US1337523A - Process of refining cracked oils - Google Patents

Description

E. H. LESLIE AND C. BARBRE.

PROCESS OF REFINING CRACKED 0|LS. APPLICATION man SEPT. 13, I917.

Patented Apr. 20, 1920.

UNITED STATES PATENT OFFICE.

EUGENE H. LESLIE AND CLARENCE BABBiR'E, or Los ANGELES, CALIFORNIA, ASSIGNORS T GENERAL PETROLEUM CORPORATION, A CORPORATION OF CA IFORNIA.

PROCESS BEFINING CRACKED OILS.

Specification ofLetters Patent.

Application filed September 13, 1917. Serial No. 191,131.

To all whom it may concern:

Be it known that we, EUGENE H. LESLIE and CLARENCE Bannnn, both citizens of the United States, residing at Los Angeles, in the county of Los Angeles and State'ot' California, have invented anew and useful Process of Refining Cracked Oils, of which the following is a specification,

Our invention relates to the art of refining petroleum oils, and the principal-object of the invention is to provide a process by which a cracked oil may be refined to improve its color and odor and render-it more stable. A number of processes have been de such 'oils often contain organic acids or bases, phenols, and othcr compounds which tend to give objectionable color and odor. All these materials are hereinafter referred to as unsaturated compoundsand the term cracked oils is herein used as inclusive of all hydrocarbon oils containing such un- F) saturated compounds. Such cracked oils may be gas'olenes. burning. lubricating, or other oils of any specific gravity or viscosity found in the refining art.

By our invention the unsaturated compounds are in part polymerized and condensed'and a water white distillate of good odor is produced, from five to fifteen per cent. of the oil treated appearing, however, as a resinous still residue. This resinous still residue is a valuable commercial product and its production is made the subject :of a companion application Serial No.

191,198, filed September 25,- 1917, entitled- Process of producing synthetic resins.

Further objects and advantages will be made evident hereinafter.

In the drawing, which is very diagrammatic, an apparatus adapted to carry on our process is shown.

This apparatus consists of a digester 11, a filter 12, a still 13, a primary condenser 14, and afinal condenser 15. The digest'er 11 is provided with an agitator 16, operated through a shaft 17 by means of a belt 18 from a prime mover, not shown. A pipe 20 is secured in the top of the digester 11, being connected through avalve 21 with a cracked oil supply pipe 22, and through a valve 23 with a condensate discharge pipe 24 of the primary condenser 14. The pipe 24 is also connected through a valve|25 with a primary product delivery pipe 26. A charging opening 19, closed'by a suitable cover, is-

provided in the top of the digester. A steam jacket 27, supplied with steam through a pipe 28, controlled by a valve 29, is provided for the purpose of heatingthe bottom of the digesterill. A vapor pipe 30 carries the vapor from the top of the digester 11 to the primary condenser 14. i

The condensers 14 and 15 may be of any suitable design, those shown being identical as to construction and consisting of a closed shell 31,'having intermediate'heads 32 and 33. entering end of the condenser into two chambers, the vapor being delivered into the'top chamber and, passing through tubes Patented Apr. 20, 1920.

A battle 34' divides the space at the n35 into the space between the head 32 and y into the lower chamber, from whichthe condensed products may be removed through adelivery pipe. Water is supplied and removed from the condensers through pipes 37, this water surrounding the tubes 35 and 36 and providing .the cooling medium.

A pipe 38, controlled by a valve 39, conmeets the lower portion of the digester 11 with the top of the filter 12. This filter consists of a shell 40, having an opening 41, closed by a suitable cover in the top thereof and having a vapor pipe 42, leading to a condenser, not shown, controlled by a valve 43, also secured in the top. thereof. Secured in the bottom is a perforated diaphragm 44 forming with the bottom of the shell 40 a filtered oil space 45. When in operation acanvas or other suitable filter the end of the shell, and through tubes 36 with a steam jacket 54, supplied with steam through a pipe 55, controlled by a valve A residuum discharge opening 57, closedby a suitable cover, is .provided'in the bottom of the still 13. .The final condenser 15 is of the same general constructionas the primary condenser 14 and is provided with a final product delivery pipe 58 The method of operation is as follows:

The cracked oil to be treated is supplied to the digester 11 through the pipe 22, the:

. valve 21 and the pipe 20, the valve 21 being open and the valve 23 be'ng closed. The digester is also-charged w ith a porous catalyzer through the opening 19. The term porous catalyzer as used throughout this specification refers to any suitable comminuted material such as fullers earth, kiesel gilihr, clay, charcoal,- powdered coke, or the The digester may also be charged with a neutralizer. The term .neutra'lizer as used in this specification refers to calcium carbonate, other alkaline earth carbonates, weak .acid salts of any of the alkali or alkaline earth metals, or to any other suitable metallic base weaker than alkaline earths. The cracked oil, porous catalyzer and the neutralizer are stirred by the agitator 16, heat I being applied by thesteam jacket 27 on the bottom'thereof. We have found that the prelimlnary boiling may advantageously continue from two to five hours. During- .this time the valves 21 and 25 are closed andthe-valve'23 is open so that the vapor passing through the pipe 30 is condensed in' the primary condenser 14, the condensate being returned to the digester 11 through pipes 24 and 20. At the end of this time the valve 23 is closed and the valve 25 is opened and'from five to twentyper cent. of the oil may bedistilled ofl, passing through the pipe 30 intothe condenser 14, where it is condensed, and delivered as a. primary product through the primary product delivery pipe 26. After the five to twenty per cent. of oil, above referred to,- has been distilled ofl, it is found that the boiling po1nt w1ll have risen and that it is possible to raise the temperature of the refluxing mass in the digester. 'Th,is increases the ;speed of the polymerizing reactions The refluxing is now continued for from two to five hours longer with a further production of vapors which are condensed in the condenser l4 and returned through the pipes 24 and 20 to the digester 11,- the valve 23 being open and the valve 25 being closed.

At theend of this time the valve 23 is closed and the valve 25 opened, and from five to twenty per cent. of the contents are distilled off, being, delivered as primary product through the-pipe 26. As a result the boiling point of the oil in therefluxer is again higher, and the refluxing is again continued at a higher temperature for several hours more.

The residue is then discharged through the pipe 38 into the filter 12. The liquid components of this residue then pass through the diaphragm 44 and the filter cloth 46 into the space 45. The solid constituents of the residue are removed through the discharge opening 47 after the adhering oil has been distilled off" by introduction of steam at 48 and removal of the vapor at 42. The liquid components are deliveredthrough the pipe 50 into the still 13 where they are evaporated, the vapors passing through the pipe 52 into the condenser; 15; the condensate from which is a waterwhite distillate which is free from objectionable compounds and Without objectionable odor, and which is delivered as a final product through the pipe 58. The residue left in the still 13 is a resinous material, having a considerable commercial value, which may be removed from thedischarge opening 57.

The function of the porous catalyzer is to produce a rapid polymerization andresinification of the unsaturated and olefinic hydrocarbon portions as well as the unsaturated and bad odored nitrogen and sulfur compounds. The function of the neutrali'zer is to remove or anic acids, phenols and other compounds which tend to render the oil acid or give it a badjodor.

We claim as our'invention 1.. Any process of refining cracked oils and producing a synthetic resin which ineludes heating the oil .in the presence of a porous catalyzer; filtering out the catalyzer;

and distilling the residue'to separate the oil from the resins formed by the'process.

2. Any process of refining cracked oils and producing a synthetic resin which includes heating and agitating the oil 'in the presence of a porous catalyzer; filtering out the catalyzer; and distilling the residue to separate the oil from the resins formed by the process. e

3. Any process of refining cracked oils and producing a synthetic resinwhich includes heating the oil in thepresence of a porous catalyzer and a suitable neutralizing I J agent; filtering out the catalyzer and distilling the residue to separate the oil from the resins formed by the process.

4. Any process of refining cracked oils and producing a synthetic resin which 'in- 5 eludes heating and agitating the oil inthe presence of a porous catalyzer and a suitable neutralizing. agent; filtering out the cata.-'

'lyzer; and distilling the residue to separate the oil from the resins formed by the process.

In testimony whereof we have hereunto 10' set our hands at Los Angeles, California, this 8th day of September 1917.

EUGENE H. LESLIE. CLARENCE BARBRE.

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