US2256603A - Processing with nonstainingcom - Google Patents

Processing with nonstainingcom Download PDF

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US2256603A
US2256603A US2256603DA US2256603A US 2256603 A US2256603 A US 2256603A US 2256603D A US2256603D A US 2256603DA US 2256603 A US2256603 A US 2256603A
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M1/00Liquid compositions essentially based on mineral lubricating oils or fatty oils; Their use as lubricants
    • C10M1/08Liquid compositions essentially based on mineral lubricating oils or fatty oils; Their use as lubricants with additives
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2205/00Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions
    • C10M2205/02Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions containing acyclic monomers
    • C10M2205/026Butene
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    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/10Carboxylix acids; Neutral salts thereof
    • C10M2207/12Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms
    • C10M2207/125Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms having hydrocarbon chains of eight up to twenty-nine carbon atoms, i.e. fatty acids
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/10Carboxylix acids; Neutral salts thereof
    • C10M2207/12Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms
    • C10M2207/129Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms having hydrocarbon chains of thirty or more carbon atoms
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    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/28Esters
    • C10M2207/281Esters of (cyclo)aliphatic monocarboxylic acids
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/28Esters
    • C10M2207/282Esters of (cyclo)aliphatic oolycarboxylic acids
    • CCHEMISTRY; METALLURGY
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    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/28Esters
    • C10M2207/283Esters of polyhydroxy compounds
    • CCHEMISTRY; METALLURGY
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    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/28Esters
    • C10M2207/286Esters of polymerised unsaturated acids
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/40Fatty vegetable or animal oils
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/40Fatty vegetable or animal oils
    • C10M2207/404Fatty vegetable or animal oils obtained from genetically modified species
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2040/00Specified use or application for which the lubricating composition is intended
    • C10N2040/20Metal working
    • C10N2040/24Metal working without essential removal of material, e.g. forming, gorging, drawing, pressing, stamping, rolling or extruding; Punching metal
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2040/00Specified use or application for which the lubricating composition is intended
    • C10N2040/20Metal working
    • C10N2040/241Manufacturing joint-less pipes
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    • C10N2040/00Specified use or application for which the lubricating composition is intended
    • C10N2040/20Metal working
    • C10N2040/242Hot working
    • CCHEMISTRY; METALLURGY
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    • C10N2040/00Specified use or application for which the lubricating composition is intended
    • C10N2040/20Metal working
    • C10N2040/243Cold working
    • CCHEMISTRY; METALLURGY
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    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2040/00Specified use or application for which the lubricating composition is intended
    • C10N2040/20Metal working
    • C10N2040/244Metal working of specific metals
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2040/00Specified use or application for which the lubricating composition is intended
    • C10N2040/20Metal working
    • C10N2040/244Metal working of specific metals
    • C10N2040/245Soft metals, e.g. aluminum
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2040/00Specified use or application for which the lubricating composition is intended
    • C10N2040/20Metal working
    • C10N2040/244Metal working of specific metals
    • C10N2040/246Iron or steel
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
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    • C10N2040/00Specified use or application for which the lubricating composition is intended
    • C10N2040/20Metal working
    • C10N2040/244Metal working of specific metals
    • C10N2040/247Stainless steel

Definitions

  • This invention relates to operations in working and forming structural solid articles from fusible materials, such as metals, with the aid of Volatile oils. More particularly, it is concerned with the utilization in these operations of improved oil compositions.
  • Roll oils, drawing compounds, and die swabbing oils which have been in use up until now have the disadvantage of leaving on the annealed articles dark stains.
  • This stain formation evidently results from a thermal decomposition of oil on the surface of the metal article when it is treated at an annealing temperature even in a non-x1 dizing atmosphere, but it does not appear to be a function of the carbon content of the oil, since with conventional oil products approximately the same degree of staining is obtained with a parafi'inic as witha naphthenicbase oil of thesame viscosity.
  • a piece of tough, pliable metal is passed between a train of cylindrical: rolls constructed of chilled iron or steel.
  • the rolls are set one above the other with their axes parallel and held in housings sothat there is a fixed spaced between them.
  • the upper and lower rolls are so connected as 'to rotate in oppositev directions and the space between these rolls' is adjusted so that the rolls exert a high compression on the metal piece passed between them.
  • this invention provides nonstaining oil compositions to be applied to the surface of theprocessingapparatus and the material being worked or formed.
  • this invention provides oil compositions which have satisfactory viscosity, oiliness, and load bearing characteristics for use in the mechanical forming operations and which leave no objectionable stain on the articles after they have been heated to an elevated temperature in an annealing treatment
  • j I v Compositions which are used according to the present invention for a cold working of metals prior to an annealing treatment comprise preferably petroleum distillates of lower boiling range than lubricating oils and a sufiicient amount of polybutenes of high molecular weight to confer upon the composition viscosity, consistency, and filming characteristics necessary for any given metal Working condition.
  • An oiliness agent such as a fatty ester, a fatty oil, a vegetable oil, or a soap maybeadded me minor amount to the composition to give improved oiliness.
  • the high molecular weight polybutene ingredient is the product obtainable byp-olymerizing isobutene at a low temperature, for instance below -10 Crand preferably below 40 C. with centages of oiliness agents to help preventstickthe aid of a catalyst, such as boron fluoride, In
  • polybutenes are essentially derived from isobutene, but varying V quantities ,of normal butenes may be present, also, other low molecular weight hydrocarbons which act as 'diluents. variations of this procedure and other iso-olefin reactants,-e. g. isopentene, whichmaybeused to form polymers possessing similar physical and chemical properties in general.
  • the poly-Q mers of 'iso-olefins are'consideredto be linearv type polymers of a homologous series and be con-Q j stituted of recurring branched alkene units, vizz"
  • these polymers may be called appropri ately polyalkenes or polyisoalkenes. They have V a low iodine number and a hydrogen to carbon ratio of about 2.0, which indicates; that .on an average no more than one. double bond is present in each polymer molecule; v i
  • a naphtha boiling in the range from about 300 F. to 500 F., akerosene fraction boiling from 350 F. to 600 R, or a mineral seal oil boiling from about 450 F.
  • the minimum distillation point isadvisably above about 300 E. mainlyxas a safeguard against fire hazards, since as ,a safety measure the composition is generally re- :quired to have a minimum flash point nolower than 100 F.
  • the petroleum oil distillate used as the basef-or the composition maycome from pounds characterized by structures of long chains zof saturated'carbon atoms, a number of which are attachedto azrecurring organic radical'by a unsaturated-aliphatic radical and an-arrangement which predisposes themolecules'to unite into a longchain of carbon atoms, all of which with a 'possible exception of a-terminal pair of carbon atoms are saturated and with alternate individual or pairs of carbon'atoms in the chain linked to 'alkyl radicals.
  • V "A' polybutene product varies in consistency from-viscous liquids to tough, elastic'solids as the average molecular weight of the polymers in-' creases from about 1000- to 200,000 or higher 1
  • the transition from liquid to solid consistency occurs when the average'molecular weight of the polymersis in theneighborhood of- 27,000 determined by the viscosity method; Beginning] at this pointof transition the polymers also acquire a pronouncedstringiness- It has been-found that "for more satisfactory results, the polybu tenes with molecular weights ranging above about 27,000'are preferred, since they make an oil composition moreresistant to shock, diminish the throwing off by centrifugal force, and increase the load bearing capacityof the-oil composition.
  • a petroleum distillate base used for the. composition may besee- .lected advantageously from a class of petroleum lany type of crude and be produced by any of the well known methods of refining, because, in genera1, such light fractions all'are refractory. to decomposition by heat to a highdegree.
  • This composition has a viscosity of 99 Saybolt Universalgseconds at 100 F. and a boiling range of 510 -620 FJat atmospheric pressure; V Y r
  • satisfactory non-staining'roll oils are compounded, to containabove of a volatile, non-"viscous petroleum base oil and about 0.5 to 10%tof the viscid-polybutenes, which give the blend-a viscosity ranging from 55 to about;300
  • Wires 'andbther structural shapes mayi'vary widelyin consistency, but are generally-required to b'e more viscous than roll oils and even semifluid; Furthermore; they may frequentlyrequire as ingredients materials which impart additional 7 oilinessor film strength characteristics.
  • nonestaining drawing compound oi semi-fluid consistency contains 15,3%-ot poly-'- but'enes havingaverage molecular weights of*50,:-
  • satisfactory drawing compounds may contain from about 5% to about of high molecular weight polybutenes.
  • compositions provided by this invention possess great merit in the metal fabrication processes for obtaining smooth and clean
  • the step which comprises bringing between surfaces of the article being processed and the shaping apparatus that tends to contact with said article a non-staining oil composition comprising high molecular Weight polymeric homologous compounds characterized by structures of long chains of saturated carbon atoms, of which a number have a carbon to carbon link to a recurring organic radical.
  • a non-staining oil composition comprising a volatile petroleum oil distillate having a maximum boiling point of not more than about 750 F. and a minor proportion of polyalkenes having an average molecular weight above 1,000.
  • said oil composition comprises a petroleum oil distillate boiling in the range of 300 F. to 750 F., and a suiiicient quantity of polybutenes to give the composition a viscosity above about 55 Saybolt seconds at 100 F.
  • a method of improving the finish of a shaped metal article which is produced by cold rolling and a subsequent annealing treatment which comprises wetting the surfaces of the article as it is being cold rolled with an oil composition containing high molecular weight polybutenes and a petroleum distillate boiling below 750 F.
  • a method of improving the finish of a shaped metal article produced by die drawing which comprises coating a metal piece as it is being drawn with a non-staining drawing compound containing a major proportion of a petroleum.
  • the step of applying to the surface of the metal being rolled a non-staining oil composition comprising above of a petroleum distillate boiling substantially in the range of 300 to 620 F. blended with a sufiicient proportion of viscid polybutenes having an average molecular weight above 27,000 to give the blend a viscosity ranging from 55 to 300 Saybolt Universal seconds at F.
  • the method of improving the finish of the shaped article which comprises the step of applying to the die a non-staining oil composition comprising a petroleum distillate boiling substantially in the range of 300 F. to 750 F. blended with a minor proportion of viscid polybutenes in sufficient amount to give the oil a viscosity above 55 Saybolt Universal seconds at DONALD L. WRIGHT.

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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)
  • Lubricants (AREA)

Description

ferrous industries. 7 commonly almost 100% petroleum o'ils ini'com- Patented Sept. 23, 1941 UNi'rs PROCESSING WITH NONSTAINING COM- POUNDS Donald L. Wright, Westfield, N. J., assignor to Standard Oil Development Company, a corporation of Delaware No Drawing. Application December 21, 1939,
Serial No. 310,469
8 Claims; (01. 205-221 This invention relates to operations in working and forming structural solid articles from fusible materials, such as metals, with the aid of Volatile oils. More particularly, it is concerned with the utilization in these operations of improved oil compositions.
In the fabrication of ferrous metals, non-ferrous metals, and other fusible materials, the use of oil compositions as a medium between the surfaces of the working apparatus and the article being worked to produce an improved finish on the product plays an important part. For example, the cold rolling of steel, brass, aluminum, copper, or the like, is benefitted to a greater:- tent by having a film of oil between the rolls and the metal piece being shaped. The oil tends to make the surface of the shaped article smoother, to prevent overheating, and to avoid the picking up of particles by the rolls from the material being Worked. Similar functions are performed by the oil in metal drawing and die pressing, and die forging operations. In each case there has been considerable difiiculty in the removal of decomposition products of the oils'f'rom the processed articles after they have been-annealed-.
Roll oils, drawing compounds, and die swabbing oils which have been in use up until now have the disadvantage of leaving on the annealed articles dark stains. This stain formation evidently results from a thermal decomposition of oil on the surface of the metal article when it is treated at an annealing temperature even in a non-x1 dizing atmosphere, but it does not appear to be a function of the carbon content of the oil, since with conventional oil products approximately the same degree of staining is obtained with a parafi'inic as witha naphthenicbase oil of thesame viscosity. There is evidence that the distillation and heat stability characteristics of a lubricant are important factors in: the degree of staining left by what seems to be a cracking and polymer izin of the oil during the annealing processat highly elevated temperatures ranging-up to about Conventionaloil' roducts-now. in use as. roll oils have certain minimum viscosity and. load bearing. requirements which usually cannot be successfully met by lubricating oils of visco'sities lower than 55-60 .Saybolt Universal seconds at 100 F. for the non-ferrous metal industries and 90-100 Saybolt Universal seconds at 100 F. for Such oil products have been position but may, 'on occasion, contain small per ing of the rolls to the processed metal and to provide smoother metal surfaces. 7
In the usual production of rolled metalshapes,
a piece of tough, pliable metal is passed between a train of cylindrical: rolls constructed of chilled iron or steel. The rolls are set one above the other with their axes parallel and held in housings sothat there is a fixed spaced between them. The upper and lower rolls are so connected as 'to rotate in oppositev directions and the space between these rolls' is adjusted so that the rolls exert a high compression on the metal piece passed between them.
Ina drawing operation, a metal bar is compressed and elongated bybeing drawn through a tapering hole, whereby a smoothly finished product of reduced cross section is formed. To accomplish this, operation more efficiently, it is the usual practice to have the piece enter the. die coated, with a lubricating medium or drawing compound. Many types ofcompounds have been in use for this purpose, and it has been found that unless the compound gives satisfactory lubrication, the die scratches the work and quickly becomes rough. For this reason, special quality petroleum oils and greases have generally been adopted. 7
It is an objectofthis inventionto provide nonstaining oil compositions to be applied to the surface of theprocessingapparatus and the material being worked or formed. In a more specific sense, this invention provides oil compositions which have satisfactory viscosity, oiliness, and load bearing characteristics for use in the mechanical forming operations and which leave no objectionable stain on the articles after they have been heated to an elevated temperature in an annealing treatment, j I v Compositions which are used according to the present invention for a cold working of metals prior to an annealing treatment comprise preferably petroleum distillates of lower boiling range than lubricating oils and a sufiicient amount of polybutenes of high molecular weight to confer upon the composition viscosity, consistency, and filming characteristics necessary for any given metal Working condition. An oiliness agent such as a fatty ester, a fatty oil, a vegetable oil, or a soap maybeadded me minor amount to the composition to give improved oiliness.
The high molecular weight polybutene ingredient is the product obtainable byp-olymerizing isobutene at a low temperature, for instance below -10 Crand preferably below 40 C. with centages of oiliness agents to help preventstickthe aid of a catalyst, such as boron fluoride, In
their commercial production the polybutenes are essentially derived from isobutene, but varying V quantities ,of normal butenes may be present, also, other low molecular weight hydrocarbons which act as 'diluents. variations of this procedure and other iso-olefin reactants,-e. g. isopentene, whichmaybeused to form polymers possessing similar physical and chemical properties in general. From their synthesis and analytical determinations, the poly-Q mers of 'iso-olefins are'consideredto be linearv type polymers of a homologous series and be con-Q j stituted of recurring branched alkene units, vizz" Hence, these polymers may be called appropri ately polyalkenes or polyisoalkenes. They have V a low iodine number and a hydrogen to carbon ratio of about 2.0, which indicates; that .on an average no more than one. double bond is present in each polymer molecule; v i
Aconvenient way of describing high molecular weight compounds of the polyalkene type utilizable. in the present invention is to refer to them descriptively. as ,:polyrne ric homologous com- There are a number of oils which are more resistant to thermal decomposition and more volatile, and therefore more completely change to a gaseous state at any given temperature than the type of oils which have hitherto been necessarily employed to comply with requirements on viscosities;
Tests have shown that toguard against objectionable residue from destructive decomposition of the oilbase which tends to occurin some of the higher temperature forming operations and Iv ,7 annealing-treatments, it'is importantto restricth the maximum boiling point of a base oil to below a distillation point corresponding to 750 F. at-
760 mm. ,mercury pressure.
In accordance with the present invention, it
is possible to use as the base stock a naphtha boiling in the range from about 300 F. to 500 F., akerosene fraction boiling from 350 F. to 600 R, or a mineral seal oil boiling from about 450 F.
to 620 F. or other distillates with final boiling points as high as 750 F. The minimum distillation point isadvisably above about 300 E. mainlyxas a safeguard against fire hazards, since as ,a safety measure the composition is generally re- :quired to have a minimum flash point nolower than 100 F. The petroleum oil distillate used as the basef-or the composition maycome from pounds characterized by structures of long chains zof saturated'carbon atoms, a number of which are attachedto azrecurring organic radical'by a unsaturated-aliphatic radical and an-arrangement which predisposes themolecules'to unite into a longchain of carbon atoms, all of which with a 'possible exception of a-terminal pair of carbon atoms are saturated and with alternate individual or pairs of carbon'atoms in the chain linked to 'alkyl radicals. Such polymeric homo- V V 'logouscompounds, as typified'by' the p-olyalkenes of high molecular weight, when heated to temperatures above 300 C. undergo disintegration by scission of the carbon to carbon bonds. V "A' polybutene product varies in consistency from-viscous liquids to tough, elastic'solids as the average molecular weight of the polymers in-' creases from about 1000- to 200,000 or higher 1 The transition from liquid to solid consistency occurs when the average'molecular weight of the polymersis in theneighborhood of- 27,000 determined by the viscosity method; Beginning] at this pointof transition the polymers also acquire a pronouncedstringiness- It has been-found that "for more satisfactory results, the polybu tenes with molecular weights ranging above about 27,000'are preferred, since they make an oil composition moreresistant to shock, diminish the throwing off by centrifugal force, and increase the load bearing capacityof the-oil composition.
Practically any desired increase ofviscosity in anloil composition can'be obtained by' varying I the molecular weight and proportion of the poly.-
mer incorporated. Accordingly, a petroleum distillate base used for the. composition may besee- .lected advantageously from a class of petroleum lany type of crude and be produced by any of the well known methods of refining, because, in genera1, such light fractions all'are refractory. to decomposition by heat to a highdegree.
For the sake of illustration, the .formulaeare, given as illustrating typical com positions fLnOn staining roll oils:
5 j 7 Ingredients izfigfig Petroleum naphtha distillate (boiling from 307396 F.) A 96 Polybutenes 50,00060,0 00 molecular weight .1 3 Isopropyl esters of oxidized wax acids I 1 This compositionhas a viscosity of 1 03 say bu Uniyersalseconds atv 100 F. and aboiling range of 3l7 F. to 434 F. at atmospheric pressure.
/ i i i Percent by Ingredients I weight 7 Mineral seal oil (boiling from 480-600 F.) .1 98. 5 Polybutenes 50,00060,000 molecular weight. 0. 5 lsopro pyl' esters of oxldized wax acids. 1; 0
This composition has a viscosity of 99 Saybolt Universalgseconds at 100 F. and a boiling range of 510 -620 FJat atmospheric pressure; V Y r Thus, satisfactory non-staining'roll oils are compounded, to containabove of a volatile, non-"viscous petroleum base oil and about 0.5 to 10%tof the viscid-polybutenes, which give the blend-a viscosity ranging from 55 to about;300
Sayboit Universal seconds at F. j g Y Products for use as, i drawing compounds in mechanical forming of seamless tubes, f rods, and
Wires 'andbther structural shapes mayi'vary widelyin consistency, but are generally-required to b'e more viscous than roll oils and even semifluid; Furthermore; they may frequentlyrequire as ingredients materials which impart additional 7 oilinessor film strength characteristics. v
-:1A:. typical; nonestaining drawing compound oi semi-fluid consistency contains 15,3%-ot poly-'- but'enes havingaverage molecular weights of*50,:-
following i 000-60000; 83.7% of mineral seal oil boiling in the range of 480 F. to 620 F. and 1% of an oiliness agent. In general, satisfactory drawing compounds may contain from about 5% to about of high molecular weight polybutenes.
Although the decided improvement in the described metal working operations through the use of the high molecular weight polybutenes is most noteworthy in that they can be compounded with volatile oils to form a product that leaves no stain on the finished product after heat treat-- ment, it is difficult to ascertain exactly the manner in which certain other advantages are obtained. They stay in place on the working surface of the die or roll to which they are applied under the operating conditions when subjected to a. high pressure and high temperature conditions encountered as in a drop forge die. The stability of such compositions to oxidation well may be another factor. They act efiiciently to clean the die and to instantly release the die pressure after it has been applied because they readily form gases at the temperatures developed in the compression step. Furthermore, the manner in which they leave the operating die or rolls in a clean condition and protect such tools is also greatly in their favor.
Just as the compositions provided by this invention possess great merit in the metal fabrication processes for obtaining smooth and clean,
finished products, they are also useful in other industries in which fusible materials are worked and molded, as for example, in the glass and resin industry, because similar blends may be used for swabbing metal molds with avoidance of v the formation of varnish-like deposits which are caused by thermal decomposition of conventional petroleum oils hitherto used as mold swabbing oils.
In the foregoing description, the illustrative examples are not intended to limit this invention, as there may be a relatively wide variation in the kinds and proportions of ingredients used in the oil composition, also in the manner in which these compositions are applied to articles being formed and to tools or apparatus used in processing the articles.
I claim:
1. In operations of mechanical working and forming of shaped structural articles from fusible solid materials, the step which comprises bringing between surfaces of the article being processed and the shaping apparatus that tends to contact with said article a non-staining oil composition comprising high molecular Weight polymeric homologous compounds characterized by structures of long chains of saturated carbon atoms, of which a number have a carbon to carbon link to a recurring organic radical.
2. A step as described in claim 1, in which said high molecular weight polymeric compounds consist in polyalkenes having an average molecular weight above 1,000. g
3. In operations of cold working metal pieces, the step of applying to the surface of the piece being Worked a non-staining oil composition comprising a volatile petroleum oil distillate having a maximum boiling point of not more than about 750 F. and a minor proportion of polyalkenes having an average molecular weight above 1,000.
4. A step as described in claim 3, in which said oil composition comprises a petroleum oil distillate boiling in the range of 300 F. to 750 F., and a suiiicient quantity of polybutenes to give the composition a viscosity above about 55 Saybolt seconds at 100 F.
5. A method of improving the finish of a shaped metal article which is produced by cold rolling and a subsequent annealing treatment, which comprises wetting the surfaces of the article as it is being cold rolled with an oil composition containing high molecular weight polybutenes and a petroleum distillate boiling below 750 F.
6. A method of improving the finish of a shaped metal article produced by die drawing, which comprises coating a metal piece as it is being drawn with a non-staining drawing compound containing a major proportion of a petroleum.
distillate boiling below 750 F. and from 5% to 30% of high molecular weight polybutenes.
7. In the art of cold rolling metals in which the rolled metals are substantially annealed at elevated temperatures, the step of applying to the surface of the metal being rolled a non-staining oil composition comprising above of a petroleum distillate boiling substantially in the range of 300 to 620 F. blended with a sufiicient proportion of viscid polybutenes having an average molecular weight above 27,000 to give the blend a viscosity ranging from 55 to 300 Saybolt Universal seconds at F.
8. In the art of molding and die casting fusible solid materials, the method of improving the finish of the shaped article, which comprises the step of applying to the die a non-staining oil composition comprising a petroleum distillate boiling substantially in the range of 300 F. to 750 F. blended with a minor proportion of viscid polybutenes in sufficient amount to give the oil a viscosity above 55 Saybolt Universal seconds at DONALD L. WRIGHT.
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Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2546447A (en) * 1945-05-15 1951-03-27 American Steel & Wire Co Art of drawing fine steel wire
US2549535A (en) * 1949-02-11 1951-04-17 Standard Oil Dev Co Glass molding lubricant
US2590451A (en) * 1947-08-09 1952-03-25 Shell Dev Metalworking lubricant
US2605224A (en) * 1949-06-24 1952-07-29 Shell Dev Metalworking lubricant
US2621159A (en) * 1949-11-05 1952-12-09 Shell Dev Metal working lubricant
US2639213A (en) * 1950-03-21 1953-05-19 Price Driscoll Corp Mold parting surface and method of application
US2851330A (en) * 1955-04-15 1958-09-09 Owens Illinois Glass Co Method of treating molds
US2899390A (en) * 1959-08-11 Non-staining aluminum rolling
US3098042A (en) * 1957-01-17 1963-07-16 Exxon Research Engineering Co Lubricants containing polybutene-1
US3250103A (en) * 1964-01-30 1966-05-10 Shell Oil Co Metal working process
US3267037A (en) * 1963-05-27 1966-08-16 Phillips Petroleum Co Process for lubricating metal surfaces during working of the same
US3298951A (en) * 1966-01-24 1967-01-17 Roman D Guminski Stabilized polybutene composition
US20050198925A1 (en) * 2004-03-15 2005-09-15 Daniel Perlman Aluminum foil cups for covering laboratory vessels
EP1818119B1 (en) 2004-08-31 2018-10-17 Aoki Science Institute Co., Ltd. Mold-releasing agent for oil die casting, method for setting solvent mixing ratio and casting method

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2899390A (en) * 1959-08-11 Non-staining aluminum rolling
US2546447A (en) * 1945-05-15 1951-03-27 American Steel & Wire Co Art of drawing fine steel wire
US2590451A (en) * 1947-08-09 1952-03-25 Shell Dev Metalworking lubricant
US2549535A (en) * 1949-02-11 1951-04-17 Standard Oil Dev Co Glass molding lubricant
US2605224A (en) * 1949-06-24 1952-07-29 Shell Dev Metalworking lubricant
US2621159A (en) * 1949-11-05 1952-12-09 Shell Dev Metal working lubricant
US2639213A (en) * 1950-03-21 1953-05-19 Price Driscoll Corp Mold parting surface and method of application
US2851330A (en) * 1955-04-15 1958-09-09 Owens Illinois Glass Co Method of treating molds
US3098042A (en) * 1957-01-17 1963-07-16 Exxon Research Engineering Co Lubricants containing polybutene-1
US3267037A (en) * 1963-05-27 1966-08-16 Phillips Petroleum Co Process for lubricating metal surfaces during working of the same
US3250103A (en) * 1964-01-30 1966-05-10 Shell Oil Co Metal working process
US3298951A (en) * 1966-01-24 1967-01-17 Roman D Guminski Stabilized polybutene composition
US20050198925A1 (en) * 2004-03-15 2005-09-15 Daniel Perlman Aluminum foil cups for covering laboratory vessels
EP1818119B1 (en) 2004-08-31 2018-10-17 Aoki Science Institute Co., Ltd. Mold-releasing agent for oil die casting, method for setting solvent mixing ratio and casting method

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