US1826144A

US1826144A - Process of refining hydrocarbon oils with manganese salts

Info

Publication number: US1826144A
Application number: US361519A
Authority: US
Inventors: Lachman Arthur
Original assignee: RICHFIELD OIL Co OF CALIF
Current assignee: RICHFIELD OIL Co OF CALIF; RICHFIELD OIL Co OF CALIFORNIA
Priority date: 1929-05-08
Filing date: 1929-05-08
Publication date: 1931-10-06
Anticipated expiration: 1948-10-06
Also published as: US1826142A; US1826143A; US1826139A; US1826146A; US1826145A; US1826141A; US1826140A; US1826147A; US1809170A

Description

Oct. 6, 1931. I A. LACHMAN 1,326,144

PROCESS OF REFINING HYDROCARBON OILS WITH MANGANESE SALTS ol igina l Filed May 8, 1929 INVENTOR fiRT/IMQ LICV/Ni/V ATTOR.NEY

Patented Oct. 6, 1931 ARTHUR LAOHMAN, OF BERKELEY, CALIFORNIA, ASSIGNOR TO RICHFIELD OIL COIVL PANY 01? CALIFORNIA, OF LOS ANGELES, CALIFORNIA, A CORPORATION OF BIBLE:

WARE

PROCESS OF BEFINING- HYDBOCARBON OILS WITH MANGANESE SALTS Original application filed May 8, 1929, Serial No. 361,513. Divided and this application filed May 8, 1929.

Serial No. 361,519.

The process or" refining hydrocarbon oils,

as described in this application, is applicable to all mineral oil products derived by distillation or cracking operations, such as lubrieating oils, lamp oil stocks, gasoline stocks,

distillates derived from oil shale, etc., and is particularly adaptable to gasoline stocks obtained by cracking higher boiling hydrocarbon oils. For the purpose of simplifying the description, reference will be made to gasoline only.

Crude gasoline stocks obtained by distilling or cracking petroleum oils consist of a mixture of saturated and unsaturated hydrocarbonstogether with sulphur compounds, nitrogen bases and other substances of an undefined nature. These latter substances are readily oxidizable at ordinary temperatures and are usually responsible for the change of color which takes place when refined gasoline is stored. These oxidizable substances are removed with difficulty when gasoline stocks are treated by the methods known in common use.

in order to show the nature of my invention, it is desirable to describe the method now in common use in oil refineries, and particularly that step of refining gasoline stocks which consists in deodorizing and stabilizing the same. Crude gasoline stocks obtained by distillation ofcrude petroleum oil or by cracking a higher boiling petroleum oil, are customarily treated with approximately from 1 per cent to as high as 8 per cent by weight sulphuric acid, the quantity of sulphuric acid depending upon the nature of the gasoline stock to be treated and the product desired. This acid treatment usually consists in eommingling the gasoline stock with the required amount of sulphuric acid necessary to obtain the desired extraction, either by the well-known batch or'continuous treatment, after which the products of the acid reaction are permitted to settle. and then withdraw from the treated gasoline stock. The acid treated gasoline stock is then neutralized by washing with a water solution of an alkali and finally with water. This treatment removes most of the impurities, but subsequent treatments are usually necessary to deodorize and remove or convert corrosive sulphur compounds into non-corrosive bodies. .For this purpose, a Water solution of sodium plumbite or sodium hypochlorite is usually employed to render the gasoline sweet to the doctor test The general objections to a treatment of this character are as follows:

(1) Gasoline purified by this method trequently becomes discolored when stored for a period of time;

(2) Considerable quantities of sulphuric acid are required, which are difiicult to recover;

(3) As high as 10 per cent of the valuable stable unsaturated hydrocarbons contained in the gasoline. stock may be lost; and

l} The treatment must frequently be followed by a deodorizing' or sweetening process, such as that heretofore described.

New, T have discovered that the sulphuric acid normally used to treat crude gasoline stocks may be reduced to a highextent, and in many cases may be entirely eliminated by the employment of a water solution of certain metallic salts, or mixtures otthe same, which may be zinc, copper, cadmium, mercury, iron, chromium, manganese, alum num, nickel or cobalt water soluble salts, such as the chloride, bromide, iodide, sulphate, nitrate, and also any of the water soluble salts of the above named metals or organic acids such as the sulphonic acids of benzol, toluol and xylol, or the sulphonic acids derived from the treatment of petroleum oils with sulphuric acid.

The process described briefly consists in passing the hydrocarbon oil product such as gasoline stock while in a vapor state, through or in contact with a hot concentrated water solution of any of the aforesaid metallic salts or mixtures thereof. The gasoline stock so treated is usually pure enough for immediate use, although it sometimes may contain small amounts of hydrogen sulphide, which may be removed by washing with an alkaline solution of sodium or calcium hydroxide, or the carbonates of sodium or potassium.

The hydrocarbon oil stock to be treated by my invention may or may not have had a preliminary treatment with sulphuric acid, or other agents to partly purify the same, or mav be first partly purified by my invention and the purifications completed by methods known in the art, such as treatment with caustic alkali, sulphuric acid, etc. In case of gasoline stocks produced by cracking high sulphur bearing crude petroleum oils or residuums it may be advantageous to treat such gasoline stocks with small amounts of sulphuric acid before the treatment with a concentrated water solution of any of the aforestated metallic salts, which may also be followed by treatment with an alkaline water solution of sodium, potassium or calcium hydroxide, or the carbonates of sodium or potassium.

Although a solution of less concentration may be employed which may range from 50 or less to approximately 85 per cent, the strength of the water solution of the metallic salt or mixture of salts employed is preferably a substantially concentrated solution, and the temperature employed for the treatment is approximately 300 to 400 degrees E, which normally fluctuates, depending upon the vaporizing temperature of the oil under treatment.

With the foregoing preliminary explanation, the preferred embodiment of my invention will now be more fully explained by reference to the accompanying drawing which is a diagrammatic view of one form of apparatus which may be employed for carrying out the objects of the present invention.

Referring to the drawing, 2 indicates a pipe leading to a source of crude gasoline vapors not shown, such as a fractionating tower employed to separate the lower boiling oils from the higher boiling oils. B indicates a tower of suitable height and diameter filled with resistant or contact material, such as fire brick, spiral tile or the like, indicated at 3, which forms numerous tortuous passages through the tower, although it is to be understood that the well-known bubble cap contact tower may be employed. Disposed above the tower or adjacent to the same, is a tank 12 containing a substantially concentrated water solution of a metallic salt or mixtures of the same, as heretofore enumerated, having a concentration of from 50 per cent or less to as high as approximately 85 per cent. This tank is connected to the top of the tower by means of a pipe 4 having a regulating valve 5. This pipe terminates over a spreader plate 6 and this plate evenly distributes the water solution of the metallic salt or salts when the valve 5 is opened, over the brick work or contact material. The water solution of the metallic salt or salts flows downward through this contact material and may finally be discharged through the bottom by a pipe 7, after which it is treated for recovery. The tower B is also provided with a steam or water inlet pipe 8, which intermittently or continuously supplies a predetermined amount of water or steam to the tower. The hot gasoline vapors from the pipe 2 enter the lower end of the tower B at a point 9. The oil vapors pass up through the numerous contact passages in the brick work and thereby come into intimate contact with the said water solution of metallic salt or salts flowing over the same. Although other temperatures may be employed, both the water solution of metallic salt or salts and oil vapors are generally maintained at a temperature of approximately 300 to 400 degrees F., and the oil vapors are discharged at the upper end of the tower through a pipe 10 which is connected with a condenser 11 of suitable construction. The gasoline vapors passing through the contact tower B at the temperature specified, vaporize a certain amount of water from the water solution of metallic salts and the purpose of the steam or water inlet pipe 8 is that of continuously maintaining the solution at a certain water content so as to maintain the necessary fluidity which is essential for good contact between the rising gasoline vapor and the down-flowing water solution of metallic salt or salts. Preferably the concentration of the water solution of metallic salt or salts is maintained at its predetermined limits of concentration by a continuous introduction of water or water vapor. Otherwise solid metallic salt or salts ,and solid sludge impurities may plug the passages through which the gasoline vapors are being conducted.

While not always necessary, it is beneficial that the water solution of metallic salt or salts contain hydroxides or oxides of any of the metals, or mixtures thereof, heretofore enumerated, before being introduced into the system. This may be accomplished by agitating the water solution of the metallic salt or salts with any of the hydroxides or oxides of any of the enumerated metals. The optimum amount or" the metal oxide or hydroxide ranges from about of 1 per cent to 3 per cent by weight of the water solution of metallic salt or salts. In explanation, when the oxides or hydi oxides of any of the aforementioned metals or mixtures thereof are soluble in substantial amounts in the salt or salts solution at the temperature and pressure employed, it is no doubt that the beneficitl action will be enhanced, but even it no substantial solubility exists, useful effects can be obtained if the oxides and hydroxides are suspended in the salt or salts solution.

The reaction tower B is kept full of the water solution of the metallic salt or salts containing metallic hydroxides or oxides of any of the enumerated metals or mixtures of the same, and a fresh supply of approximate ly 15 pounds of the said solution is admitted for each barrel of gasoline stock under treat.- ment and a corresponding amount of the spent solution is withdrawn at the same time.

The amount of water vapor required to replace the vaporized water from the water solution of metallic salt or salts varies within wide limits, depending upon the concentration of the solution employed, the temperature at which the operation is carried out and the nature and amount of inert gases which may accompany the gasoline vapor being treated. Approximately to 100 pounds of water or water vapor will usually be suiiicient for each barrel of gasol ne stock treated; By this treatment the maior portion of the impurities contained by the gasoline stock is removed and carried out with the water solution of metallic salt or salts as a sludge and the purified gasoline vapors. when condensed, are suitable tor use as a refined gasoline stock of high purity.

While the process herein described is well adapted for carrying out the objects of the present invention, it is to be understood that various modifications and changes may be made without departing from the invention, such for example as the use of centrifugal or other mechanical mixers or the employment .of any of the well-known contact towers wherein a water solution of a metallic salt or mixtures of metallic salts. either organic or inorganic, heretofore enumerated, may be commingled with or brought. into contact with a petroleum oil vapor at the reacting temperaturcs and the invention includes all such modifications and changes as come within the scope of the appended claims.

What I claim is:

1. A process of refining mineral oils. comprising, vaporizing a mineral oil, contacting the vaporized oil with a maintained water solution of a manganese salt, and then condensing purified oil vapor separated from. products of reaction and treating agent.

2. A process of refining mineral oils, coinprising, vaporizing a mineral oil by the application of heat, contacting theheated vaporized mineral oil with a substantially concentrated water solution of a manganese salt maintained in solution, and then condensing purified oil vapor separated from products of reaction and treating agent.

3. A process of refining mineral oils, comprising, vaporizing a mineral oil, contacting the vaporized mineral oil with a maintained water solution of a mixture of manganese salts, and then condensing purified oil vapor separated from products of reaction and treating agent.

4. A process of refining mineral oils comprising, vaporizing a mineral oil by the application of heat, contacting the heated vaporized mineral oil with a heated maintained water solution of a manganese salt, and then condensing purified oil vapor separated from products of reaction and treating agent.

5. A process of refining mineral oils, comprising, vaporizing a mineral oil by the application of heat, contacting the heated vaporized mineral oil with a maintained water solution or a manganese salt, heated to a temperature of not less than the vaporizing temperature of the vaporized mineral oil under treatment, and then condensing purified oil. vapor separated from products of reaction and treating agent.

6. A process of refining mineral oils, comprising, heating a mineral oil to form a vapor at a temperature of approximately 300 to 400 degrees F., contacting the heated vapor with a water solution of a manganese salt maintained in solution at a substantially similar temperature and then condensing purified oil vapor separated from products of reaction and treating agent.

'7. A process of refining mineral oils, comprising, heating a mineral oil to .torm a vapor, at temperatures of approximately 300 to 400 degrees F, passing the heated vapors through or in contact with a water solution of manganese salts maintained in solution at a substantially similar temperature, having a concentration of approximately 50*85% and then condensing purified oil vapor separated from products of reaction and treating agent.

8. A process of refining mineral oils, coniprising, heating a mineral oil to form a vapor. contacting the heated vapor with a maintained water solution of manganese salts containing an oxide of manganese, and then condensing purified oil vapor separated from productsor reaction and treating agent.

9. Ji process of refining mineral Oils. com prising, heating a mineral oil to form a vapor. assing the heated vapor through and in contact with a water solution of mangancsc salts, maintaining the solution in a fluid condition by the addition or water dur ing contact of the water and treating solution, and condensing the vapor after passing through the solution.

10. A process of refining mineral oils, comprising, commingling the vapors of a mineral oil with a Water solution of a manganese salt and then condensing purified oil vapor separated from products of reaction and treating agent maintained in a fluid condition during contact of the vapors and treating solution.

11. A process of refining mineral oils, comprising, heating a mineral oil to form a vapor, passing the heated vapor through and in contact With a Water solution of a manganese salt containing an oxide of manganese, maintaining the solution in a fluid condition by the addition of Water during contact of the vapor and treating solution, and condensing the vapor after passing through the solution.

12. A process of refining mineral oils, comprising, heating a mineral oil to form a vapor, passing the heated vapor through and in contact with a Water solution of manganese salts containing from 1/2 of l per cent to 3 per cent by Weight of manganese oxides, maintaining the solution in a fiuid condition by addition of Water during contact of the vapor and treating solution and condensing the vapor after passing through the solution.

13. A process of refining mineral oils, comprising, heating a mineral oil to form a vapor, passing the heated vapor through and in contact With a water solution of manganese salts, maintaining the concentration of the solution within predetermined limits by the addition of Water during contact of the vapor and treating solution, and condensing the vapor after passing through the solution.

14. A process of refining mineral oils, comprising, heating a mineral oil to form a vapor, at temperatures of approximately 300 to 400 degrees F, passing the heated vapor through and in contact With a Water solution of a manganese salt, maintained at a similar temperature and having a concentration of approximately 50-85%, main tainiug the concentration of the solution as specified by the continuous addition of Water during contact of the vapor and treating solution, and then condensing the vapor after passing through the solution.

15. A process of refining mineral oils, con'iprising, vaporizing a mineral oil, contacling' the vaporized oil with a Water soluion of a manganese salt, intermittently introducing water into the solution of manga nese salt to maintain the aqueous solution and continuously condensing vapors of the purified mineral oil separated from the products of reaction and solution of manganese salt.

16. A process of refining mineral oils, comprising, heating a mineral oil to form a