US2685578A - Hydrocarbon separation process - Google Patents

Description

Patented Aug. 3, 1954 HYDROOARBON SEPARATION PROCESS Alfred S. Brengle, Richmond, Calif., assignor to California Research Corporation, San Francisco, Calif., a corporation of Delaware No Drawing. Application September 10, 1949,

Serial No. 115,100

8 Claims. 1

This invention relates to an improved method of separating normal parafiinic hydrocarbons from hydrocarbon mixtures containing these and other hydrocarbons by contacting these mixtures with solid urea pre-wet with a low boiling nonpolar liquid in the manner hereinafter described.

It is known that normal paraffinic' hydrocarbons containing at least six carbon atoms per molecule can be separated from hydrocarbon mixtures containing these and other hydrocarbons by contacting the mixtures with a concentrated solution of urea in methanol or with a urea-methanol slurry. As a result of this contact, a solid composite consisting essentially of normal parafiinic hydrocarbons and urea is formed and may be separated by filtration from the unr'eacted portion of the hydrocarbon mixture. The normal paraifinic hydrocarbons may then be separated from the composite by heating or by adding water to the composite. The alcohol employed in this method appears, for the most part, in the filtrate obtained, but minor quantities of the alcohol are retained on the composite and appear in the normal parafiinic hydrocarbons which are separated therefrom.

When it is attempted to employ this method on a large scale to separate hydrocarbons for use as fuels or as charging stocks to processes such as cracking, isomerization, and the like, serious process difficulties are encountered. The alcohol isan excellent solvent for urea, and that portion of the alcohol which passes through the filter carries with it considerable quantities of dissolved urea. Both the urea and the alcohol must be removed from the filtrate to render it suitable for use as fuel or as a process charge stock.

Similarly, the normal paraifinic hydrocarbons separated from the solid composite must be treated for the removal of alcohol and dissolved urea prior to their use or further processing.

The difiiculties attending the use of a solvent for urea, such as methanol, in the process have previously been recognized, and it has been found that the separation of normal parafiinic hydrocarbons from hydrocarbon mixtures may be eifected by vigorously contacting these mixtures with urea in the absence of any solvent. Where this method is employed, the hydrocarbon mixture and the urea must be very vigorously contacted by a method which applies strong shearing forces to the solid particles in the mixture and the period of contact must be prolonged.

It is an object of this invention to provide a method for separating normal parafiinic hydrocarbons from hydrocarbon mixtures, in which no solvent for urea is employed and which, consequently, makes process steps adapted to remove urea from the filtrate and from the normal paraffinic hydrocarbons separated unnecessary.

It is a further object of this invention to provide a process for the separation of normally paraflinic hydrocarbons from hydrocarbon mixtures by which rapid and complete removal of the normal parafiinic hydrocarbons from the mixtures may be obtained without severe agitation and without BIICOllIltGIlIlg the process difficulties which are met when a solvent for urea, such as methanol, is employed.

It has now been found that the rapidity and completeness with which the formation of the composite of urea and normalparaflinic hydrocarbons proceeds may be increased by pre-wetting solid urea with a small amount of a low boiling, normally liquid, non-polar material and then contacting the urea so wetted with the hydrocarbon mixture from which it is desired to separate the normal .parafiinic hydrocarbons.

Suitable low-boiling, non-polar liquids include aromatic hydrocarbons such as benzene and toluene, paraifinic hydrocarbons such as the pentanes, hexanes, heptanes, and octanes, olefinic hydrocarbons such as the pentenes, hexenes and actenes, naphthenic hydrocarbons such as cyclopentane, methylcyclopentane, dimethylcyclopentanes, cyclohexane and methyl cyclohexane, and halogenated hydrocarbons such as carbon tetrachloride, chloroform, and the like.

According to this invention, solid urea is moistened with a minor amount, of the order of 0.1% to about 10% of its weight, of a low-boiling, non-polar liquid. The urea wetted with the nonpolar liquid is then contacted with the hydrocarbon mixture containing normal paraffinic hydrocarbons and other hydrocarbons, and a solid composite comprising urea and normal parafiinic hydrocarbons is rapidly formed.

The process of this invention may be practiced in either batch operation or continuous operation. Where batch operation is employed, the urea, preferably in finely divided form is slurried with a substantial quantity of the low-boiling, nonpolar liquid, and the resulting slurry is then filtered to remove the excess of the non-polar liquid, and to leave on the urea only a sufficient quantity of this liquid to moisten the surfaces of the urea particles. The urea, after filtration in this manner, is contacted with the hydrocarbon feed mixture either by stirrin the hydrocarbon and the urea together, or by shaking the mixture of hydrocarbon and urea. After a contact of a few minutes duration, the solid composite of urea and normal parafiinic hydrocarbons is formed and the mixture is filtered. The filtrate recovered is a hydrocarbon liquid having a substantially lower content of normal parafiinic hydrocarbons than that of the feed, and the filter cake consists essentially of urea and normal parafiinic hydrocarbons. The filter cake may then be separated into its constituent components by heating or by washing with a hot hydrocarbon liquid. Where the composite is separated into its constituent parts by washing with a hot hydrocarbon liquid, the washing is conducted at a temperature below the melting point of urea and the normal parafiinic hydrocarbons are washed from the composite by the hot hydrocarbon, leaving solid, finely-divided urea which may be used in separating further quantities of the hydrocarbon mixture.

The process may be conducted in a continuous manner either by continuously slurrying urea pro-wet with a low-boiling, non-polar liquid with the hydrocarbon mixture, continuously withdrawing the resultant slurry of unreacted hydrocarbons and composite, continuously filtering the slurry, decomposing the composite, and returning the recovered urea to contact further quantities of the feed. The process may also be conducted continuously by disposing finely-divided urea in a fixed bed, wetting the urea with a low-boiling, non-polar liquid in the manner above described, and then percolating the hydrocarbon mixture through the fixed bed. The percolate is characterized by a low content of normal parafiinic hydrocarbons, and the bed of urea is converted to a bed of urea-normal parafiinic hydrocarbon composite. The composite may be separated into its constituent components by washing it with a hot hydrocarbon liquid to remove the normal parafiinic hydrocarbons and leave the finely-divided urea in suitable condition for re-use in the process. In some instances, it is possible to use a hot hydrocarbon liquid for the decomposition of the composite which is also a suitable low-boiling, non-polar liquid for the pre-wetting of the urea. For example, hot toluene may be used to decompose the composite, and the residual toluene remaining on the urea when the normal paraifins have been removed will function as the desired low-boiling, non-polar liquid when the urea is again contacted with the feed.

The process of this invention is especially applicable to petroleum distillates having a 50% point on an ASTM D-158 distillation above about 300 F., such as gas oils, kerosenes, lubricating oil distillates, and heavy naphthas. The lowboiling, non-polar liquids which have been found suitable for use in the process of this invention boil below about 250 F. These liquids, even though they are used in small amount in the process, are desirably recovered from the process products and re-used. Where petroleum distillates of the type described constitute the feed material to the process, recovery of the low-boiling, non-polar liquids from the process products is readily effected by fractional distillation.

When lower boiling petroleum distillates, such as a straight run gasoline, are to be contacted with urea to separate normal parafiinic hydrocarbons according to the method of this invention, the urea is pre-wet with a non-polar liquid boiling below about 250 F. and boiling in a range below the boiling range of the distillate. For example, the ureais Wetted with a C5 hydro- 4 carbon or with petroleum ether prior to contacting it with gasoline.

The following table is illustrative of the improved results obtained in treating a California gas oil with urea according to the process of this invention. The gas oil constituting the feed in the experiments summarized in the table had the following properties:

API gravity 31.1 Aniline point 170 Four point F +45 ASTM 13-158 distillation:

Start, 540 F.; 10%-590 F.; 30%602 F.; 50%-614-. F.; '70%-626 F.; 9070-647 F.; end point, 675 F.

Content of hydrocarbon types as determined by ASTM Method D-875:

Per cent Paraffins 89 Naphthenes 8 Aromatics 3 200 Thinner, straight run distillate of California crude oil:

APT gravity 60.8 ASTM D-86 distillation:

Start 162 F.; 10%177 F.; 50%190 F.; '70%198 F.; %-2l2 F.; end point 255 F.

Content of hydrocarbon types as determined by ASTM Method D875:

Per cent Paraffins 49 Naphthenes 44 Aromatics 7 250 Thinner, straight run distillate of California crude oil:

APT gravity 56.4

ASTM D-86 distillation:

Start 186 F.; 10%-199 F.; 50%212 F.; 70%-222 F.; 90%-24=4 F.; end point 290 F.

Content of hydrocarbon types as determined by ASTM Method 13-875:

Percent Paraifins 43 Naphthenes 48 Aromatics 9 by ASTM Method D-8752 Per cent Paraffins 35 Naphthenes 49 Aromatics 16 In each of the experiments recorded in the table, 50 grams of approximately 100-mesh urea were stirred up with 200. cc. of the loweboiling, non-polar liquid, and the mixture was filtered on a vacuum filter. The urea was weighed after filtration to determine the amount of the nonpolar liquid retained on the urea surface. The urea and 100 cc. of the gas oil described above were then stirred with a glass rod in a beaker. After minutes, the resulting mixture was filtered, the filtrate was heated and blown with nitrogen to expel any of the non-polar liquid carried into it, and the pour point of the filtrate was then determined.

Hydrocarbon separation fromthem is effective in increasing the completenessandv rapidity with which the urea-normal parafiinic hydrocarbon composite is formed. The magnitude of the effect with these stocks is comparable to that obtained with the gas oil in the experiments summarized in the above table.

Experiments have been conducted in which low-boiling, non-polar hydrocarbons were mixed with the feed and the mixture was then contacted with finely-divided urea. The results obtained in these experiments indicate that the addition of a low-boiling, non-polar liquid to the feed is either ineffective, or much less effective, in bringing about the rapid and complete formation of the urea-normal parafi'inic hydrocarbon composite than is the method of pre-wetting the urea with the non-polar liquid and thereafter contacting the urea so wetted with the hydrocarbon feed.

It has been found that the employment of lowboiling, non-polar liquids to pre-wet urea in the Weight Weight Tem per- Maxi- Total New I L of Urea of Urea ature at mum I Reaction Filtrate po ar iquid Before After Sec Temp Time to Tbicken Time Pour Wash, Wash, 0 F o F mjnuts Pt., F. grams grams None 50 77 79 Stirred 7 min. No 10 +45 thickening. Benzene 50 54 73 99 3 min. 02 sec 10 -30 Petroleum Ether 5O 50. 2 75 104 3 min. 55 sec 10 25 n-heptane 50 54 82 93 1 min. 20 sec 10 15 n-pcntane 50 50. 3 70 96 3 min. 40 sec 10 25 50 57 72 95 6 min. sec 10 --15 50 51 72 99 5 min. 45 sec 10 25 50 54 73 96 3 min. 10 sec 10 30 50 50. 6 73 102 4 min. sec 10 25 50 53 71 99 3 min. sec 10 25 53 75 93 2 min. 00 sec 10 18 300 Thinner 50 55 73 75 Stlgei 7 10 +40 1c enmg. Decahydronaphthalene. 50 58 Stgrjei 7 min. No 10 +45 c emng.

The formation of the composite of urea with the normal parafiinic hydrocarbon contained in the gas oil in the experiments tabulated above is evidenced by a visible thickening of the mixture of urea and the gas oil as it is stirred and by an apparent swelling of the solid urea. The time at which this thickening was observed has been recorded to indicate the rapidity with which the composite formed.

No non-polar liquid which boils above 250 F. has been found which is effective in bringing about the rapid formation of the urea-normal paraifinic hydrocarbon composite. The ineffectiveness of higher-boiling, non-polar materials for this purpose is well illustrated by the results obtained with 300 Thinner and with decahydronaphthalene recorded in the above table.

From the column of data indicating the weight of the urea after wetting with a non-polar liquid, it is clear that it need be present in only very small amounts in order to exert a remarkable effect on the rate and completeness of the composite formation. The amount of the low-boiling, non-polar liquid employed does not ordinarily exceed 10% by weight of the solid urea. Larger amounts may be used, but unless they are desirably present in the filtrate which is obtained as a process product, their use is undesirable.

Experiments similar to those summarized in the above table conducted with kerosene, naphtha, Arabian gasoline, and light lubricating oil fractions demonstrate that the employment of low-boiling, non-polar liquids to wet the urea prior to contacting it with these stocks to eifect the removal of normal paraffinic hydrocarbons manner above described is especially effective with finely-divided urea. If urea particles which pass through a -mesh sieve are used, the com-bination of the non-polar liquid with the small average particle size of the urea makes possible very rapid formation of the composite.

I claim:

1. In a process for separating normal paramnic hydrocarbons from a petroleum distillate having an ASTM D-158 fifty per cent point above about 300 F. by contacting said distillate with solid urea, the improved method which comprises wetting the urea with 0.1 to 10% by weight, based on urea content, of a hydrocarbon liquid boiling below about 250 F. and then contacting the dis tillate with the urea so wetted.

2. The method as defined in claim 1 wherein the hydrocarbon liquid consists predominantly of low-boiling normal paraffins.

3. In a process for separating normal parafiinic hydrocarbons from petroleum distillates having an ASTM D-l58 fifty per cent point above about 300 F. by contacting said distillates with solid urea, the improved method which comprises wetting the urea with 0.1 to 10% by weight, based on urea content, of a normally liquid halogenated hydrocarbon boiling below about 250 F. and then contacting the distillate with the urea so wetted.

4. The method as defined in claim 1 wherein the hydrocarbon liquid is an aromatic hydrocarbon.

5. The method as defined in claim 1 wherein the hydrocarbon liquid is a paraflinic hydrocarbon.

6. The method as defined in claim 1 wherein the hydrocarbon liquid is a naphthenic hydrocarbon.

7. The method as defined in claim 1 wherein the hydrocarbon liquid is a petroleum distillate.

8. The method as defined in claim 4 wherein the petroleum distillate is a. naphtha.

References Cited in the file of this patent UNITED STATES PATENTS Number Name Date 2,499,820 Fetterly Mar. '7, 1950 Number Name Date 2,518,677 Garner et al Aug. 15, 1950 2,588,602 Adams et al Mar. 11, 1952 2,594,481 Bowman Apr. 29, 1952 FOREIGN PATENTS Number Country Date 1,733,947 Australia Feb. 12, 1948 OTHER REFERENCES Zimmerschied et al.: J. A. C. S., 11, 2947 (August 1949).

Claims (1)

1. IN A PROCESS FOR SEPARATING NORMAL PARAFFINIC HYDROCARBONS FROM A PETROLEUM DISTILATE HAVING AN ASTM D-158 FIFTY PER CENT POINT ABOVE ABOUT 300* F. BY CONTACTING SAID DISTILLATE WITH SOLID UREA, THE IMPROVED METHOD WHICH COMPRISES WETTING THE UREA WITH 0.1 TO 10% BY WEIGHT, BASED ON UREA CONTENT, OF A HYDROCARBON LIQUID BOILING BELOW ABOUT 250* F. AND THEN CONTACTING THE DISTILLATE WITH THE UREA SO WETTED.