US2731455A - Pour point reduction of petroleum oil - Google Patents

Pour point reduction of petroleum oil Download PDF

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US2731455A
US2731455A US2731455DA US2731455A US 2731455 A US2731455 A US 2731455A US 2731455D A US2731455D A US 2731455DA US 2731455 A US2731455 A US 2731455A
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urea
wax
petroleum
pour point
complex
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    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G73/00—Recovery or refining of mineral waxes, e.g. montan wax
    • C10G73/02—Recovery of petroleum waxes from hydrocarbon oils; Dewaxing of hydrocarbon oils
    • C10G73/24—Recovery of petroleum waxes from hydrocarbon oils; Dewaxing of hydrocarbon oils by formation of adducts

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  • This invention relates to new and useful improvements in the pour point reduction of petroleum oil fractions.
  • Wax-bearing oils such as lubricating oil fractions, possess a so-called pour point, i. e., that temperature at which the oil loses fluidity.
  • the pour point is conventionally determined by the well known ASTM tests such as the one designated as 697-39.
  • the reduction of the at times relatively high pour point of a wax-bearing lubricating oil fraction may be obtained either by the use of suitable additives such as, for example, aluminum stearate or other material, or by physical removal of the wax.
  • suitable additives such as, for example, aluminum stearate or other material
  • the additive performs the function of a crystallization modifier to thereby influence the pour point.
  • a large amount of wax is physically removed from the oil.
  • the use of additives may reduce the pour point of an oil to a satisfactory low point to meet relatively rigid tempera ture conditions it is, in many instances, not desired to retain in the oil appreciable quantities of wax.
  • removal of wax from the oil by mechanical operations, such as centrifuging will not ordinarily remove a sufficient quantity of the wax to give a satisfactory low pour point.
  • petroleum oil fractions and, preferably, lubricating oil fractions having a relatively high pout point for instance due to the wax contained therein are intimately contacted at a temperature of about 60-110 F. and preferably 7090 F. with urea, in amount sufficient to appreciably lower the normal pour point of said fractions, preferably at least 10 F.
  • Such urea' treatments may be conducted either as a .single batch operation or as a multiple stage treatment.
  • activator is preferably a lower alcohol not exceeding three carbon atoms in the aliphatic chain. Satisfactory activators are, for instance, methanol, ethanol, propyl and isopropyl alcohol. Methanol, however, gives particularly goodresults and is the preferred activator material. It is also of advantage to continuously stir the mix of urea and petroleum oil fraction. For best results ice the mixing should be adequate for efficient contact purposes.
  • the activator used in accordance with the practice of the invention disclosed in co-pending application Serial No. 185,691 should be preferably at least 0.5% by volume of the total volume of liquid present. Best results are obtained by an amount of activator of about 2% by volume. Amounts of activator appreciably higher than about 2% do not further increase the efiiciency of the activator. Though 2% by volume of activator material gives maximum results, it has been disclosed that l-1.5% of activator material is most practical for use in large scale operation.
  • the dewaxing capacity of the urea is partly or completely exhausted in the treatment of oil fractions, the extent of exhaustion depending upon the type, duration, number of contacts or other conditions of such treatment.
  • One object of this invention comprises the regeneration of partially or completely exhausted urea'obtained in the cloud or pour point reduction of a wax-bearing petroleum oil fraction.
  • the regeneration of the urea in accordance with the invention is carried out by contacting the exhausted or partially exhausted urea with a hot petroleum solvent and preferably in the presence of a relatively small amount of water.
  • the contacting may be carried out by mixing the urea product with the petroleum solvent, by pouring the pea troleum solvent over the urea product, or by percolating the petroleum solvent over the urea. In the latter method the petroleum solvent may be continually recovered and reused until the regeneration process is complete.
  • the petroleum solvents useful in accordance with the invention may be any of the petroleum solvents conventionally so known and designated, providing that such petroleum solvents are such that wax is soluble therein but urea is not substantially soluble therein. It is preferable that these solvents have a flash-point in excess of F. and ASTM pour point of 0 F. or lower. It is also of advantage if the petroleum solvent has a boiling point low enough so that it may be removed from the dissolved wax by distillation. Lighter fractions of petroleum oil have proved effective, and fractions of the kerosene range, preferably with a boiling point of about 375-500 F. have proved particularly effective. It is necessary that an amount of solvent sufiicient to dissolve all the wax in the urea product be used.
  • the water may be added either by suspending it in the petroleum solvent prior to use or while stirring the urea with the hydrocarbon solvent.
  • the amount of water required is inversely proportional to the temperature employed for regeneration. The higher the temperature, the less water is necessary, and vice versa.
  • the amount of water normally required for best results is one-fourth to five percent and preferably one-fourth to three percent by weight of the urea present.
  • the urea product referred to in the invention may be any urea product formed by contacting urea with a petroleum fraction to remove the wax.
  • the urea may be urea used alone or urea used in any combination.
  • This application discloses a method for dewaxing a white petroleum oil. This dewaxing of the white petroleum oil is accomplished by intimately contacting the said white petroleum oil with a composition comprising urea intimately mixed with an adsorbent.
  • This adsorbent may be 'fullers earth, silica gel, bauxite, etc.
  • this invention comprises the regeneration of a urea product, said urea product being a product obtained by mixing urea either'in combinationwith another substance, such as a petroleum adsorption product, or urea alone with a waxbearing petroleum fraction.
  • the product obtained after the regeneration in accordance with the invention is a urea product which has at least substantially the same ability to remove Wax from a wax-bearing petroleum oil fraction as new urea.
  • the urea product and the petroleum solvent may be contacted at any temperature above F. However, when temperatures above 220 F. are used, difliculties arise. Preferred temperature range in accordance with the invention is 210 F. When at least water by weight of the urea present is used, a temperature range between and 200 F. is preferred. Excellent regeneration results are obtained when, after first contacting the urea with the petroleum solvent and then separating the two, a further treatment of the urea substance with a washing solvent is performed.
  • Method for obtaining urea activated for petroleum wax-urea complex formatiom which comprises subjecting urea at least twice to the cycle of contacting urea with a wax bearing petroleum oil fraction to thereby obtain a complex between said urea and wax in said fraction, intimately contacting the resulting complex with a petroleum oil fraction of the kerosene range in amount normally sufficient to form a solution of the amount of wax carried by said urea complex, at a temperature not appreciably less than 165 F. and in the presence of about %5% of water by weight of urea, and separating the resulting urea substance.
  • Method for obtaining activated urea from a urea complex resulting from the urea contact treatment of a wax-bearing petroleum oil fraction comprising the cycle of intimately contacting such a urea complex with a petroleum oil fraction of the kerosene range in amount normally sufiicient to form a solution of the amount of wax carried by said urea complex, at a temperature not appreciably less than 165 F.

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Description

United States Patent POUR POINT REDUCTION OF PETROLEUM OIL FRACTIONS WITH ACTIVATED UREA-WAX COMPLEX No Drawing. Application September 19, 1950, Serial No. 185,692
8 Claims. (Cl. 260-96.5)
This invention relates to new and useful improvements in the pour point reduction of petroleum oil fractions.
Wax-bearing oils, such as lubricating oil fractions, possess a so-called pour point, i. e., that temperature at which the oil loses fluidity. The pour point is conventionally determined by the well known ASTM tests such as the one designated as 697-39.
The reduction of the at times relatively high pour point of a wax-bearing lubricating oil fraction may be obtained either by the use of suitable additives such as, for example, aluminum stearate or other material, or by physical removal of the wax. In the former at least a portion of the wax remains largely in the oil and the additive performs the function of a crystallization modifier to thereby influence the pour point. In the mechanical wax separation for the reduction of pour point, a large amount of wax is physically removed from the oil. Though the use of additives may reduce the pour point of an oil to a satisfactory low point to meet relatively rigid tempera ture conditions it is, in many instances, not desired to retain in the oil appreciable quantities of wax. Alternatively, removal of wax from the oil by mechanical operations, such as centrifuging, will not ordinarily remove a sufficient quantity of the wax to give a satisfactory low pour point.
Co-pending application, Serial No. 185,691 filed September 19, 1950, discloses the lowering of the relatively high pour point of a lubricating oil fraction permitting the obtaining of appreciably lowered pour points and preferably pour points lowered by at least 10 F.
In accordance with this disclosure petroleum oil fractions and, preferably, lubricating oil fractions having a relatively high pout point for instance due to the wax contained therein, are intimately contacted at a temperature of about 60-110 F. and preferably 7090 F. with urea, in amount sufficient to appreciably lower the normal pour point of said fractions, preferably at least 10 F.
Such urea' treatments may be conducted either as a .single batch operation or as a multiple stage treatment.
In most cases, and particularly when using a single batch treatment, up to about 50% by weight of urea calculated on the amount of oil fraction present, and preferably 35% by Weight of urea, give satisfactory results reducing the pour point in most cases appreciably more than by 10 F. When using the multiple stage treatment it is possible to use lesser amounts of urea and obtain a more economical operation with substantially the same pour point reducing efficiency.
It is in most cases necessary to add a suitable activator while the urea treatment of the oil fraction is proceeding. Such activator is preferably a lower alcohol not exceeding three carbon atoms in the aliphatic chain. Satisfactory activators are, for instance, methanol, ethanol, propyl and isopropyl alcohol. Methanol, however, gives particularly goodresults and is the preferred activator material. It is also of advantage to continuously stir the mix of urea and petroleum oil fraction. For best results ice the mixing should be adequate for efficient contact purposes.
The activator used in accordance with the practice of the invention disclosed in co-pending application Serial No. 185,691 should be preferably at least 0.5% by volume of the total volume of liquid present. Best results are obtained by an amount of activator of about 2% by volume. Amounts of activator appreciably higher than about 2% do not further increase the efiiciency of the activator. Though 2% by volume of activator material gives maximum results, it has been disclosed that l-1.5% of activator material is most practical for use in large scale operation.
As shown in said co-pending application the dewaxing capacity of the urea is partly or completely exhausted in the treatment of oil fractions, the extent of exhaustion depending upon the type, duration, number of contacts or other conditions of such treatment.
One object of this invention comprises the regeneration of partially or completely exhausted urea'obtained in the cloud or pour point reduction of a wax-bearing petroleum oil fraction.
The foregoing and further objects of the invention will be apparent from the following description.
The regeneration of the urea in accordance with the invention is carried out by contacting the exhausted or partially exhausted urea with a hot petroleum solvent and preferably in the presence of a relatively small amount of water.
The contacting may be carried out by mixing the urea product with the petroleum solvent, by pouring the pea troleum solvent over the urea product, or by percolating the petroleum solvent over the urea. In the latter method the petroleum solvent may be continually recovered and reused until the regeneration process is complete.
The petroleum solvents useful in accordance with the invention may be any of the petroleum solvents conventionally so known and designated, providing that such petroleum solvents are such that wax is soluble therein but urea is not substantially soluble therein. It is preferable that these solvents have a flash-point in excess of F. and ASTM pour point of 0 F. or lower. It is also of advantage if the petroleum solvent has a boiling point low enough so that it may be removed from the dissolved wax by distillation. Lighter fractions of petroleum oil have proved effective, and fractions of the kerosene range, preferably with a boiling point of about 375-500 F. have proved particularly effective. It is necessary that an amount of solvent sufiicient to dissolve all the wax in the urea product be used. In most cases amounts of petroleum solvent of at least twice the volume of the urea product to be regenerated, are needed, and preferably volumes of the petroleum solvent equaling at least three times the volume of the urea product to be regenerated, are needed. When the petroleum solvent is used alone to regenerate the urea (that is, without the presence of water) it is necessary to carry the operation out at temperatures of about 200 F. or higher. However, this procedure has several disadvantages, in that decomposition accompanied by discoloration of the urea products result at these high temperatures. It is also found' carried out at lower temperatures, preferably at tempera" tures from 180200 F. over a relatively short period of time, usually 30-45 minutes, if a relatively small amount of water is present. The water may be added either by suspending it in the petroleum solvent prior to use or while stirring the urea with the hydrocarbon solvent. The amount of water required is inversely proportional to the temperature employed for regeneration. The higher the temperature, the less water is necessary, and vice versa. The amount of water normally required for best results is one-fourth to five percent and preferably one-fourth to three percent by weight of the urea present.
Thus, while it is possible to carry out the regeneration of the urea without the presence of water, in most cases it is highly desirable, depending upon requirements or conditions dictated by desired freedom from decomposition or facility of operations, to include water.
The following example is furnished by way of illustration, but not of limitation:
EXAMPLE 300 grams of an oil having the'following characteristics (flash F. 420, viscosity 210 F. 45 seconds, ASTM cloud point 50 F., ASTM pour point 40 F.) was contacted with 100 grams of urea in the presence of 5 cc. of methyl alcohol for 45 minutes at a temperature of 70 F. The slurry was then filtered over a Buchner funnel and the filtrate (dewaxed oil) tested for cloud and pour points. The filter cake was suspended in about three times its weight of a kerosene range oil having a fiash point of 220 F. and pour point below F. One cubic centimeter of water was added and the resulting mixture agitated at a temperature of 180-190 F.'for
Cloud Point Pour Point of Treated oi Taeiited Treatment Cycle No.
Oil
l cocoocoooccacscoooomm The urea product referred to in the invention may be any urea product formed by contacting urea with a petroleum fraction to remove the wax. The urea may be urea used alone or urea used in any combination. This includes urea used in the urea adsorbent composition described in co-pending application, Serial No. 185,693. This application discloses a method for dewaxing a white petroleum oil. This dewaxing of the white petroleum oil is accomplished by intimately contacting the said white petroleum oil with a composition comprising urea intimately mixed with an adsorbent. This adsorbent may be 'fullers earth, silica gel, bauxite, etc.
It may thus be seen from the foregoing that this invention comprises the regeneration of a urea product, said urea product being a product obtained by mixing urea either'in combinationwith another substance, such as a petroleum adsorption product, or urea alone with a waxbearing petroleum fraction. The product obtained after the regeneration in accordance with the invention is a urea product which has at least substantially the same ability to remove Wax from a wax-bearing petroleum oil fraction as new urea. After the urea product has been regenerated several times it has the ability to remove wax from a wax-bearing petroleum oil fraction superior to that of new urea and is ready to be used again for additional dewaxing operations.
The urea product and the petroleum solvent may be contacted at any temperature above F. However, when temperatures above 220 F. are used, difliculties arise. Preferred temperature range in accordance with the invention is 210 F. When at least water by weight of the urea present is used, a temperature range between and 200 F. is preferred. Excellent regeneration results are obtained when, after first contacting the urea with the petroleum solvent and then separating the two, a further treatment of the urea substance with a washing solvent is performed.
We claim:
1. Method for obtaining urea activated for petroleum wax-urea complex formatiomwhich comprises subjecting urea at least twice to the cycle of contacting urea with a wax bearing petroleum oil fraction to thereby obtain a complex between said urea and wax in said fraction, intimately contacting the resulting complex with a petroleum oil fraction of the kerosene range in amount normally sufficient to form a solution of the amount of wax carried by said urea complex, at a temperature not appreciably less than 165 F. and in the presence of about %5% of water by weight of urea, and separating the resulting urea substance.
2. Method for obtaining activated urea from a urea complex resulting from the urea contact treatment of a wax-bearing petroleum oil fraction, comprising the cycle of intimately contacting such a urea complex with a petroleum oil fraction of the kerosene range in amount normally sufiicient to form a solution of the amount of wax carried by said urea complex, at a temperature not appreciably less than 165 F. and in the presence of about A--5% of water by weight of urea, and separating the resulting urea substance, thereafter contacting the latter with a wax-bearing petroleum oil fraction to thereby obtain a complex between said separated urea and wax in said last mentioned fraction and thereafter subjecting said last mentioned complex to the contacting and separating steps of said cycle.
3. Method in accordance with claim 2 in which said intimate contact is carried out at a temperature ranging from 165-220 F.
4. Method in accordance with claim 2 in which said intimate contact is carried out at a temperature ranging from l75-210 F.
5. Method in accordance with claim 2 in which said intimate contact is carried out at a temperature ranging from 180-200 F.
6. Method in accordance with claim 2 in which said intimate contact is carried out at a temperature ranging from 175-210 F. and said urea complex is a urea complex obtained by intimately contacting urea and an adsorbent with a petroleum fraction.
7. Method in accordance withclaim 2 in which said petroleum oil fraction of the kerosene range is present in amount equalling at least two times the volume of said urea product and in which said intimate contacting is carried out at a temperature ranging between about 180-200 F.
8. Method in accordance with claim 2 in which said recovery of. the said regenerated urea substance includes the separation of the petroleum oil fraction of the kerosene range and the said urea substance and one further treatment of the urea substance with a washing solvent.
(References on following page) Yul References Cited in the file of this patent UNITED STATES PATENTS Fetterly Mar. 7, 1950 Garner Aug. 15, 1950 5 Fetterly Aug. 29, 1950 Fetterly -1 Aug. 29, 1950 Arabian ct a]. Mar. 27, 1951 Adams et a1. Mar. 11, 1952 Fettarly Oct. 7, 1952 Gross Mar. 17, 1953 Fetterly June 16, 1953

Claims (1)

1. METHOD FOR OBTAINING UREA ACTIVATED FOR PETROLEUM WAX-UREA COMPLEX FORMATION, WHICH COMPRISES SUBJECTING UREA AT LEAST TWICE TO THE CYCLE OF CONTACTING UREA WITH A WAX BEARING PETROLEUM OIL FRACTION TO THEREBY OBTAIN A COMPLEX BETWEEN SAID UREA AND WAX IN SAID FRACTION, INTIMATELY CONTACTING THE RESULTING COMPLEX WITH A PETROLEUM OIL FRACTION OF THE KEROSENE RANGE IN AMOUNT NORMALLY SUFFICIENT TO FORM A SOLUTION OF THE AMOUNT OF WAX CARRIED BY SAID UREA COMPLEX, AT A TEMPERATURE NOT APPRECIABLY LESS THAN 165* F. AND IN THE PRESENCE OF ABOUT 1/4-5% OF WATER BY WEIGHT OF UREA, AND SEPARATING THE RESULTING UREA SUBSTANCE.
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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2861941A (en) * 1958-11-25 Urea-dewaxing lubricating oil
US2862868A (en) * 1958-12-02 Production of low cold-test oils
US2879220A (en) * 1959-03-24 Method of separating mixtures of organic compounds
US2890161A (en) * 1959-06-09 Production of low cold-test oils using urea
US2913390A (en) * 1959-11-17 Urea-dewaxing method for producing low cold-test oils
US3133011A (en) * 1960-02-05 1964-05-12 Process for the production of readily
US4070269A (en) * 1976-10-12 1978-01-24 Suntech, Inc. Urea adduction process for refrigeration oil manufacture

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2499820A (en) * 1947-02-21 1950-03-07 Thiourea-hydrocarbon complexes
US2518677A (en) * 1950-08-15 Separation of hydrocarbons using
US2520715A (en) * 1947-03-29 1950-08-29 Method of separating organic
US2520716A (en) * 1950-08-29 Method of separating organic com
US2546328A (en) * 1948-09-27 1951-03-27 Shell Dev Carnauba wax substitute
US2588602A (en) * 1952-03-11 Fractionation of organic compounds
US2613204A (en) * 1952-10-07 of urea
US2632002A (en) * 1953-03-17 Countercurkent sltjbb
US2642377A (en) * 1947-10-27 1953-06-16 Shell Dev Dewaxing process

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2518677A (en) * 1950-08-15 Separation of hydrocarbons using
US2520716A (en) * 1950-08-29 Method of separating organic com
US2588602A (en) * 1952-03-11 Fractionation of organic compounds
US2613204A (en) * 1952-10-07 of urea
US2632002A (en) * 1953-03-17 Countercurkent sltjbb
US2499820A (en) * 1947-02-21 1950-03-07 Thiourea-hydrocarbon complexes
US2520715A (en) * 1947-03-29 1950-08-29 Method of separating organic
US2642377A (en) * 1947-10-27 1953-06-16 Shell Dev Dewaxing process
US2546328A (en) * 1948-09-27 1951-03-27 Shell Dev Carnauba wax substitute

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2861941A (en) * 1958-11-25 Urea-dewaxing lubricating oil
US2862868A (en) * 1958-12-02 Production of low cold-test oils
US2879220A (en) * 1959-03-24 Method of separating mixtures of organic compounds
US2890161A (en) * 1959-06-09 Production of low cold-test oils using urea
US2913390A (en) * 1959-11-17 Urea-dewaxing method for producing low cold-test oils
US3133011A (en) * 1960-02-05 1964-05-12 Process for the production of readily
US4070269A (en) * 1976-10-12 1978-01-24 Suntech, Inc. Urea adduction process for refrigeration oil manufacture

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