WO2005037964A2 - Lubricant base oils with optimized branching - Google Patents
Lubricant base oils with optimized branching Download PDFInfo
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- WO2005037964A2 WO2005037964A2 PCT/US2004/030134 US2004030134W WO2005037964A2 WO 2005037964 A2 WO2005037964 A2 WO 2005037964A2 US 2004030134 W US2004030134 W US 2004030134W WO 2005037964 A2 WO2005037964 A2 WO 2005037964A2
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M107/00—Lubricating compositions characterised by the base-material being a macromolecular compound
- C10M107/02—Hydrocarbon polymers; Hydrocarbon polymers modified by oxidation
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M171/00—Lubricating compositions characterised by purely physical criteria, e.g. containing as base-material, thickener or additive, ingredients which are characterised exclusively by their numerically specified physical properties, i.e. containing ingredients which are physically well-defined but for which the chemical nature is either unspecified or only very vaguely indicated
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2205/00—Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions
- C10M2205/17—Fisher Tropsch reaction products
- C10M2205/173—Fisher Tropsch reaction products used as base material
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2020/00—Specified physical or chemical properties or characteristics, i.e. function, of component of lubricating compositions
- C10N2020/01—Physico-chemical properties
- C10N2020/02—Viscosity; Viscosity index
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2020/00—Specified physical or chemical properties or characteristics, i.e. function, of component of lubricating compositions
- C10N2020/01—Physico-chemical properties
- C10N2020/071—Branched chain compounds
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2070/00—Specific manufacturing methods for lubricant compositions
Definitions
- This invention relates to lubricant base oils comprising paraffimc components that have optimized branching.
- the lubricant base oils comprising paraffinic components with optimized branching have low amounts of branching with the branching concentrated toward the center of the lubricant base oil molecules.
- the lubricant base oils comprising paraffinic components with optimized branching have low pour points and extremely high viscosity indexes.
- the invention further relates to processes of producing the lubricant base oils comprising paraffinic components with optimized branching from waxy feeds.
- the lubricant base oils are useful in commercial finished lubricants.
- High quality lubricants should be, and generally are, paraffinic in nature, since paraffins have a high viscosity index.
- normal paraffins in particular, are waxy in character, and contribute to a high pour point in the oil.
- waxy paraffinic feeds may be converted to lubricant base oils by hydroisomerization dewaxing, which creates branching on the paraffinic molecules.
- Hydroisomerization dewaxing typically produces a lubricant base oil having relatively high branching. While creating branching on waxy paraffinic molecules generally lowers the pour point, it also lowers the viscosity Index (VI).
- VI viscosity Index
- Lubricant base oil products produced by a hydroisomerization process may have branching characteristics similar to those products described in US Patent Nos. 6,096,940, 6,090,989, and 6,059,955.
- Low pour points are desirable in lubricant base oils.
- a low pour point indicates that a lubricant base oil will flow and lubricate at low temperatures.
- Pour point is a measurement of the temperature at which the sample will begin to flow under carefully controlled conditions. Pour point may be determined as described in ASTM D 5950.
- Viscosity Index is an empirical, unitless number indicating the effect of temperature change on the kinematic viscosity of the oil.
- VI viscosity Index
- Waxy hydrocarbons prepared from a Fischer Tropsch process are a good potential feedstock for preparing high quality lubricants.
- the Fischer Tropsch products contain little, if any, of typical petroleum contaminants, such as aromatic compounds, sulfur compounds, and nitrogen compounds.
- the initial Fischer Tropsch waxy paraffins are generally straight chain waxes. Accordingly, the Fischer Tropsch products need to be subjected to further processing or upgrading to provide high quality lubricant base oil stocks.
- the lubricant oil basestocks as disclosed therein contain paraffinic hydrocarbon components in which the extent of branching, as measured by the percentage of methyl hydrogens (BI), and the proximity of branching, as measured by the percentage of recurring methylene carbons which are four or more carbons removed from an end group or branch (CH 2 >4), are such that: (a) BI-0.5(CH 2 >4) of greater than 15 and (b) BI +0.85(CH 2 >4) ⁇ 45.
- This calculation means that for a molecule containing 24 carbons, that molecule would have at least 2.5 branches per molecule, or for every 100 carbons there are greater than about 9 branches.
- 6,008,164 discloses a method for producing a lubricant base stock from a Fischer Tropsch wax wherein the lubricant base stock has a preselected oxidative stability.
- the lubricant base oils are disclosed as containing a mixture of branched paraffins wherein the branched paraffins contain up to four alkyl branches and wherein the free carbon index (FCI) of the branched paraffins is at least about 3.
- FCI free carbon index
- WO 99/45085 discloses an integrated process for preparing a lubricant oil base stock including an isomerization step followed by a solvent dewaxing step.
- a waxy feed as disclosed therein, a waxy feed is isomerized to an intermediate pour point over a select molecular sieve and the isomerized oil is then solvent dewaxed.
- the lubricant oil base stocks obtained were disclosed as having viscosity indexes of greater than about 140.
- the Examples of the '085 publication demonstrate lubricant oil base stocks with viscosity indexes in the 140's with the highest being 156.
- EP 0776959 A2 discloses a process for preparing lubricant base oils having a VI of at least 150 from a Fischer Tropsch wax feed comprising contacting the Fischer Tropsch wax feed with a hydroconversion catalyst under hydroconversion conditions; separating the hydroconverted effluent obtained into at least one lighter fraction and a heavy fraction; and dewaxing the heavy fraction to yield the base oil.
- the feed to the process is narrowly limited to a Fischer-Tropsch wax having a congealing point of at least 50°C and has a boiling range where the difference between the 90 % wt boiling point and the 10 % wt boiling point is in the range of from 40 to 150°C.
- the hydroconversion catalysts are disclosed as being amo ⁇ hous catalysts.
- U.S. Patent No. 6,096,940 discloses a process for producing a biodegradable hydrocarbon lubricant base oil. The process comprises contacting a 700°F+ Fischer
- Tropsch wax feed with hydrogen over a bifunctional non-noble Group VIII metal catalyst to produce hydroisomerization and hydrocracking reactions at 700°F+ conversion levels ranging from about 20 to about 50 percent on a once through basis, based on the weight of 700°F+ feed converted to 700°F- materials, to produce a C 5 -1050°F crude fraction.
- the isoparaffins contained in the crude fraction are disclosed as having methyl branches in an amount of less than about 7.5 methyl branches per 100 carbons.
- a residual fraction having an initial boiling point ranging from about 650°F to about 750°F is recovered.
- the residual fraction is dewaxed and a dewaxed oil is recovered.
- the dewaxing catalysts suitable for use in this invention are defined broadly and include catalysts such as fluorided alumina.
- catalysts such as fluorided alumina.
- FJJVIS field ionization mass spectrornetry
- the present invention relates to a lubricant base oil comprising paraffinic hydrocarbon components in which the extent of branching is less than 8 alkyl branches per 100 carbons and less than 20 wt% of the alkyl branches are at the 2 position.
- the present invention relates to a finished lubricant.
- the finished lubricant comprises the lubricant base oils as described herein and one or more lubricant additives.
- the present invention relates to an intermediate oil isomerate.
- the intermediate oil isomerate comprises Fischer-Tropsch derived paraffinic hydrocarbon components in which the extent of branching is less than 7 alkyl branches per 100 carbons.
- the present invention relates to lubricant base oils, comprising a mixture of paraffinic hydrocarbon components wherein the mixture of paraffinic hydrocarbon components have optimized branching.
- These lubricant base oils comprising a mixture of paraffinic hydrocarbon components with optimized branching have low amounts of branching overall with the branching concentrated toward the center of the lubricant base oil molecules.
- the present invention also relates to processes of producing these lubricant base oils from waxy feeds and commercial finished lubricants comprising these lubricant base oils.
- optimizing branching can provide exceptionally low pour points and extremely high viscosity indexes, that are greater than the Target Viscosity Index, as defined herein.
- Optimizing branching according to the present invention means that the lubricant base oil molecules comprise paraffinic hydrocarbon components having low amounts of branching overall with the branching concentrated toward the center of the molecules.
- Lubricant base oils comprising paraffinic hydrocarbon components with optimized branching and having kinematic viscosities greater than about 3.2 cSt at 100°C can be produced by a combination of a mild hydroisomerization followed by solvent dewaxing.
- a waxy feed is subjected to a mild hydroisomerization process under conditions such that an intermediate oil isomerate comprising paraffinic hydrocarbon components having specific branching properties is formed.
- the intermediate oil isomerate is then subjected to solvent dewaxing under conditions to provide a lubricant base oil comprising paraffinic hydrocarbon components with optimized branching and having a kinematic viscosity greater than about 3.2 cSt at 100°C.
- the process of the present invention results in a lubricant base oil comprising paraffinic hydrocarbon components with optimized branching such that there are low amounts of branching overall with the branching concentrated toward the center of the molecules.
- the extent of branching and branching position can be determined by NMR Analysis.
- waxy hydrocarbon feedstock is a feed or stream comprising molecules with a carbon number of C 0+ and having a boiling point generally above about 600 °F (316 °C).
- the waxy hydrocarbon feedstocks useful in the processes disclosed herein may be synthetic waxy feedstocks, such as Fischer Tropsch waxy hydrocarbons, or may be derived from natural sources, such as petroleum waxes.
- Lubricant base oil means a fraction or product meeting specifications for a lubricant base oil.
- Lubricant base oil fractions are provided according to the processes of the present invention by a hydroisomeration/solvent dewaxing process and have optimized branching properties. Additional properties of the lubricant base oils provided according to the present invention include initial boiling points in the range of 600 to 950°F, end boiling points in the range of 800 to 1200°F, viscosities in the range of 3.2 to 20 cSt at 100°C, viscosity indices in the range of 158 to 240, preferably in the range of 163 to 220, and more preferably in the range of 165 to
- the lubricant base oils further have pour points less then -8°C, preferably less than -9°C, more preferably ⁇ -15°C, and even more preferably less than -15°C, and preferably in the range of -8 to -35°C.
- the lubricant base oils may also have cloud points in the range of +5 to -20°C.
- “Hydrocarbon or hydrocarbonaceous” means a compound or substance that contains hydrogen and carbon atoms, which may also include heteroatoms such as oxygen, sulfur or nitrogen.
- “Target Viscosity Index” is an empirical number derived from kinematic viscosity and Viscosity Index.
- Target Viscosity Index 22 x ln(Kinematic Viscosity at 100 °C)+132 wherein ln(Kinematic Viscosity at 100 °C) is the natural logarithm of Kinematic
- Alkyl means a linear saturated monovalent hydrocarbon radical of one to six carbon atoms or a branched saturated monovalent hydrocarbon radical of three to eight carbon atoms.
- the alkyl groups are methyl.
- alkyl groups include, but are not limited to, groups such as methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, sec-butyl, t-butyl, n-pentyl, and the like.
- FCI Free Carbon Index
- FCI Free Carbon Index
- lubricant base oils with kinematic viscosities greater than about 3.2 cSt at 100 °C comprising paraffinic hydrocarbon components having certain desired branching properties (optimized branching) have extremely high viscosity indexes and excellent low pour points.
- the Viscosity Indexes of the lubricant base oils of the present invention are greater than the Target Viscosity Index of the oil.
- the viscosity indexes of the lubricant base oils of the present invention are greater than the Target Viscosity Index of the oil plus 5.
- These lubricant base oils comprise a mixture of paraffinic hydrocarbon components wherein the overall mixture of paraffinic hydrocarbon components have optimized branching.
- These lubricant base oils comprising paraffinic hydrocarbon components with optimized branching are produced from waxy feeds.
- the present invention also relates to intermediate oil isomerates made in the processes of making the lubricant base oils of the present invention.
- the intermediate oil isomerates of the present invention comprising paraffinic hydrocarbon components having specific branching properties. Accordingly, when the intermediate isomerates are converted to lubricant base oils, the lubricant base oils comprise paraffinic hydrocarbon components having optimized branching properties.
- the intermediate oil isomerates are comprised of paraffinic hydrocarbon components in which the paraffinic hydrocarbon components have low amounts of branching overall.
- the branches on the paraffinic hydrocarbon components of the lubricant base oils and intermediate oil isomerates are alkyl branches.
- the alkyl branches are predominantly methyl branches (- CH 3 ).
- the branching properties are optimized.
- the branching properties include the extent of branching and the position of branching.
- the extent of branching can be measured by the number of alkyl branches per a given number of carbons of the paraffinic hydrocarbon components.
- the extent of branching is measured by the number of alkyl branches per 100 carbons.
- the position of branching is measured relative to the ends of the hydrocarbon chain of the paraffin, with the terminal carbons being the 1 position, the next-in adjacent carbon being the 2 position, the subsequent-in carbon being the 3 position, and so forth until the center of the hydrocarbon chain is reached.
- the positions on the hydrocarbon chain may be illustrated as follows:
- the intermediate oil isomerates are intermediate products of the process to make the lubricant base oils of the present invention.
- the intermediate oil isomerates are produced by subjecting a waxy feed to a mild hydroisomerization process using a specific class of shape selective catalysts that impart a large degree of pour point reduction with a minimum degree of branching.
- the intermediate oil isomerates are solvent dewaxed to provide the lubricant base oils of the present invention.
- the intermediate oil isomerates comprise paraffimc hydrocarbon components having specific branching properties.
- the intermediate oil isomerates are comprised of paraffinic hydrocarbon components having low amounts of branching overall.
- the intermediate oil isomerates comprise paraffinic hydrocarbon components having less than 7.0 alkyl branches per 100 carbons and preferably less than less than 6.5 alkyl branches per 100 carbons.
- the intermediate oil isomerates are solvent dewaxed to provide the lubricant base oils of the present invention.
- the lubricant base oils comprise paraffinic hydrocarbon components in which the branching is optimized.
- the lubricant base oils comprise paraffinic hydrocarbon components having optimized branching in that the paraffinic hydrocarbon components of the isomerates have low amounts of branching overall with the branching concentrated toward the center of the molecules.
- the lubricant base oils comprise paraffinic hydrocarbon components having less than 8 alkyl branches per 100 carbons, preferably less than 7 alkyl branches per 100 carbons, and more preferably less than 6.5 alkyl branches per 100 carbons.
- the lubricant base oils comprise paraffinic hydrocarbon components having less than 20 wt% branching at the two position and preferably less than 15% branching at the two position.
- the lubricant base oils also have low amounts of branching at the two plus three positions, preferably less than 25 wt% and more preferably less than 20 wt%.
- the lubricant base oils have branching at the five or greater positions of greater than 45 wt% and more preferably greater than 50 wt%.
- lubricant base oils with low kinematic viscosities generally less than about 3.2 cSt at 100 °C, and having low pour points
- the paraffinic hydrocarbon molecules comprising lubricant base oils of low kinematic viscosities are of relatively shorter paraffinic chains, generally less than about 25 carbons in length. Since lubricant base oils having relatively low kinematic viscosities are of relatively shorter paraffinic chains, these lubricant base oils generally require fewer branches to reach a low pour point.
- higher viscosity lubricant base oils comprise paraffinic hydrocarbon molecules of longer chain length.
- these longer paraffinic hydrocarbon molecules of higher viscosity lubricant base oils it is much more difficult to isomerize to low amounts of branching and obtain a low pour point.
- branches move toward the middle of linear paraffins for butyl, phenyl, and cyclohexyl branches, the
- the lubricant base oils of the present invention have kinematic viscosities at 100 °C greater than about 3.2 cSt, preferably between about 3.2 cSt and about 20 cSt.
- the lubricant base oils of the present invention comprise average carbon numbers of greater than about 27, preferably greater than about 30, and more preferably greater than about 27 and less than about 70. The extent of branching and branching position can be determined by NMR
- NMR Branching Analysis The branching properties of the lubricant base oils and intermediate oil isomerates of the present invention are determined by analyzing a sample of oil using carbon-13 NMR according to the following eight-step process. References cited in the description of the process provide details of the process steps. Steps 1 and 2 are performed only on the initial materials from a new process. 1.) Identify the CH branch centers and the CH 3 branch termination points using the DEPT Pulse sequence (Doddrell, D.T.; D. T. Pegg; M.R. Bendall, Journal of Magnetic Resonance 1982, 48, 323ff.). 2.) Verify the absence of carbons initiating multiple branches
- FCI Free Carbon Index
- molecular weight is preferably determined by ASTM D2503-02. 6.) Calculate the Branching Index (BI) and Branching Proximity (BP) using the calculations described in U.S. Patent No. 6,090,989.
- Branching Index is the ratio in percent of non-benzylic methyl hydrogens in the range of 0.5 to 1.05 ppm, to the total non-benzylic aliphatic hydrogens in the range of 0.5 to 2.1 ppm.
- the Branching Proximity is the % equivalent recurring methylene carbons, which are five or more removed from an end group or branch (epsilon carbons). 7.) The number of branches per molecule is the sum of the branches found in step 4.
- the number of alkyl branches per 100 carbon atoms is calculated from the number of branches per molecule (step 7) times 100/number of carbons per molecule. Measurements can be performed using any Fourier Transform NMR spectrometer. Preferably, the measurements are performed using a spectrometer having a magnet of 7.0T or greater. In all cases, after verification by Mass Spectrometry, UV or an NMR survey that aromatic carbons were absent, the spectral width was limited to the saturated carbon region, about 0-80 ppm vs. TMS (tetramethylsilane). Solutions of 15-25% by weight in chloroform-dl were excited by 45° pulses followed by an 0.8 sec acquisition time.
- the proton decoupler was gated off during a 10 sec delay prior to the excitation pulse and on during acquisition. Total experiment times ranged from 11-80 minutes.
- the DEPT and APT sequences were carried out according to literature descriptions with minor deviations described in the Varian or Bruker operating manuals.
- DEPT is Distortionless Enhancement by Polarization Transfer. DEPT does not show quaternaries.
- the DEPT 45 sequence gives a signal all carbons bonded to protons.
- DEPT 90 shows CH carbons only.
- DEPT 135 shows CH and CH 3 up and
- APT is Attached Proton Test. It allows all carbons to be seen, but if CH and CH 3 are up, then quaternaries and CH 2 are down. The sequences are useful in that every branch methyl should have a corresponding CH. And the methyls are clearly identified by chemical shift and phase. Both are described in the references cited.
- the branching properties of each sample were determined by C-13 NMR using the assumption in the calculations that the entire sample of lubricant base oil or intermediate oil isomerate was iso-paraffinic. Corrections were not made for n- paraffins or naphthenes, which may have been present in the oil samples in varying amounts.
- the % total naphthenes in the lubricant base oils were generally low or absent, due to the mild hydroisomerization dewaxing process used in the preparation.
- the naphthenes content may be measured using Field Ionization Mass Spectroscopy (F S).
- the feed to the process to produce lubricant base oils with optimized branching is a waxy hydrocarbon feed.
- the waxy hydrocarbon feedstocks useful in the processes disclosed herein may be synthetic waxy feedstocks, such as Fischer Tropsch waxy hydrocarbons, or may be derived from natural sources, such as petroleum waxes. Accordingly, the waxy feedstocks to the processes may comprise Fischer Tropsch derived waxy feeds, petroleum waxes, waxy distillate stocks such as gas oils, lubricant oil stocks, high pour point polyalphaolefins, foots oils, normal alpha olefin waxes, slack waxes, deoiled waxes, and microcrystalline waxes, and mixtures thereof.
- the waxy feedstocks are derived from Fischer Tropsch waxy feeds.
- a substantial proportion of the waxy feed comprises molecules with a carbon number of C 2 o + and has a boiling point generally above about 600 °F (316 °C).
- the majority of the molecules in the waxy feed are higher molecular weight n-paraffins and slightly branched paraffins which contribute to the waxy nature of the feed.
- the waxy hydrocarbon feedstock may be hydrotreated prior to the process as described herein if desired.
- the waxy feedstocks of the present invention are derived from Fischer Tropsch waxy feeds.
- Fischer-Tropsch chemistry syngas is converted to liquid hydrocarbons by contact with a Fischer-Tropsch catalyst under reactive conditions.
- methane and optionally heavier hydrocarbons ethane and heavier
- synthesis gas contains hydrogen and carbon monoxide, and may include minor amounts of carbon dioxide and/or water. The presence of sulfur, nitrogen, halogen, selenium, phosphorus and arsenic contaminants in the syngas is undesirable.
- Fischer-Tropsch reactor to remove carbon dioxide produced during the syngas reaction and any additional sulfur compounds not already removed. This can be accomplished, for example, by contacting the syngas with a mildly alkaline solution (e.g., aqueous potassium carbonate) in a packed column.
- a mildly alkaline solution e.g., aqueous potassium carbonate
- contacting a synthesis gas comprising a mixture of H 2 and CO with a Fischer-Tropsch catalyst under suitable temperature and pressure reactive conditions forms liquid and gaseous hydrocarbons.
- the Fischer-Tropsch reaction is typically conducted at temperatures of about 300-700°F (149-371°C), preferably about 400-550°F (204-228°C); pressures of about 10-600 psia, (0.7-41 bars), preferably about 30-300 psia, (2-21 bars); and catalyst space velocities of about 100-10,000 cc/g/hr, preferably about 300-3,000 cc/g/hr. Examples of conditions for performing Fischer-Tropsch type reactions are well known to those of skill in the art.
- the products of the Fischer-Tropsch synthesis process may range from Ci to C 00+ with a majority in the C 5 to C 100+ range.
- the reaction can be conducted in a variety of reactor types, such as fixed bed reactors containing one or more catalyst beds, slurry reactors, fluidized bed reactors, or a combination of different type reactors.
- reactor types such as fixed bed reactors containing one or more catalyst beds, slurry reactors, fluidized bed reactors, or a combination of different type reactors.
- Such reaction processes and reactors are well known and documented in the literature.
- the slurry Fischer-Tropsch process which is prefe ⁇ ed in the practice of the invention, utilizes superior heat (and mass) transfer characteristics for the strongly exothermic synthesis reaction and is able to produce relatively high molecular weight, paraffinic hydrocarbons when using a cobalt catalyst.
- a syngas comprising a mixture of hydrogen and carbon monoxide is bubbled up as a third phase through a slurry which comprises a particulate Fischer-Tropsch type hydrocarbon synthesis catalyst dispersed and suspended in a slurry liquid comprising hydrocarbon products of the synthesis reaction which are liquid under the reaction conditions.
- the mole ratio of the hydrogen to the carbon monoxide may broadly range from about 0.5 to about 4, but is more typically within the range of from about 0.7 to about 2.75 and preferably from about 0.7 to about 2.5.
- a particularly preferred Fischer-Tropsch process is taught in EP0609079, also completely inco ⁇ orated herein by reference for all pu ⁇ oses.
- Fischer-Tropsch catalysts contain a Group VIII transition metal on a metal oxide support.
- the catalysts may also contain a noble metal promoter(s) and/or crystalline molecular sieves.
- Suitable Fischer-Tropsch catalysts comprise one or more of Fe, Ni, Co, Ru and Re, with cobalt being preferred.
- a preferred Fischer-Tropsch catalyst comprises effective amounts of cobalt and one or more of Re, Ru, Pt, Fe, Ni, Th, Zr, Hf, U, Mg and La on a suitable inorganic support material, preferably one which comprises one or more refractory metal oxides.
- the amount of cobalt present in the catalyst is between about 1 and about 50 weight percent of the total catalyst composition.
- the catalysts can also contain basic oxide promoters such as ThO 2 , La 2 O 3 , MgO, and TiO 2 , promoters such as ZrO 2 , noble metals (Pt, Pd, Ru, Rh, Os, Ir), coinage metals (Cu, Ag, Au), and other transition metals such as Fe, Mn, Ni, and Re.
- Suitable support materials include alumina, silica, magnesia and titania or mixtures thereof.
- Preferred supports for cobalt containing catalysts comprise titania.
- Useful catalysts and their preparation are known and illustrated in U.S. Patent 4,568,663, which is intended to be illustrative but non-limiting relative to catalyst selection.
- Certain catalysts are known to provide chain growth probabilities that are relatively low to moderate, and the reaction products include a relatively high proportion of low molecular (C 2-8 ) weight olefins and a relatively low proportion of high molecular weight (C 30+ ) waxes. Certain other catalysts are known to provide relatively high chain growth probabilities, and the reaction products include a relatively low proportion of low molecular (C 2-8 ) weight olefins and a relatively high proportion of high molecular weight (C 30+ ) waxes. Such catalysts are well known to those of skill in the art and can be readily obtained and/or prepared. The product from a Fischer-Tropsch process contains predominantly paraffins.
- the products from Fischer-Tropsch reactions generally include a light reaction product and a waxy reaction product.
- the light reaction product i.e., the condensate fraction
- the waxy reaction product i.e., the wax fraction
- hydrocarbons boiling above about 600°F e.g., vacuum gas oil through heavy paraffins
- the waxy product generally comprises greater than 70 weight % normal paraffins, and often greater than 80 weight % normal paraffins.
- the light reaction product comprises paraffinic products with a significant proportion of alcohols and olefins. In some cases, the light reaction product may comprise as much as 50 weight %, and even higher, alcohols and olefins. It is the waxy reaction product (i.e., the wax fraction) that may be used as a feedstock for the processes of the present invention.
- the waxy hydrocarbon feedstock is subjected to hydroisomerization in a hydroisomerization zone, producing an intermediate oil isomerate.
- Hydroisomerization is intended to improve the cold flow properties of a lubricant base oil by the selective addition of branching into the molecular structure.
- Hydroisomerization dewaxing ideally will achieve high conversion levels of waxy feed to non-waxy iso-paraffins while at the same time minimizing the conversion by cracking.
- hydroisomerization is conducted using a shape selective intermediate pore size molecular sieve.
- Hydroisomerization catalysts useful in the present invention comprise a shape selective intermediate pore size molecular sieve and optionally a catalytically active metal hydrogenation component on a refractory oxide support.
- intermediate pore size means an effective pore aperture in the range of from about 4.0 to about 7.1 A when the porous inorganic oxide is in the calcined form.
- shape selective intermediate pore size molecular sieves used in the practice of the present invention are generally 1-D 10-, 11- or 12-ring molecular sieves.
- the preferred molecular sieves of the invention are of the 1-D 10-ring variety, where 10-(or 11-or 12-) ring molecular sieves have 10 (or 11 or 12) tetrahedrally-coordinated atoms (T-atoms) joined by oxygens.
- T-atoms tetrahedrally-coordinated atoms
- the 10-ring (or larger) pores are parallel with each other, and do not interconnect.
- the classification of intrazeolite channels as 1-D, 2-D and 3-D is set forth by R. M. Barrer in Zeolites, Science and Technology, edited by F. R. Rodrigues, L.D. Rollman and C. Naccache, NATO ASI Series, 1984 which classification is inco ⁇ orated in its entirety by reference (see particularly page 75).
- Preferred shape selective intermediate pore size molecular sieves used for hydroisomerization are based upon aluminum phosphates, such as SAPO-11, SAPO- 31, and SAPO-41.
- SAPO-11 and SAPO-31 are more preferred, with SAPO-11 being most preferred.
- SM-3 is a particularly preferred shape selective intermediate pore size SAPO, which has a crystalline structure falling within that of the SAPO-11 molecular sieves. The preparation of SM-3 and its unique characteristics are described in U.S. Patent Nos. 4,943,424 and 5,158,665.
- zeolites such as ZSM-22, ZSM-23, ZSM-35, ZSM-48, ZSM-57, SSZ-32, offretite, and ferrierite. SSZ-32 and ZSM-23 are more preferred.
- a preferred intermediate pore size molecular sieve is characterized by selected crystallographic free diameters of the channels, selected crystallite size (corresponding to selected channel length), and selected acidity.
- Desirable crystallographic free diameters of the channels of the molecular sieves are in the range of from about 4.0 to about 7.1 Angstrom, having a maximum crystallographic free diameter of not more than 7.1 and a minimum crystallographic free diameter of not less than 3.9 Angstrom.
- the maximum crystallographic free diameter is not more than 7.1 and the minimum crystallographic free diameter is not less than
- the maximum crystallographic free diameter is not more than 6.5 and the minimum crystallographic free diameter is not less than 4.0 Angstrom.
- the crystallographic free diameters of the channels of molecular sieves are published in the "Atlas of Zeolite Framework Types", Fifth Revised Edition, 2001, by Ch. Baerlocher, W.M. Meier, and D.H. Olson, Elsevier, pp 10-15, which is inco ⁇ orated herein by reference.
- a particularly preferred intermediate pore size molecular sieve, which is useful in the present process is described, for example, in United States Patents No. 5,135,638 and 5,282,958, the contents of which are hereby inco ⁇ orated by reference in their entirety.
- such an intermediate pore size molecular sieve has a crystallite size of no more than about 0.5 microns and pores with a minimum diameter of at least about 4.8 A and with a maximum diameter of about 7.1 A.
- the catalyst has sufficient acidity so that 0.5 grams thereof when positioned in a tube reactor converts at least 50% of hexadecane at 370°C, a pressure of 1200 psig, a hydrogen flow of 160 ml/min, and a feed rate of 1 ml hr.
- the catalyst also exhibits isomerization selectivity of 40 percent or greater (isomerization selectivity is determined as follows: 100 x (weight % branched Cj 6 in product) / (weight % branched C 16 in product + weight % C 13- in product) when used under conditions leading to 96% conversion of normal hexadecane (n-C 16 ) to other species.
- Such a particularly prefe ⁇ ed molecular sieve may further be characterized by pores or channels having a crystallographic free diameter in the range of from about 4.0 to about 7.1 A, and preferably in the range of 4.0 to 6.5 A.
- the crystallographic free diameters of the channels of molecular sieves are published in the "Atlas of Zeolite Framework Types", Fifth Revised Edition, 2001 , by Ch. Baerlocher, W.M.
- the effective pore size of the molecular sieve can be measured using standard adso ⁇ tion techniques and hydrocarbonaceous compounds of known minimum kinetic diameters. See Breck, Zeolite Molecular Sieves, 1974 (especially Chapter 8); Anderson et al. J. Catalysis 58, 114 (1979); and U.S. Pat. No. 4,440,871, the pertinent portions of which are inco ⁇ orated herein by reference. In performing adso ⁇ tion measurements to determine pore size, standard techniques are used.
- Hydroisomerization catalysts useful in the present invention optionally comprise a catalytically active hydrogenation metal.
- a catalytically active hydrogenation metal leads to product improvement, especially VI and stability.
- Typical catalytically active hydrogenation metals include chromium, molybdenum, nickel, vanadium, cobalt, tungsten, zinc, platinum, and palladium.
- the metals platinum and palladium are especially prefe ⁇ ed, with platinum most especially preferred. If platinum and/or palladium is used, the total amount of active hydrogenation metal is typically in the range of 0.1 to 5 weight percent of the total catalyst, usually from 0.1 to 2 weight percent, and not to exceed 10 weight percent.
- the refractory oxide support may be selected from those oxide supports, which are conventionally used for catalysts, including silica, alumina, silica- alumina, magnesia, titania and combinations thereof.
- the conditions for hydroisomerization will be tailored to achieve an isomerized oil intermediate with specific branching properties, as described above, and thus will depend on the characteristics of feed used.
- conditions for hydroisomerization in the present invention are mild such that the conversion of wax to materials boiling below about 700 °F is maintained below about 35 wt % in producing the intermediate oil isomerates.
- Mild hydroisomerization conditions are achieved through operating at a lower temperature, generally between about 390 °F and 650 °F at a LHSV generally between about 0.5 hr _1 and about 20 hr "1 .
- the pressure is typically from about 15 psig to about 2500 psig, preferably from about 50 psig to about 2000 psig, more preferably from about 100 psig to about 1500 psig.
- Low pressure provides enhanced isomerization selectivity, which results in more isomerization and less cracking of the feed, thus producing an increased yield.
- Hydrogen is present in the reaction zone during the hydroisomerization process, typically in a hydrogen to feed ratio from about 0.5 to 30 MSCF/bbl (thousand standard cubic feet per barrel), preferably from about 1 to about 10 MSCF/bbl. Hydrogen may be separated from the product and recycled to the reaction zone.
- These mild hydroisomerization conditions using the shape selective intermediate pore size molecular sieves produce intermediate oil isomerates comprising paraffinic hydrocarbon components having specific branching properties, i.e., having low amounts of branching overall.
- the intermediate oil isomerates have less than 7.0, preferably less than 6.5 alkyl branches per 100 carbons, as determined by NMR branching analysis.
- the intermediate oil isomerates are subjected to solvent dewaxing, producing lubricant base oils comprising paraffinic hydrocarbon components with optimized branching properties. Therefore, the solvent dewaxing produces lubricant base oils comprising paraffinic hydrocarbon components having low amounts of branching overall with branching concentrated toward the center of the molecules.
- Solvent dewaxing is used to remove the remaining waxy molecules from the intermediate oil isomerate by dissolving the intermediate oil isomerate in a solvent, such as methyl ethyl ketone, methyl iso-butyl ketone, or toluene, or precipitating the wax molecules as discussed in Chemical Technology of Petroleum, 3rd Edition, William Gruse and Donald Stevens, McGraw-Hill Book Company, Inc., New York, 1960, pages 566 to 570. See also US Patents 4,477,333, 3,773,650 and 3,775,288.
- solvent dewaxing is advantageously used following hydroisomerization to recover unconverted wax following hydroisomerization at mild conditions where conversions of the wax to material boiling below about 700°F is less than about 35%.
- the solvent dewaxing may be conducted by conventional processes well known to those of skill in the art. Solvent dewaxing may be accomplished by cooling intermediate oil isomerate/solvent admixtures under controlled conditions for crystallization of the paraffinic wax present in the admixtures. In such processes, the intermediate oil isomerate and dewaxing solvent, are heated to a temperature at which the wax is dissolved. The heated charge is then passed into a cooling zone wherein cooling is undertaken at a uniform slow rate in the range of about 0.5° to 4.5°C/min until a temperature is reached (e.g. -10° to -
- the mixture of wax crystals, intermediate oil isomerate, and solvent is subjected to solid-liquid separation for recovery of a wax free oil-solvent solution and a solid wax containing a minor proportion of oil.
- Solid- liquid separation techniques which may be employed for separation of wax crystals from the oil-solvent solutions, include known solid-liquid separation processes, such as gravity settling, centrifugation, and filtration. Most commonly, in commercial processes, filtration in a rotary vacuum filter, followed by solvent wash of the wax cake, is employed.
- the solid wax/oil solution obtained after separation of the solid wax is known as slack wax.
- the separated oil-solvent solution is subjected to distillation for recovery of a solvent fraction and a dewaxed lubricant base oil product fraction.
- Solvents known to be useful as dewaxing solvents are ketones containing 3 to 6 carbon atoms, for example, acetone, methylethyl ketone (MEK), and methylisobutylketone (MIBK), mixtures of ketones, and mixtures of ketones with aromatic hydrocarbons including benzene and toluene.
- Halogenated low molecular weight hydrocarbons including dichloromethane and dichloroethane, and mixtures thereof are also known dewaxing solvents.
- Solvent dilution of waxy oil stocks maintains fluidity of the oil for facilitating easy handling, for obtaining optimum wax-oil separation, and for obtaining optimum dewaxed oil yields.
- the extent of solvent dilution depends upon the particular intermediate oil isomerate stocks and solvents used, the approach to filtration temperature in the cooling zone, and the desired final ratio of solvent to oil in the separation zone.
- All or a portion of the wax removed in the dewaxing step may be recovered and recycled to the hydroisomerization step for use in the process of the present invention and/or collected for other uses (e.g., for processing into or use as salable wax).
- the wax may be subjected to the hydroisomerization step of the present invention alone or may be combined with another waxy feedstock. Recycling all or a portion of the recovered wax increases the yield of the process.
- a lubricant base oil comprising paraffinic hydrocarbon components with optimized branching is provided.
- Optimized branching means that the lubricant base oil comprises paraffinic hydrocarbon components having low amounts of branching overall with the branching concentrated toward the center of the molecules.
- the lubricant base oils comprising paraffinic hydrocarbon components with optimized branching recovered from the process of the present invention have a kinematic viscosity at 100°C of greater than about 3.2 cSt.
- the lubricant base oils comprising paraffinic hydrocarbon components having optimized branching have Viscosity Indexes greater than the Target Viscosity Indexes of the oil, as defined above.
- the viscosity indexes of the lubricant base oils of the present invention are greater than the Target Viscosity Index of the oil plus 5.
- the lubricant base oils also have a pour point of less than -8 °C, preferably less than -9 °C, more preferably ⁇ -15 °C, and even more preferably less than -15 °C.
- a pour point of less than -8 °C, preferably less than -9 °C, more preferably ⁇ -15 °C, and even more preferably less than -15 °C.
- the difference in pour points between the pour point of the lubricant base oil and the intermediate oil isomerate prior to solvent dewaxing is greater than about 25 °F.
- the lubricant base oil comprising paraffinic hydrocarbon components with optimized branching, or optionally the intermediate oil isomerate, may be hydrofinished in order to improve product quality and stability.
- overall LHSV is about 0.25 to 2.0, preferably about 0.5 to 1.0.
- the hydrogen partial pressure is greater than 200 psia, preferably ranging from about 500 psia to about 2000 psia.
- Hydrogen recirculation rates are typically greater than 50 SCF/Bbl, and are preferably between 1000 and 5000 SCF/Bbl.
- Temperatures range from about 300°F to about 750°F, preferably ranging from 450°F to 600°F.
- Suitable hydrofinishing catalysts include noble metals from Group VJJIA
- the non-noble metal such as nickel-molybdenum and/or tungsten, and at least about 0.5, and generally about 1 to about 15 weight percent of nickel and/or cobalt determined as the corresponding oxides.
- the noble metal (such as platinum) catalyst contains in excess ofO.Ol percent metal, preferably between 0.1 and 1.0 percent metal.
- Combinations of noble metals may also be used, such as mixtures of platinum and palladium.
- the lubricant base oils of the present invention comprise paraffinic hydrocarbon components in which the branching is optimized.
- the lubricant base oils comprising paraffinic hydrocarbon components with optimized branching have high viscosities, low pour points, and exceptionally high VFs.
- the lubricant base oils of the present invention have kinematic viscosities at 100 °C greater than about 3.2 cSt, preferably between about 3.2 cSt and about 20 cSt.
- the lubricant base oils of the present invention comprise paraffinic hydrocarbon components having average carbon numbers of greater than about 27, preferably greater than about 30, and more preferably greater than about 27 and less than about 70.
- the American Petroleum Institute has classified base oils according to their chemical composition.
- Group III oils are very high viscosity index oils (>120) having a total sulfur content less than 300 ppm and a saturates content of greater than or equal to 90%.
- API Group III oils also are traditionally manufactured by severe hydrocracking and or wax isomerization.
- Lubricant base oils of the present invention are generally classified as API Group III base oils. When they are made from waxy feeds with a low total sulfur content, such as a Fischer-Tropsch feeds, the lubricant base oils will also have a total sulfur content less than 300 ppm.
- Lubricant base oils according to the present invention made from Fischer- Tropsch waxy feeds generally have total sulfur contents of less than about 5 ppm, saturates contents of greater than 95%, and total naphthene contents of between zero and about 8%, and preferably between zero and about 5%. Total sulfur is determined using ultraviolet fluorescence by ASTM D 5453-00.
- the lubricant base oils comprise paraffinic hydrocarbon components having less than 8 alkyl branches per 100 carbons, preferably less than 7 alkyl branches per 100 carbons, and more preferably less than 6.5 alkyl branches per 100 carbons. The branching at the two position, as determined by NMR branching analysis, is less than 20 wt%, preferably less than 15 wt%.
- the branching at the two plus three positions is less than 25 wt%, preferably less than 20 wt%. In addition the branching at the five or greater positions is greater than 50 wt%, preferably greater than 60 wt%.
- the free carbon indexes of the lubricant base oils of the present invention are generally greater than about 3, and preferably greater than about 5.
- the lubricant base oils of the present invention comprise paraffinic hydrocarbon components in which the extent of branching, as measured by the percentage of methyl hydrogens (BI), and the proximity of branching, as measured by the percentage of recurring methylene carbons which are four or more carbons removed from an end group or branch (CH 2 >4), are such that BI-0.5(CH 2 >4) is less than 12, while retaining low pour points.
- the lubricant base oils of the present invention have branching such that the BI - 0.5BP is less than 10, more preferably less than 8, and even more preferably less than 6, while retaining low pour points.
- Pour point is the temperature at which a sample of the lubricant base oil will begin to flow under carefully controlled conditions. Where pour point is given herein, unless stated otherwise, it has been determined by standard analytical method ASTM D 5950-02.
- the lubricant base oils with optimized branching according to the present invention have excellent pour points.
- the pour points of the lubricant base oils are less than -8 °C, preferably less than -9 °C, more preferably ⁇ -15 °C, and even more preferably less than -15 °C.
- Cloud point is a measurement complementary to the pour point, and is expressed as a temperature at which a sample of the lubricant base oil begins to develop a haze under carefully specified conditions. Cloud point may be determined by, for example, ASTM D 5773-95.
- the lubricant base oils with optimized branching according to the present invention have cloud points of less than 0 °C.
- the viscosity indexes of the lubricant base oils comprising paraffinic hydrocarbon components with optimized branching are extremely high and are greater than the Target Viscosity Index of the lubricant base oil, preferably greater than the Target Viscosity Index of the lubricant base oil plus 5.
- the range of kinematic viscosities of the lubricant base oils with optimized branching are greater than 3.2 cSt at 100 °C and may be between about 3.2 cSt and about 20 cSt at 100 °C.
- the % total naphthenes in the lubricant base oils are generally low or absent, due to the mild hydroisomerization dewaxing process used in the preparation. Generally, when naphthenes are present, the naphthenes are almost exclusively as mononaphthenes. In the lubricant base oils the total amount of naphthenes present is between zero and about 8 wt %, and preferably between zero and about 5 wt %.
- the naphthenes are measured using Field Ionization Mass Spectroscopy (FIMS), as described in the publication by Kramer, D.C., et al, "Influence of Group II & III Base Oil Composition on VI and Oxidation Stability," prepared for presentation at the 1999 AIChE Spring National Meeting in Houston, March 16, 1999.
- the percent total naphthenes content of the lubricant base oils of this invention is determined by taking the sum of the % mononaphthenes, % dinaphthenes, % trinaphthenes, % tetranaphthenes, % pentanaphthenes, and % hexanaphthenes measured by FIMS for each sample.
- the lubricant base oils of the present invention have extremely low amounts of aromatics and multi-ring naphthenes, the lubricant base oils have superior oxidation stability.
- One way to measure the oxidation stability of lubricant base oils is the Oxidator BN test, as described by U.S. Patent No. 3,852,207.
- the Oxidator BN test measures the resistance to oxidation by means of a Dornte-type oxygen abso ⁇ tion apparatus. R. W. Dornte "Oxidation of White Oils," Industrial and Engineering Chemistry, Vol. 28, page 26, 1936. Normally, the conditions are one atmosphere of pure oxygen at 340°F. The results are reported in hours to absorb 1000 ml of O by 100 g of oil.
- the catalyst is a mixture of soluble metal-naphthenates in kerosene simulating the average metal analysis of used crankcase oil.
- the additive package is 80 millimoles of zinc bispolypropylenephenyldithiophosphate per 100 grams of oil to be tested.
- Oxidator BN measures the response of a lubricant base oil in a simulated application. High values, or long times to absorb one liter of oxygen, indicate good oxidation stability. For general use, it is desired that the Oxidator BN of a lubricant base oil be above 7 hours. For the lubricant base oils of the present invention, the Oxidator BN value is greater than about 15 hours, preferably greater than about 30 hours.
- the lubricant base oils of the present invention may be used alone or may be blended with additional base oils selected from the group consisting of conventional Group I base oils, conventional Group II base oils, conventional Group III base oils, isomerized petroleum wax, polyalphaolefins (PAO), poly internal olefins (PIO), diesters, polyol esters, phosphate esters, alkylated aromatics, and mixtures thereof.
- Alkylated aromatics are synthetic lubricants produced from the alkylation of aromatics with haloalkanes, alcohols, or olefins in the presence of a Lewis or Bronstead acid catalyst. An overview of alkylated aromatic lubricants is given in
- alkylated aromatics are alkylated naphthalene and alkylated benzene.
- Alkylated aromatics have good low temperature properties, and may provide improved additive solubility and performance in blends with other base oils. Since the lubricant base oils of the present invention have excellent cold flow properties, high VFs, and high oxidation stability, they are ideal blending stocks for upgrading conventional lubricant base oils. It is prefe ⁇ ed that when the lubricant base oils of the present invention are blended with one or more additional lubricant base oils, the additional base oils be present in an amount of less than 95 wt % of the total resultant base oil composition.
- Lubricant base oils are the most important component of finished lubricants, generally comprising greater than 70% of the finished lubricants. Finished lubricants comprise a lubricant base oil and at least one additive. Finished lubricants may be used in automobiles, diesel engines, axles, transmissions, and industrial applications. Finished lubricants must meet the specifications for their intended application as defined by the concerned governing organization.
- the lubricant base oils of the present invention are useful in commercial finished lubricants. As a result of their excellent VFs and low temperature properties, the lubricant base oils of the present invention are suitable for formulating finished lubricants intended for many of these applications.
- additives which may be blended with the lubricant base oil of the present invention, to provide a finished lubricant composition include those which are intended to improve select properties of the finished lubricant.
- Typical additives include, for example, anti-wear additives, EP agents, detergents, dispersants, antioxidants, pour point depressants, VI improvers, viscosity modifiers, friction modifiers, demulsifiers, antifoaming agents, corrosion inhibitors, rust inhibitors, seal swell agents, emulsifiers, wetting agents, lubricity improvers, metal deactivators, gelling agents, tackiness agents, bactericides, fluid-loss additives, colorants, and the like.
- Other hydrocarbons such as those described in U.S. Patent Nos.
- U.S. Patent No. 5,096,883 relates to a substantially non- toxic base oil that consists essentially of branched-chain paraffins or branched-chain paraffins substituted with an ester functionality, or mixtures thereof, the base-oil preferably having between about 18 and about 40 carbon atoms per molecule and, more preferably, between about 18 and about 32 carbon atoms per molecule.
- U.S. Patent No. 5096,883 relates to a substantially non- toxic base oil that consists essentially of branched-chain paraffins or branched-chain paraffins substituted with an ester functionality, or mixtures thereof, the base-oil preferably having between about 18 and about 40 carbon atoms per molecule and, more preferably, between about 18 and about 32 carbon atoms per molecule.
- 5,189,012 relates to synthetic hydrocarbons selected from the group consisting of branched chain oligomers synthesized from one or more olefins containing a C 2 to C 14 chain length and wherein the oligomers have an average molecular weight of from 120 to 1000.
- the total amount of additives in the finished lubricant will be approximately 1 to about 30 weight percent of the finished lubricant.
- the lubricant base oils of the present invention have excellent properties including low pour point, high VFs, and excellent oxidative stability, a lower amount of additives may be required to meet the specifications for the finished lubricant than is typically required with base oils made by other processes.
- the use of additives in formulating finished lubricants is well documented in the literature and well known to those of skill in the art.
- Example 1 produced a lubricant base oil made from n-C 28 feed (purchased from Aldrich) using a Pt/SSZ-32 catalyst (0.3 wt% Pt) bound with 35 wt% Catapal alumina. The run was at 1000 psig, 0.8 LHSV, and 7 MSCF/bbl once-through H 2 .
- Reactor temperature was 575 °F.
- the effluent from the reactor was subsequently passed over a Pt-Pd/SiO 2 -Al O 3 hydrofinisbing catalyst at 450°F and, other than temperature, the same conditions were used as in the isomerization reactor.
- the yield of 600°F+ product was 71.5 wt%.
- the conversion of the wax to 600°F- boiling range material was 28.5 wt%.
- the conversion below 700°F was 33.6 wt%.
- the bottoms fraction from the run (75.2 wt%) was cut at 743°F to give 89.2 wt% bottoms (67.1 wt% on the whole feed).
- Table I The properties of the hydroisomerized oil bottoms are summarized below in Table I:
- the stripper bottoms were solvent dewaxed using methylethyl ketone (MEK)/toluene at - 15 °C.
- the wax content was 31.5 wt%, and oil yield was 68.2 wt%.
- a hydrotreated Fischer-Tropsch wax was isomerized over a Pt/SSZ-32 catalyst, which contained 0.3% Pt and 35% Catapal alumina binder. Run conditions were 560°F, 1.0 LHSV, 300 psig reactor pressure, and a once-through hydrogen rate of 6 MSCF/bbl. The reactor effluent passed directly to a second reactor, also at 300 psig, which contained a Pt/Pd on silica-alumina hydrofinishing catalyst. Conditions in that reactor were a temperature of 450°F and LHSV of 1.0. Properties of the hydrotreated Fischer-Tropsch wax are summarized below in Table IV. Conversion and yields, as well as the properties of the hydroisomerized stripper bottoms are summarized below in Table V.
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CN2004800303032A CN1867653B (en) | 2003-10-14 | 2004-09-13 | Lubricant base oils with optimized branching |
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Also Published As
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GB0421204D0 (en) | 2004-10-27 |
CN1867653A (en) | 2006-11-22 |
US20050077208A1 (en) | 2005-04-14 |
GB2407326A (en) | 2005-04-27 |
JP2007508441A (en) | 2007-04-05 |
NL1027242C2 (en) | 2005-12-23 |
BRPI0415265B1 (en) | 2014-06-17 |
AU2004281378A1 (en) | 2005-04-28 |
SG147434A1 (en) | 2008-11-28 |
NL1027242A1 (en) | 2005-04-15 |
CN1867653B (en) | 2010-06-16 |
JP5680028B2 (en) | 2015-03-04 |
WO2005037964A3 (en) | 2006-03-09 |
ZA200602725B (en) | 2008-05-28 |
JP5336703B2 (en) | 2013-11-06 |
BRPI0415265A (en) | 2006-12-12 |
JP2012193385A (en) | 2012-10-11 |
GB2407326B (en) | 2007-05-09 |
AU2004281378B2 (en) | 2010-03-11 |
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