US1992310A - Process for treating hydrocarbons - Google Patents

Description

Feb. 26, 1935. w HULTMA'N 1,992,310

9 PROCESS FOR TREATING HYDROCARBONS Filed May 17, 1933 INVENTOR MAQQZ ATTORNEYS Edgar i/fflalimmz Patented Feb. 26, 1935 UNITED STATES;

PROCESS FOR TREATING Edgar w. Hnltman, Los mas, calm, assignor to Hultman & Powell Corporation, Dover, Del., a corporation of Delaware Application May 11, 193;, Serial No. 011.52: a Claims. (01. 204-9) This invention relates broadly to a method for purifying and improving the characteristics and quality, for certain purposes, of hydrocarbons such as gasolines, motor fuels, kerosenmdistillates, mineral oils and other similar hydrocarbons both liquid and gaseous and oi. the hydrocarbon products from the destructive distillation of organic materials such as tars and derivatives thereof.

This method may be practised as a part of usual and customary refining operations or it may be carried out as an addition to or auxiliary to a refining operation. It may also be practised as an entirelyindependent and separate process depending upon the nature of the substance to be treated or the particular characteristics or qualities it is proposed to modify or improve.

The invention relates particularly to contacting the substance to be treated with electrolytes which, if desired, may be rendered more active by electrolysis. It has been found that sulphuric acid when so activated is most eifective in accomplishing the results to be obtained by. practising the invention.

In addition to its application for improving the characteristics of the substance treated, the process lends itself to the accomplishment of othor desirable results; more particularly to the production of certain oxidation products such as alcohols, aldehydes, glycols, fatty acids and the like from a variety of materials. The method of producing oxidation products may be practised as an independent process or as an auxiliary process or it may be carried out simultaneously withthe o treatment of hydrocarbon products.

When sulphuric acid is used in practising the invention it may be subjected to electrolysis in a cell provided with a platinum anode and a lead cathode separated by a diaphragm to keep the gases formedat the cathode separated from those formed at the anode. The decomposition of sulphuric acid thereby caused results in the'production of substantial amounts of persulphuric acid. Caros acid, hydrogen peroxide, women and ozone.

V The so treated acid, in varying degrees of strength but preferably of less than approximately 70% concentration, has been found to be admirably suited for the purpose of refining the hydrocarbon products, hereinbefore mentioned.

In the treatment of kerosene with the acid so activated, undesirable sulphur may be removed and the kerosene improved in color, odor and,

burning qualities. If it is desired to treat gasoline or motor fuels, sulphur may be removed and at the same time the anti-knock characteristics or octane rating may be improvedby proper manipulation of the concentration of the acid used in the process.

If desired, oxidation products such as alcohols,' aldehydes, glycols and fatty acids may be pro- 5 duced by intimately contacting hydrocarbons with sulphm'ic acid activated by electrolysis in a cell similar to that hereinbefore described. The productsformed in the anode compartment of the cell may be passed into the hydrocarbons to be It) treated, agitated therewith, and then returned to' the cell in a continuous cycle. The reaction thereby eflected results in the formation of oxidation products which are soluble in the acid solution and which may be separated therefrom either by fractional distillation or other methods.

The process may be carried out in apparatus such as is illustrated diagrammatically in the annexed drawing forming a part of this application, in which Fig. 1 is a diagrammatic illustration partly in section of one form of apparatus; and

Fig. 2 is a diagrammatic illustration partly in section of another form of apparatus.

Referring now to the drawing, 10 represents a 35 chamber which may be made of non-conductive and acid-resisting material. Said chamber is divided by a partition 11 of like material forming a compartment 12 for the stock under treatment and sulphuric acid compartment 13. The spout d 16 of funnel-shaped cup 15 extends through a suitable orifice in the partition 11. An acid return conduit 14 extends through the partition 11 through another orifice in the partition,

Positioned within the inverted cup-shaped funnel 15, which forms a diaphragm, is a platinum anode 17. "I'he anode is connected by an electrical circuit 19 to a lead cathode 18 positioned about the exterior of the diaphragm formed by funnel A hydrogen vent 21 leads from the sulphuric acid compartment 13 and a suitable conduit 26 is provided for charging acid into the compartment 13. Stock to be treated may be introduced into compartment 12 through conduit 22 connected to a suitable source 28. Outlet 23 is provided in compartment 12, if desired, for drawing oil the stock introduced through conduit'22.

In operation of this form of apparatus, acid of suitable concentration is charged into compartment 13 upto about the level indicated at 27. Stock to be treated is introduced into compartment 12 through conduit 22 to about the level indicated at 1B. A suitable current is p'assed through the electrical circuit and the electro- Iii lytic action thereby set up causes gases formed at the anode to pass upwardly through the spout 16 also providing circulation of the acid on the principle of the air lift. The acid and gaseous products from the anode are thus intimately mixed with the stock under treatment in compartment 12. The acid then settles out from the stock under treatment by gravity and is returned through acid return conduit 14 to the acid compartment l3. Hydrogen formed at the cathode may be vented through conduit 21.

The modification illustrated in Fig. 2 comprises a chamber 50 of non-conducting, acid-resisting material, separated into an anode and cathode compartment by a diaphragm 51 of like material. A platinum anode 52 and lead cathode 53 are connected to an electrical circuit 54. An inlet conduit 56 is led to the bottom of chamber 50 and has its discharge. positioned in proximity to the platinum anode 52. A pump 57 is provided which may take suction from tank 58 containing stock to be treated and for forcing said stock through conduit 56 and discharge same beneaththe surface of the sulphuric acidcontained proximity ofthe platinum anode and when the" level indicated at 61 is reached it overflows into conduit 59 and may be returned to tank 58. The circulation is continued until the desired action is complete.

While various adaptions of the invention will become apparent, the following are set forth as specific examples of the applicability of theprocess with different substances under certain typical conditions:

(A) Sulphuric acid of about 50% concentration was activated by electrolysis in a cell comprising a lead cathode and a platinum anode separated by a diaphragm in such manner as to form separate compartments for the gases formed atthe anode and cathode. The gas formed at the cathode was drawn off and kept separate.

The acid and products formed at the anode comprising substantial quantities of per'sulphuric acid, Caros acid, hydrogen peroxide, oxygen and ozone were drawn off, contacted immediately with a cracked distillate and returned to the cell in a continuous cycle. The sulphur contained in the distillate was reduced from 0.6% to 0.1% in thirty minutes. After prolonged treatment the distillate contained 18% of unsaturated compounds as against 16% before treatment. The odor of the distillate after, neutralization with a caustic wash was sweet and the color was satis-.

, trolytic cell.

utes of continuous recycling the circulation was discontinued and theacid drawn off from the agitaton, The gasoline was then given a suitable neutralization with caustic and water washing. The sulphur content had been reduced from 0.6% to 0.1% in the finished gasoline. The odor was sweet, the color water white, it was negative to the copper strip test, sweet to the sodium plumbite (doctor) test and showed no appreciable deposit when evaporated in a copper dish.

(C) Straight-run gasoline was charged into the agitator and the same procedure as hereinbefore described was followed, except that acid of 30% concentration was used and re-cycled for fortyfive minutes. The finished gasoline was water white, sweet to the doctor test, negative to the copper-strip test and showed no appreciable deposit when evaporated in a copper dish. The anti-knock characteristics of the finished gasoline were substantially improved, the octane number of the finished gasoline being 80 as against 65 for the untreated stock.

(D) A straight-run petroleum ether boiling between 40 C. and 70 C. was treated by agitating electrolyzed acid of about 50% concentration activated in a continuous cycle through the elec- After about five minutes the electrolyte solution contained substantial quantities of alcohols, including butyl, amyl, hexyl and heptyl. -After about fifteen minutes the corresponding. aldehydes were found to be present, and after a half an hour the corresponding fatty acids were present. In another instance in which a cracked distillate boiling between 40 C. of 70 C. was treated in accordance with the invention, oxidation products with substantial quantities of glycols were produced.

While certain specific examples have been set v forth it is not intended to confine the invention to the illustrations given, as heavier fractions of petroleum, such as kerosene and the light and heavy lubricating oils and also other hydrocarbons, whether liquid or gaseous or whether mineral oils or hydrocarbon products from destructive distillation, coal, wood or other organic materials, may be treated in accordance with the invention. Also it is readily apparent that owing to the immiscibility of oil or fractions thereof with the acid and the difference in specific gravity the invention lends itself to the accomplishment of the desired resul by circulating the hydrocarbon through the ce instead of circulat ing the acid. In this case the acid is maintained in the cell and the hydrocarbongnay be delivered to the bottomwhereby it may pass upwards in proximity to the anode to the surface of the acid solution as hereinbefore' described.

It is also apparent that the process may be carried out either as a continuous process through treating towers in series, or by the batch system,

or by a combination of the two, as is well known in the art.

Moreover, the invention is not confined to sul- V phuric acid as the solution to be electrolyzed and used in the refining process. Various other electrolytes, such as. sodium chloride, which may be converted into sodium hypochlorite solution containing free dissolved chlorine may be used. Other examples of solutions are mercury salts, copper salts and phosphoric acid. In some cases the reaction can be accelerated by the use of suitable catalytic agents such as, for example, cerium sulphate. Other metals such astantalum in the presence of a suitable catalyst are satisfactory for the anode of the cell in place of platinum.

' From the foregoing description it may be readily seen that the invention is adapted to a variety of purposes. In the treatment of gasoline, kerosene and other hydrocarbon products, refining losses will be materially lessened by reason of the use of much weaker acid than otherwise would ordinarily be used and in addition the qualities of the treated products may be substantially improved. Furthermore, oxidation products of great value may be made from very cheap raw materials, thus opening a wide field for commercial utilization.

While certain novel features of the invention have been disclosed and are pointed out in the annexed claims, it will be understood that various omissions, substitutions,- and changes may be made by those skilled in the art without departing from the spirit of the invention.

What is claimed is:

l. The process of treating gasoline to increase its octane rating which comprises passing a som ticn of sulphuric acid through an electrolytic cell having an anode and cathode compartment, passing the products of electrolysis formed in the anode compartment both liquid and gaseous into intimate contact with the gasoline to be treated, separating the acid and the reactionproducts dissolved therein from said gasoline, and returningsaid separated acid and said dissolved products and passing same through the cell for further electrolysis.-

2. The process of treating motor fuel which comprises passing a solution of sulphuric acid through an electrolytic cell having an anode and cathode compartment, passing the products of electrolysis both liquid and gaseous formed in the anode compartment into intimate contact with the motor fuel to be treated, separating the acid and the reaction products dissolved therein from said motor fuel, said treatment being continued' until the octane number of the motor fuel is raised, and its anti-knock characteristics are increased, returning said separated acid and said dissolved products to the cell for further electrolysis in a continous cycle.

3. The steps in treating gasoline to increase its octane rating which comprises passing a solution of sulphuric acid of less than approximately concentration through an electrolytic cell having an anode and cathode compartment, passing the liquid and gaseous products of electrolysis formed in the anode compartment into intimate contact with the gasoline to be treated, and continuing the treatment until the octane rating of the gasoline is raised, separating the acid and the reaction products dissolved thereinfrom said gasoline, returning said acid and said dissolved products to the cell for further electrolysis and recycling the electrolyzed solution.

4. Themethod of treating a hydrocarbon'with sulphuric acid which comprises maintaining said trolytic cell, subjecting the solution to electrolysis, passing the gasoline into the said solution in intimate contact with the products formed at the anode of said cell and maintaining said gasoline in intimate contact with said products suificient time to increase the anti-knock qualities of said gasoline.

od of increasing its octane ratingwhich comprises electrolyzing a dilute solution of sulphuric acid in an electrolytic cell having an anode and cathode compartment, immediately and intimately intermixing the products formed in said anode compartment with the motor fuel until the octane rating of said motor fuel is substantiallyraised, separating the solution from the motor fuel and then washing the motor fuel with an alkali. I

, 7. In the art of treating motor fuel to improve its anti-knock qualities, the improvement which comprises intimately intermixing said motor fuel with an aqueous solution of sulphuric acid of less than 70% concentration activated by elect'rolysis in an electrolytic cell having an anode and cathode compartment, theflactivated solution in said anode compartment being immediately contacted with said motor fuel and intermixed therewith until the anti-knock qualities of the motor fuel are improved.

8. The improved steps in treating motor fuels to increase the anti-knock rating comprising passing a solution of sulphuric acid continuously through an electrolytic cell, continuously sub- Jecting the solution to electrolysis, intimately contacting and intermixing the liquid and gaseous products formed at the anode pole of said electrolytic cell with the motor fuel, continuing the intermixing until the anti-knock ratingv of said motor fuel is increased, separating the motor fuel from said solution and washing the separated motor fuel with a. neutralizerfor acids.

I EDGAR W. HULTMAN.

20 6. In the art of treating motor fuels, the meth-

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