US1208833A - Process of producing phenols. - Google Patents

Description

A. s. RAMAGE. PROCESS OF PRODUCING PHENOLS.

APPLICATION HLED APR-20, 1916.

Patented Dec. 19, 1916,

. Who z mil/W64. s. WM L I sg g WRR I AGE, a subject of the King of Great Britain, residing at Detroit, in the county of Wayne ALEXANDER S. RAMAGE, OF DETROIT, MICHIGAN, ASSIGN OR TO BOSTAPH ENGINEER- IN G COMPANY, OF DETROIT, MICHIGAN, A CORPORATION OF MICHIGAN.

PROCESS OF PRODUCING PHENOLS.

Specification of Letters Patent.

Patented Dec. 19, 1910.

Application filed April 20, 1916. Serial N 0. 92,469.

To all whom it may concern Be it known that I, ALEXANDER S. RAM- and State of Michigan, have invented certain new and useful Improvements in Processes of Producing Phenols, of which the following is a specification. I

This invention is a process whereby phenols (phenol proper and its homologues, ineluding cresol) are prepared by a treatment by by rogenation, in presence of a suitable catalyst, of certain distillation products con-' tainin high boiling phenolic bodies of the creoso type.

It is known that the oils from the lowtemperature distillation of coal consist chiefly of olefins, with variable proportions of so-ealled high-boiling tar acids, such as creosol and its. homologues, boiling above 210 0. Such oils contain only very small proportions of cresol (cresylic acid) and practically no phenol, and are therefore valueless for ereosoting purposes or for phenolrecovery. According to the present invention such high-boiling tar acids from the above or any other source are converted into phenol and cresol by hydrogen acting in presence of a suitable catalyst. It is probable that by this treatment the oxymethyl groups, together with a part of the methyl groups, are substituted by hydrogen, thereby producing a mixture eontainln phenol and cresol. The catalyst prefera ly used is nickel, reduced from nickel hvdroxid at tem peratures below 325 C. and distributed over long fibered asbestos. This is placed in tubes and 300 C. The product is condensed, and

if desired purifie in any usual manner, and the excess of hydrogen is collected for re-useif so desired.

Preferably the catalyst is heated to a temperature of about 600650 0., in which case I have been able to convert more than 50 Percent. of the contained high-boiling tar acids into phenol and cresol in the course of a. single passage through a tube four inches in diameter and having a heated zone three feet, six inches in length. The product from the hydrogenation is fractionated, the fraction boiling between 175 and 208 0. being collected, and the higher boiling residue ire-processed under the same conditions to continue or eomplete'the conversion.

The described reaction proceeds, although relatively very slowly, at much lower temperatures than those mentioned above. .For example, operating at about 300 (1., ten passages of the material through a catalyst in a tube of the dimensions above mentioned were required to effect a forty per cent. conversion. It is therefore economical to operate at the higher temperature ranges mentioned above.

One form of apparatus which may be used for carrying out my invention is disclosed in the accompanying drawing, wherein the figure is a diagrammatic vertical sectional view.

In said drawing, 1 represents a tank for containingthe material to be hydrogenized, from which tank this material is delivered through pipe 2 to an injector 3 which may be of the Sehiitte-Koerting type. I I ydrogen is supplied to this injector under a pressure of about forty pounds, or suflieient to establish a flow of the vapors through the system. This hydrogen may be derived from any sourcewhatever, illustrated in the present case as a compressor 4. The hydrocarbon thus atomized is sprayed into a series of interconnected tubes 6 containing the catalyst, each tube heated by a resistance coil 7. From the tube 6 a valved pipe 8 leads to a condenser 9, operating as a reflux, whereby the high-boiling or unconverted material is returned through pipe 10 to the tank 1 for reprocessing. Suitable valved connections 5 are provided whereby any desired number of tubes 0 may be operated in series according to the temperature and other conditions. The converted product passes in the form of vapor to the condenser 12, the condensate flowing to the receptacle 13 from which it may be withdrawn as desired. The uncondensed gases consisting largely of hydrogen,

are carried through any suitable scrubbing or purifying system, and thereafter returned by pipe 11 to the hydrogen compressor 4, together with such addition of hydrogen from extraneous sources as may be required.

The process carried out under the 'condi 5 tions described above proceeds without appreciable separation of carbon, and n0 tendency toward the conversion of the hi h-boiling tar acids into parafiins and ole ns has been observed.

-I claim 1. The process of producing phenols from high-boiling tar acids, which consists in subjecting a material containing such acids, at a suitable temperature, to the action of hy- I drogen in presence of a catalyst.

- 2. The process of producing phenols from highboiling tar acids, which consists in introducing a material containing such acids in the form of a spray intimately mixed with hydrogen into a chamber containing a catalyst maintained at a suitable temperature,

and condensing and collecting the resulting phenols.

, 3. 'The process of producing phenols from high-boiling tar acids, which consists in spraying a material containing such acids by means of a jet of hydrogen into a chamber containing a heated catalyst, and condensing and collecting the resulting phenols.

4. The process of producing phenols from high-boiling tar acids, which consists in spraying a material containing such acids by means of a jet of hydrogen into a chamber containing a catalyst maintained at a temperature of about 600650 C. and condensing and collecting the resulting phenols.

5. The process of producing phenols from high-boiling tar acids, which consists in subjecting such acids at a suitable temperature to the action of hydrogen in presence of a nickel catalyst.

6. In a process of producing phenols, the step which consists in-convert1ng high-boils a on with hydrogen.

In testimony whereof I affix my signature in presence of two witnesses.

ALEXANDER S. RAMAGE.

Witnesses v CHARLES FENN, FLORENCE J ACOBI.

acids into phenols by reacting there-

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