US2367362A - Lubricating oil manufacture - Google Patents

Lubricating oil manufacture Download PDF

Info

Publication number
US2367362A
US2367362A US435109A US43510942A US2367362A US 2367362 A US2367362 A US 2367362A US 435109 A US435109 A US 435109A US 43510942 A US43510942 A US 43510942A US 2367362 A US2367362 A US 2367362A
Authority
US
United States
Prior art keywords
wax
oil
lubricating oil
sulfurized
bearing
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US435109A
Inventor
Frederic C Mccoy
Charles C Towne
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Texaco Inc
Original Assignee
Texaco Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Texaco Inc filed Critical Texaco Inc
Priority to US435109A priority Critical patent/US2367362A/en
Application granted granted Critical
Publication of US2367362A publication Critical patent/US2367362A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G73/00Recovery or refining of mineral waxes, e.g. montan wax
    • C10G73/02Recovery of petroleum waxes from hydrocarbon oils; Dewaxing of hydrocarbon oils
    • C10G73/04Recovery of petroleum waxes from hydrocarbon oils; Dewaxing of hydrocarbon oils with the use of filter aids
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G73/00Recovery or refining of mineral waxes, e.g. montan wax
    • C10G73/02Recovery of petroleum waxes from hydrocarbon oils; Dewaxing of hydrocarbon oils
    • C10G73/06Recovery of petroleum waxes from hydrocarbon oils; Dewaxing of hydrocarbon oils with the use of solvents

Definitions

  • the wax crystal modifier of this invention may be prepared from a sperm oil having a specific gravity of about 0378-0384 (60/60 F.), a Saybolt Universal viscosity at 100 F. of about 95 to 110 and a saponification number of 125 to 135.
  • the resulting sulfurized sperm oil will have an A. P. I. gravity of about 15.1, a Saybolt Universal viscosity at 210 F. of about 219 and a pour point temperature of about 55 F. and will contain. about 10% of combined sulfur.
  • the product is; substantially free from fatty acids and glyceride s i It thus consists essentially of a sulfurized fat containing about 10% combined sulfur.
  • a small amount of this sulfurized sperm oil was added to a partially dewaxed residual lubricating oil stock, the amount added being about 3% by weight of the partially dewaxed lubricating oil stock.
  • the residual lubricating oil stock had the following ap proximate characteristics: 1
  • the invention is of particular advantage in reducing the pour point of partially dewaxed residual oil or of residual type oils which, in the absence of an added modifier, have a pour point not exceeding about 25 F.-
  • the modifier may be used as a dewaxing aid.
  • the waxbearing oil-to be dewaxed is advantageously mixed with a suitable diluent or dewaxing solvent and chilled to a dewaxing temperature at which the wax is precipitated in solid form. The precipitated. wax is then separated from the chilled mixture in the presence of a small amount of the modifier or regulator substance, the separation advantageously being effected by filtration.
  • the modifier is usually incorporated in the wax-'bearing oil or a diluted wax-bearing oil mixture prior to chi1ling, the amount so added ranging from about'a fraction of a per cent to 3 or 5% by weight of the wax-bearing oil charged.
  • the dewaxing operation may be carried out so as to effect only partial removal of the wax, as,
  • customary diluents or solvents employed may comprise low boiling hydrocarbons, either normally gaseous or normally liquid or selective solvent mixtures such as mixtures of aliphatic ketones and aromatic hydrocarbons including benzol and toluol.
  • sulfurized sperm oil has been specifically described, nevertheless it is contemplated that other sulfurized neutral mono-esters of fatty acids may be employed such as methyl and ethyl oleates, glycol oleate, butyl stearate, isopropyl stearate, etc.
  • the steps comprising diluting and chilling the wax-bearing oil to a temperature at which waxis precipitated therefrom, and separating the precipitated wax from the mixture in the presence of a small quantity, not in excess of 3 to 5% by weight of the wax-bearing oil, of a wax crystal modifier weight of the wax-hearing oil, of a wax crystal modifier consisting essentially of a sulfurized non-glyceride fat containing about 10% combined sulfur.

Description

Patented Jan. 16, 1945 um'rno STATE s PATENT or ies."
LUBRICATING OIL MANUFACTURE Frederic C. McCoy and Charles C. Towne, Beacon, N. Y., assignors to The Texas Company, New York, N. Y., a corporation of Delaware No Drawing. Application March 17, 1942,
Serial No. 435,109
scl ims, ,(01. 196-18) V wax crystal modifier or regulator effective for.
either reducing the pour point of wax-bearing oil or facilitating separation of wax from the oil' or both, a substance consisting essentially, of sulfurized esters of fatty acids and particularly sulfulrized non-glyceride fatty material such as sperm oi It has been proposed heretofore to employ sulfurized materials as additives to oil for the pur-' pose of imparting oiliness and other characteristics. However, it has now been discovered that sulfurized esters of fatty acids and particularly sulfurized sperm oil possess the ability to modify or regulate wax crystal structure in wax-bearing oils. The addition of this material to wax-bearing oil and particularly to residual wax-bearing oils of relatively low wax content inhibits wax crystal growth and renders the wax crystals more dense. Reduction in crystal size, or increasing the density of the wax crystals in lubricating oil stocks permits the oil to pour at lower temperatures and also facilitates separation of the wax from a chilled dilute wax-bearing oil mixture by filtration.
The wax crystal modifier of this invention may be prepared from a sperm oil having a specific gravity of about 0378-0384 (60/60 F.), a Saybolt Universal viscosity at 100 F. of about 95 to 110 and a saponification number of 125 to 135.
Sperm oil of the foregoing characteristics is re acted with suitable amounts of sulfur at temperatures in the range about 300 to 385 F., the re:-
action being continueduntil the sulfur is combined in the form of neutral organic sulfur compounds.
The resulting sulfurized sperm oil will have an A. P. I. gravity of about 15.1, a Saybolt Universal viscosity at 210 F. of about 219 and a pour point temperature of about 55 F. and will contain. about 10% of combined sulfur. The product is; substantially free from fatty acids and glyceride s i It thus consists essentially of a sulfurized fat containing about 10% combined sulfur. By way of specific example, a small amount of this sulfurized sperm oil was added to a partially dewaxed residual lubricating oil stock, the amount added being about 3% by weight of the partially dewaxed lubricating oil stock. The residual lubricating oil stock had the following ap proximate characteristics: 1
Gravity A. P. T I 25.0 Saybolt Universal viscosity at 210 94 Pour point, F
The addition of 3% sulfurized sperm oil to this 'oil resulted in reducing the pour point to about minus 15 to minus 20 F. In other words, there was areduction of about 15 to 20 in pour point this material to the oil. Thus, this modifier appears to be superior to many substances proposed heretofore since it is quite effective in reducing the pour point of residual lubricating oil stocks.
It is therefore contemplated that the invention is of particular advantage in reducing the pour point of partially dewaxed residual oil or of residual type oils which, in the absence of an added modifier, have a pour point not exceeding about 25 F.-
It is alsocontemplated that the modifier may be used as a dewaxing aid. In such case the waxbearing oil-to be dewaxed is advantageously mixed with a suitable diluent or dewaxing solvent and chilled to a dewaxing temperature at which the wax is precipitated in solid form. The precipitated. wax is then separated from the chilled mixture in the presence of a small amount of the modifier or regulator substance, the separation advantageously being effected by filtration.
In a dewaxing operation of this character the modifier is usually incorporated in the wax-'bearing oil or a diluted wax-bearing oil mixture prior to chi1ling, the amount so added ranging from about'a fraction of a per cent to 3 or 5% by weight of the wax-bearing oil charged.
The dewaxing operation may be carried out so as to effect only partial removal of the wax, as,
for example, dewaxing at a temperature of about 0 to minus 10 F., advantage being taken of the pour depressing effect of modifying material remaining in the oil from which the wax has been separated to depress the pour point still further.
Such dewaxing operations can be carried out using conventional solvents and conventional methods of wax separation which are now well known and understood in the art so that a detailed description thereof is unnecessary. For example, customary diluents or solvents employed may comprise low boiling hydrocarbons, either normally gaseous or normally liquid or selective solvent mixtures such as mixtures of aliphatic ketones and aromatic hydrocarbons including benzol and toluol.
While sulfurized sperm oil has been specifically described, nevertheless it is contemplated that other sulfurized neutral mono-esters of fatty acids may be employed such as methyl and ethyl oleates, glycol oleate, butyl stearate, isopropyl stearate, etc.
Obviously many modifications and variations of the invention, as hereinbefore set forth, may be made without departing from the spirit and scope thereof, and therefore only such limitations should be imposed as are indicated in the appended claims.
We claim:
1. In the manufacture of low pour test lubricating oil from wax-bearing oil, the steps comprising diluting and chilling the wax-bearing oil to a temperature at which wax is precipitated therefrom, and separating the precipitated wax from the mixture by filtration in the presence of a small quantity, not in excess of 3 to 5% by weight of the wax-bearing oil, of a wax crystal modifier consisting essentially of a sulfurized mono-ester of a fatty acid.
2. In the manufacture of low pour test lubricating oil from wax-bearing oil, the steps comprising diluting and chilling the wax-bearing oil to a temperature at which waxis precipitated therefrom, and separating the precipitated wax from the mixture in the presence of a small quantity, not in excess of 3 to 5% by weight of the wax-bearing oil, of a wax crystal modifier weight of the wax-hearing oil, of a wax crystal modifier consisting essentially of a sulfurized non-glyceride fat containing about 10% combined sulfur.
FREDERIC C. MCCOY. CHARLES C. TOV/NE.
US435109A 1942-03-17 1942-03-17 Lubricating oil manufacture Expired - Lifetime US2367362A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US435109A US2367362A (en) 1942-03-17 1942-03-17 Lubricating oil manufacture

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US435109A US2367362A (en) 1942-03-17 1942-03-17 Lubricating oil manufacture

Publications (1)

Publication Number Publication Date
US2367362A true US2367362A (en) 1945-01-16

Family

ID=23727022

Family Applications (1)

Application Number Title Priority Date Filing Date
US435109A Expired - Lifetime US2367362A (en) 1942-03-17 1942-03-17 Lubricating oil manufacture

Country Status (1)

Country Link
US (1) US2367362A (en)

Similar Documents

Publication Publication Date Title
US2296037A (en) Cutting oil
US2367362A (en) Lubricating oil manufacture
US2444720A (en) Manufacture of lithium base greases
US2701783A (en) Process for the production of a high quality lube oil
US2723941A (en) Wax fractionation process
US2183783A (en) Lubricating oil
US2392891A (en) Stable sulphurized oils and the method of preparing same
US2067050A (en) Dewaxing hydrocarbon oil
US2118915A (en) Manufacture of wax acids
US2257890A (en) Lubricating composition
US2658852A (en) Method of manufacturing low melting point plastic waxes
US2119718A (en) Lubricating oil
US2198562A (en) Method of making sulphurized
US2654693A (en) Dewaxing mineral oil
US2608517A (en) Dewaxing process using filter aid
US2181638A (en) Dewaxing of mineral oils
US2150400A (en) Lubricating oil composition
US2037563A (en) Mineral oil composition
US2211163A (en) Lubricating oil composition
GB679173A (en) Improvements in or relating to the separation of wax from hydrocarbon mixtures
US2411502A (en) Treatment of mineral oils
US2081518A (en) Lowering pour point of oil
US2139668A (en) Oil composition
US2141626A (en) Solvent refining hydrocarbon oil
US2060805A (en) Dewaxing of lubricating oil