater 62. In addition, this column includes a feed conduit id for raw material. By this means the raw. materials may be caused to exert a reflux action.

The reflux unit 39 is connected by conduit 433 to a scrubber tit and distillation column 68 oi a construction such as already described with respect to Fig. l.

The following example is set forth with particular reference to Fig. 1. This example is described primarily for the purposes of illustrating our invention and is not to be construed as a limitation thereof.

Methyl ethyl ketone of commercial quality or chrome steels containing from about 15% to,

40% chrome may be employed. However, the

Presence of free iron ornickel is to be avoided.

The methyl ethyl ketone vapors are subjected to a short time of contact in the pyrolysis'chamber at a temperature of from about between400 C.

to 1000 C. dependent upon speed of passage and tube construction. As pointed out in the Clarke and Waring patent, the tube may contain metal network, corebuster or other type of construction for-better heat distribution or a narrow d ameter tube may be employed. The time of con tact would generally be less than 10 seconds and in many instances may be reduced to considerably less than 1 second. The employment of reduced pressure will' also reduce the time of pyrolysis contact.

The pyrolysis products leaving the pyrolysis tube l, at 6 contained considerable amounts of unstablematerialzsuch as ketene and methyl ketene. However, we have found that methyl ketene is actually produced by pyrolysis treatment. These pyrolysis products containing methyl ketene, which also contain ketene as well as various hydrocarbons and unreacted methyl ethyl ketone, were subjected to a substantial cooling in condenser 8. From condenser t the materials were passed into reflux column 9 where by means of condenser ii the methyl ethyl ketone is caused to fully condense out. In condensing out, this methyl ethyl ketone washes the methyl ketene gases, thereby condensing out methyl ethyl ketone contained therein. The condensed methyl ethyl ketone collects in the column base 52 where it may be subjected to a certain amount of heating for liberating any ketenic components. ethyl ketone may be subsequently returned to the vaporizer 2.

The methyl ketene containing vapors issuing from above the condenser H were passed into a contact device it such as a packed column orscrubber, where the gases were washed with warm acetic acid. This acetic acid may be of tem- Peratures between about room temperature and or C. This acetic acid is preferably glacial acetic acid but a hydrous acid may'be employed as will be set forth in further detail hereinafter.

The acetic acid may contain catalysts such as an inorganic acid (hydrochloric or sulphuric acid) or some organic compound containing either a sulphate or chloride group. Such a catalyst may be employed to facilitate the reaction between the methyl ketene and the acetic acid in which event either higher or lower temperatures than the above specified may be employed. The washing of the methyl ketene containing gases with warm acetic acid causes the formation of aceto-propionic anhydride as well as acetic anhydride. Acetic anhydride is formed due to the presence of ketene along with the methyl ketene.

This anhydride mixture was conducted to a fractional distillation column and subjected to a fractional distillation treatment. The distillation treatment caused the aceto-propionic anhydride to i e-arrange, forming acetic anhydride and propionic anhydride. The acetic and propionic anhydride was then fractionally distilled in accordance with conventional procedure.

Acetic anhydride may be distilled ofi first and then a relatively pure high-grade propionic anhydride distilled off and recovered at 241 or if desired, after the distillation of the acetic anhydride, water or dilute acid may be added which .will convert propionic' anhydrideto propionic acid or the propionic acid may be distilled from the column and recovered from the propionic acidswater azeotrope or propionic acid may be withdrawn fromthe base heater it. Any acetic anhydride-formed, if desired, may be converted The unreacted methyl However, we do not wish to be bound thereby as these equations are set forth merely for the purpose of technical explanation and for a better understanding of the theory of operation of our process.

Decomposition of methyl ethyl ketone takes place probably in-accordance with both of the following reactions:

(a) .CHaCH2COCHa Cl-IaCH=CO+CH4 Methyl ethyl ketone Methyl ketone methane Part of the methyl ketene (CI-BCHTCO). decomposes to ketene as: (c) 2cH=cI-I=c0- 2cn2=c=o+czm- Methyl ketone Ketene Ethylene (d) The methyl ketene reacts with warm acetic acid as follows:

CHiCH=CO+CIhCOOIl CHZCHICO /O CHaCO Methyl keieue Acetic acid Aceto'propionic anhydride Methyl ketene Propionic acid A similar process to that described may be carried out in the apparatus of Fig. 2, in which event more efiicient results may be expected. The passage containing methyl ketene pyrolysis vapors in contact with methyl ethyl ketone as shown in Fig. 2 produces a substantial cooling but at the same time prevents too great a cooling with the attendant condensation of methyl ethyl ketone. By this arrangement the removal of methyl ethyl ketone may be delayed and the materials are washed with the incoming methyl ethyl ketone in the reflux column 39. By this arrangement an improved separation of components is obtained as well as considerable heat recovery.

In place of pyrolyzing methyl ethyl ketone, we may also include the pyrolysis of diethyl ketone, which is decomposed in our apparatus in accordance with the following equations:

acetic acid which is more readily available than many other organic acids.

While the above examples represent our preferred embodiment, our invention has wider applications. For-example, we have found that the ketene materi lsfproduced at i3 instead of being contacted in Hlpr '44 as already described may be contacted with thoacid sludge obtained from the fibrous esterification of cellulose to cause a separation thereof. v

The aforementioned sludge comprises acetic and propionic acids and anhydrides mixed with. Stoddard solvent or other type hydrocarbon or hydrocarbon solvent. This mixture presents considerable difliculty of separation. Such sludge mixtures cannot be separated by direct distillation inasmuch as the acetic and propionic acids form constant boiling mixtures with the hydrocarbon solvent. Analysis of a sludge sample, for example, shows the following components:

Grams Acetic acid 550 Propionic acid 1'79 Acetic anhy 226 Propionic anhydride 276 Stoddard solv nt 420 By passing ketene-containing materials produced in accordance with the aforementioned processes into sludge mixtures the acids may be converted to anhydrides as, above described. This will cause the sludge mixtures to separate into layers. These layers may be then treated for separation purification by conventional fractional distillation processes. We have also found that ketene suchas produced from the pyrolysis of acetone, acetic acid and the like will also produce a layer separation in sludge mixtures.

From the foregoing description of this invention, it is apparent that various changes might be made without departing from the spirit or scope thereof, hence, we do not wish to be-restricted except in so far as necessitated by the prior art and the spirit of the appended claims.

, What we claim and desire to secure by Letters Patent 01! the United States is:

l. A process for the preparation of propionic anhydride, which comprises preparing a gas containing methyl ketene and ketene, contacting the methyl ketene and ketene with acetic acid to form an .aceto-propionlc anhydride and acetic anhydride mixture and subjecting anhydride mixture to fractional distillation whereby propionic anhydride is obtained. 2. A process for the manufacture of propionic anhydride and acid,'which comprises preparing vapors containing substantial amounts of methyl ketene, and contacting said vapors with acetic acid containing a catalyst and thereafter subjecting the reaction mixture to distillation.

3. A process for the preparation of propionh anhydride, which comprises preparing a gas containing methyl ketene and ketene from a 4-5 atom ketone, contacting the methyl ketene anc' ketene with undecomposed ketone and then witt acetic acid to form aceto-propionic anhydride an: acetic anhydride, and subjecting the anhydrid: mixture to distillation whereby propionic anhydride is obtained.

4. The process for the manufacture or propionii anhydride and acid which comprises preparin vapors containing substantial amounts of methy ketene and contacting said vapors with acetii acid containing an acetylation catalyst.

5. A process for producing propionic anhydride, which comprises preparing ketene-contain ing vapors, passing thev ketene-containing yapon into contact with a sludge mixture obtained Iron cellulose ester manufacture containing propionii acid mixed with hydrocarbons whereby separa tion into layers is obtained, and recovering propionic anhydride from the layers.

6. In a process for the manufacture of methyl ketene. the step which comprises passing methyl ethyl ketene through a stainless steel pyrolysis tube maintained at a temperature between 500 C. and 800 C. in less than 3 seconds.

7. In a process wherein methyl ketene is produced, the steps which comprise passing a 4-5 carbon atom lower dialkyl ketone through a stainless steel pyrolysis tube maintained at a temperature between 500 C., and 800 C. in less than 3 seconds, and subjecting the resultant methyl ketene containing vapors to a wash with incoming ketone.

8. In a process wherein the methyl ketene is produced, the steps which comprise pyrolysing 4-5 carbon atom lower dialkyl ketone in less th: 3 seconds and fat 9. temperature between 500 and 550 C. in contact with a stainless ste pyrolysis tube and under reduced pressure.

9. In a process wherein methyl ketene is pri duced. the stepswhich comprise passing meth; ethyl ketone through a stainless steel pyrolys tube maintained at a temperature between 501 C. and 800 C. in less than 3 seconds. contactin the products of pyrolysis which contain meth; ketene with a lower fatty acid and distilling tr reaction products resulting from said conta with the lower fatty acid.

GALE F. NADEAU. CARL J. MALM.

CERTIFICATE OF CORRECTION. Patent No. 2,255,561. March 1 19m.

v GALE F. NADEAU, ET AL.

I It is hereby certified that error appears in the printed specification of the above numbered patent requiring correction as follows: Page 11; first column, line 5, for "ketene" read ketone; and that the said Letters Patent should be read with this correction therein that the same msy conform to the record of the case in the iatent Office.

Signed and sealed this 29th day of April, A. D. 19111.

I Henry'van Arsdale,

(Seal) Acting Commissioner of Patents.

Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US2476859 *Feb 7, 1948Jul 19, 1949Eastman Kodak CoProcess for preparing acid anhydrides and acetone
US2509877 *Jun 20, 1947May 30, 1950Standard Oil Dev CoProcess for preparing acetic anhydride
US2589112 *Oct 30, 1948Mar 11, 1952Standard Oil Dev CoAbsorption of ketene
US2688635 *May 24, 1951Sep 7, 1954Allied Chem & Dye CorpProcess for the production of ketene or acetic anhydride from a mixture of acetic acid and formic acid
US2743296 *Nov 30, 1951Apr 24, 1956Eastman Kodak CoManufacture of lower aliphatic acid anhydrides
US3854886 *Nov 30, 1967Dec 17, 1974Rockwell International CorpApparatus for preparing chlorine pentafluoride
US4861436 *Feb 7, 1989Aug 29, 1989Lloyd BergWith dimethyl sulfoxide-pelargonic acid extractive agent
US5475144 *Jun 8, 1994Dec 12, 1995The University Of DelawareCatalyst and process for synthesis of ketenes from carboxylic acids
Classifications
U.S. Classification562/892, 568/302, 422/198, 568/301, 422/234
International ClassificationC07C49/88, C07C45/88, C07C51/56
Cooperative ClassificationC07C49/88, C07C51/56, C07C45/88
European ClassificationC07C51/56, C07C49/88, C07C45/88