CA2435132A1 - Compositions comprising higher diamondoids and processes for their separation - Google Patents

Abstract

Higher diamondoids ranging from tetramantanes through undecamantanes are disclosed in isolated and enriched forms. Methods for obtaining these higher diamondoids are disclosed, as well.

Description

COMPOSITIONS COMPRISING HIGHER DIAMONDOIDS
AND PROCESSES FOR THEIR SEPARATION
BACKGROUND OF THE INVENTION
Field of the Invention [0001] This invention is directed to isolated or enriched higher diamondoid components and to compositions comprising one or more higher diamondoid components. This invention is also directed to novel methods for the separation and isolation of higher diamondoid components into recoverable fractions from a feedstock containing one or more lugher diamondoid components.
References [0002] The following publications and patents are cited in this application as superscript numbers:
to [0003] 1 Fort, Jr., et al., Adamantane: Consequences of the Diamondoid Structure, Chem. Rev., :277-300 (1964) [0004] ' Sandia National Laboratories (2000), WoYld's FlYSt Diamond Mic~omachines Created at Sandia, Press Release, (2/22/2000) www.Sandia.gov.
[0005] ' Lin, et al., Natural Occu~~eface of Tetf°amantarae (Ca2Ha8),Pentamantane 15 (C26H3a) and Hexamantane (C3oH36) in a Deep Petroleum Reservoir; Fuel, (10):1512-1521 (1995) [0006] 4 Chen' et al., Isolation of High Purity Diamondoid F~actiofas and Components, U.S. Patent No. 5,414,189, issued May 9, 1995 ' [0007] ' Alexander, et al., Removal of Dianaoyadoid Compounds f~~m 2o Hydrocarbonaceous Factions, U.S. Patent No. 4,952,747, issued August 28, [0008] ° Alexander, et al., Purification ofHyd~ocanbonaceous Fractions, U.S. Patent No. 4,952,748, issued August 28, 1990 [0009] ' Alexander, et al., Removal of Diamondoid Compounds from Hydf~ocarbonaceous Ff°actions, U.S. Patent No. 4,952,749, issued August 28, 1990 25 [00010] b Alexander, et al., Pu~ificatiora of HydYOCa~bonaceous Fractions, U.S. Patent No. 4,982,049, issued January 1, 1991 [00011] y Swanson, Method for Diamondoid Extraction Using a Solvent System, U.S.
Patent No. 5,461,184, issued October 24, 1995 j00012] s° Partridge, et al., Shape-Selective Process fog Concentnatizzg Diamondoid-Corztainizzg Hydrocarbon Solvents, U.S. Patent No. 5,019,665, issued May 28, [00013] 11 Dahl, et al., Diamondoid Hydrocarbons as Indicators of Natural Oil C>~acking, Nature, , 54-57 (1999).
[00014] 1z McI~ervey, Synthetic Approaches to Laz"ge Diamondoid Hydrocarbons, Tetrahedron, 971-992 (1980).
[00015] 13 Wu, et al., High Viscosity Index Lubricant Fluid, U.S. Patent No.
5,306,851, issued April 26, 1994.
[00016] 14 Chung et al., Recent Development in High-Ezzengy Density Liquid Fuels, to Energy and Fuels, 641-649 (1999).
[00017] 15 Balaban et al., Systematic Classification and Nomenclature ofDiamond Hydrocarbons-l, Tetrahedjron, 34,3599-3609.
[00018] All of the above publications and patents are herein incorporated by reference in their entirety to the same extent as if each individual publication or patent was specifically and individually indicated to be incorporated by reference in its entirety.
[00019] Diamondoids are hydrocarbon molecules possessing amazingly rigid structures that contain carbon atom frameworks that are superimposable on the diamond crystal lattices (see FIG. 1). Adamantane, a ten-carbon molecule, is the smallest member of the diamondoid series, consisting of one cage-shaped diamond crystal subunit. Adamantane is commercially available and is widely used as a chemical intermediate. It can be synthesized and it can be recovered from petroleum. Diamantane contains two face-fused diamond subunits and triamantane three. These three materials have been synthesized and isolated from petroleum and have received research attention. Adamantane, diamantane and triamantane are classified as "lower diamondoids". Tetramantane, pentamantanes, etc., have characteristics (including multiple isomers, chirality and, above tetramantane, multiple molecular weight forms) that differ from the lower diamondoids, and are classified as "higher diamondoids".
While only one of the higher diamondoids has been synthesized, ideas concerning their structures and hypothetical properties have been set forth.
[00020] While adamantane, diamantane and triamantane show no isomers, it is 3o understood that there should be four different isomeric tetramantanes; four different shapes containing four diamond-cage subunits that can be superimposed on the diamond crystal lattice in different ways. Two of these isomers are enantiomers (mirror images of each other). Because the four tetramantanes each have ten faces to which the next diamond-cage unit could fuse, the number of pentamantanes increases over that of the tetramantanes. The number of possible isomers increases rapidly with each higher member of the diamondoid series. Also, because diamondoid crystal units can share more than a single face in some higher diamondoids, hydrogen to carbon ratios, i.e., the degree of condensation, also shows increasing variation, resulting in an increasing variety of molecular weights for each successive higher diamondoid family (FIG. 1). FIG. 2 is a table showing the different series of molecular weights calculated for higher diamondoids ranging from the tetramantanes to the undecamantanes.
[00021] Lower diamondoids are present in virtually every petroleum (oils and gas l0 condensates) as well as oil source-rock extracts.l l The natural concentration of diamondoids in petroleum varies by orders of magnitude. For instance, methyldiamantane concentrations in relatively low-maturity crude oils from the central valley of California, are on the order of a few parts per million (ppm). Low-maturity oils sourced from the Jurassic-age Smackover Formation, Gulf Coast, USA, have rnethyldiamantane concentrations of 20-30 ppm. Because 15 diamondoids show much greater stabilities than other petroleum hydrocarbons, deeply-buried petroleums, which have undergone substantial cracking as a result of intense heat may have methyldiamantane concentration in the thousands of ppms. It is not understood how higher diamondoids could be formed in natural systems, but it may involve a process requiring millions of years.
20 [00022] The higher diamondoids, which include the tetramantanes, pentamantanes, etc., have received comparatively little attention. In fact, prior to the work of inventors Dahl and Carlson embodied in United States Patent Application Serial No. 60/262,842 filed January 19, 2001 and numerous subsequent filings, these compo~.mds were hypothetical with only one such compound having been synthesized and a few others tentatively identified (but not 25 isolated). More specifically, McKervey, et al. reported the synthesis of anti-tetramantane in low yields using a laborious, multistep process.l2 Higher diamondoids cannot be synthesized by carbocation isoinerization methods useful for the lower diamondoids. Lin, et al. have suggested the existence of tetramantane, pentamantane and hexamantane in deep petroleum reservoirs from mass spectroscopy alone and without any attempt to isolate materials.3 The 3o possible presence of tetramantane and pentamantane in pot material recovered after a distillation of a diamondoid-containing feedstock has been discussed by Chen, et a1.4 Again, they made no attempt to isolate materials from this pot material.

[00023] As additional background, it is pointed out that the present inventors separately isolated the higher diamondoid cyclohexamantane, the most condensed member of the hexamantane series, and have made that invention the subject of its own patent application.
[00024] To summarize, the higher diamondoids have not been identified or isolated or otherwise provided with the following exceptions: iso-tetramantane -synthesizedl2 and unsubstituted cyclohexamantane - separately discovered by the present inventors.
SUMMARY OF THE INVENTION
[00025] This invention provides higher diamondoids, as enriched or isolated compounds.
l0 It also provides the individual higher diamondoid isomers (referred to as "higher diamondoid components" as enriched or isolated compounds for the first time. In addition, this invention provides processes with which the enriched and isolated higher diamondoids and higher diamondoid components can be obtained.
[00026] In accord with this invention we have isolated as crystals a variety of previously 15 unavailable higher diamondoids including tetramantanes, pentamantanes, hexamantanes, heptamantanes, octamantanes, nonamantanes and even decamantane. The isolation of the higher molecular weight higher diamondoids is especially unexpected in light of our finding that the relative abundance of each diamondoid family (tetra vs. penta, etc.) drops by a factor of about 10 for each crystal sub-unit added to the structure. This means that the decamantane 20 we have isolated, for example is about 10-6 times as prevalent in feedstocks as any of the tetramantanes, including the species which was synthesized in the prior art.

BRIEF DESCRIPTION OF THE DRAWINGS
[00027] FIG. 1 illustrates the cage-shaped structure of diamondoids and their correlation to diamonds. Specifically illustrated is the correlation of the structures of diamondoids to subunits of the diamond crystal lattice.
[00028] FIG. 2 is a table depicting the different molecular weights shown by each higher diamondoid series.
[00029] FIG. 3 illustrates the structure of the tetramantanes provided by this invention.
[00030] FIG. 4 illustrates that the four tetramantanes have carbon frameworks that correlate with the diamond lattice and can be viewed into their 100 lattice plane (FIG. 4A), 1o 110 lattice plane (FIG. 4B) and 111 diamond lattice plane (FIG. 4C).
[00031] FIG. 5 illustrates the structure of the pentamantanes provided by this invention.
[00032] FIG's. 6A, 6B, 6C and 6D illustrate the structure of the hexamantanes provided by this invention.
[00033] FIG's. 7A, 7B and 7C illustrate the structure of the heptamantanes provided by this invention. Only one of each enantiomer is shown.
[00034] FIG. 8 illustrates the structure of the octamantanes provided by this invention.
Only examples of the 500, 486, 472 and 432 molecular weight forms axe shown.
[00035] FIG. 9 illustrates the structure of the nonamantanes provided by this invention.
Only examples of each molecular weight family are shown.
[00036] FIG. 10 illustrates the structure of the decamantanes provided by this invention.
Only examples of each molecular weight family are shown.
[00037] FIG. 11 illustrates the structure of the undecamantanes provided by this invention. Only examples of each molecular weight family axe shown.
[00038] FIG. 12 gives a flow chart representing the various steps used in the isolation of higher diamondoid-containing fractions and individual higher diamondoid components.
Note that the steps can in some cases be used in a different sequence and possibly skipped as discussed in the Examples.

[00039] FIG's. 13A and 13B are compilations of the GC/MS and HPLC properties of various higher diamondoids included in this application.
[00040] FIG. 14 shows the two-HPLC column strategy used to isolate individual tetramantanes and pentamantanes.
[00041] FIG. 15 illustrates the size and shape of selected higher diamondoids relative to C6o (Buckminsterfullerene) and a representative carbon nanotube used in the development of molecular electronic devices. The carbon framework structures of the selected diamondoids can be found in FIG's 5, 6, 8, 9 and 10.
[00042] FIG. 16 illustrates the gas chromatogram of a gas condensate feedstock; one of l0 the original feedstocks used in the Examples (Feedstock A); showing minute concentrations of higher diamonds (not detectable on this scale).
[00043] FIG. 17 illustrates a high temperature simulated distillation profile of Feedstock B using the atmospheric distillation 650 °F + bottoms as feedstoclc.
This figure also illustrates the targeted cut points (1-10) we used for higher diamondoid isolations.
[00044] FIG's. 18A and 18B illustrate gas clmomatograms (FID) of distillate fraction #6 (Table 3B, FIG. 18) of Feedstock B 650 °F + distillation bottoms, and the resulting product of pyrolytic processing. These figures show that nondiamondoid components have been destroyed by the pyrolytic processing and that higher diamondoids, especially hexasnantanes, have been concentrated and made available for isolation.
[00045] FIG's. 19 and 20 are charts illustrating elution sequences for a variety of individual higher diamondoids (hexamantanes) on two different HPLC
chromatography colurmls: ODS and Hypercarb as discussed in Examples 1 and 7.
[00046] FIG's. 21A and 21B illustrate the preparative capillary gas chromatographic data for tetramantane isolations carried out in Examples 3 and 5. FIG. 21A shows cuts made on distillate fraction #33, Feedstock A. The bold face numbers refer to peaks of the tetramantanes. FIG. 21B shows peaks isolated and sent to the traps. The circled numbered peaks (2, 4, and 6) are the tetramantanes. It is noted that both enantiomers of the optically-active tetramantane are contained within one of these peaks.

[00047] FIG's. 22A, 22B and 22C illustrate photomicrographs of tetramantane crystals isolated from Feedstock A by preparative gas chromatography (FIG. 21). FIG.
22A was isolated from trap fraction #2, FIG. 22B was isolated from trap fraction #4, and FIG. 22C
was isolated from trap fraction #6. Because the two enantiomeric tetramantanes have identical GC retentions times in FIG. 21, one of the crystals contains both enantiomers.
[00048] FIG. 23A illustrates the gas chromatogram of Feedstock B atmospheric distillation hold up fraction, exemplified in Example 1, which was used as feedstock in pyrolytic processing. The hold up fraction is the material recovered from the distillation column after distillation of Feedstock B at approximately 650°F.
Tetramantanes #1 to #3 are 1 o shown.
[00049] FIG. 23B illustrates the gas chromatogram of the pyrolytic product from the starting material in FIG. 23A, i.e. the holdup fraction of Feedstock B
atmospheric distillation 650 °F + bottoms, showing the degradation of non-diamondoid components.
[00050] FIG.' S 24A and 24B compare the gas chromatograms of a tetramantane-containing starting mixture injected into a Vydac ODS HPLC column, and HPLC
cut #6 enriched in a tetramantane component.
[00051] FIG. 25 illustrates a preparative ODS HPLC isolation of the holdup fraction of Feedstock B atmospheric distillation 650 °F + bottoms, showing fractions taken at various retention times and the elution order of the tetramantane components and the location time of 2o fraction #12 used in subsequent isolations steps. FIG. 23 above, displays the gas chromatograph of this feedstock.
[00052] FIG. 26 illustrates the HPLC chromatogram of fraction 12 (FIG. 25) run on Hypercarb stationary phase with acetone mobile phase resulting in the isolation of tetramantane #2.
[00053] FIG's. 27A and 27B illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of tetramantane #1 isolated by using two different HPLC columns.
[00054] FIG's. 28A and 28B illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of tetramantane #2 isolated by using two different HPLC columns.

[00055] FIG's. 29A and 29B illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of tetramantane #3 isolated by using two different HPLC columns.
[00056] FIG's. 30A and 30B show the GC/MS total ion chromatogram (TIC) and mass spectrum of a methyltetramantane isolated using Hypercarb HPLC.
[00057] FIG's. 31A and 31B illustrate a preparative capillary gas chromatographic data for pentamantane isolations. FIG. 31A, shows the first column cut containing one of the pentamantanes from thermally treated Feedstock B. The material in that cut was separated on a second column. FIG. 31B, shows the second column peak sent to the trap.
Pentamantane #l, the first pentamantane to elute in GC/MS analysis, was isolated in trap 6.
[00058] FIG's. 32A and 32B show the GC/MS total ion chromatogram and mass spectrum of pentamantane #1 isolated by preparative capillary gas chromatography.
[00059] FIG. 33A is a photomicrograph of pentamantane #1 crystals isolated from Feedstock B by preparative gas chromatography (FIG. 31 and 32). FIG. 33B
illustrates a pentamantane co-crystal.
[00060] FIG. 34 illustrates the preparative HPLC Refractive Index trace (with negative polarity) of Feedstock B distillate cut pyrolysis product saturated hydrocarbon fraction showing HPLC fractions taken using octadecyl silane columns and acetone mobile phase.
Pentamantanes are numbered in order of their elution on the GC/MS analyses.
[00061] FIG. 35 illustrates the chromatogram of ODS HPLC fraction 11 (FIG. 34) run on Hypercarb stationary phase with acetone mobile phase resulting in the isolation of pentamantane #1.
[00062] FIG's. 36A and 36B illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of pentamantane #1 isolated using two different HPLC columns.
[00063] FIG's. 37A and 37B illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of pentamantane #2 isolated using two different HPLC columns.
[00064] FIG's. 38A and 38B illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of pentamantane #3 isolated using two different HPLC columns.

[00065] FIG's. 39A and 39B illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of pentamantane #4 isolated using two different HPLC columns.
[00066] FIG's. 40A and 40B illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of pentamantane #5 isolated using two different HPLC columns.
[00067] FIG's. 41A and 41B illustrate GClMS total ion chromatogram (TIC) and mass spectrum of pentamantane #6 isolated using two different HPLC columns.
[00068] FIG's. 42A and 42B illustrate the preparative capillary gas chromatographic data for hexamantane isolations. FIG. 42A, shows the first column cuts containing two of the hexamantanes from Feedstock B. FIG. 42B, shows the second column peaks isolated and l0 sent to the traps. From this procedure pure hexamantanes were isolated (FIG.'s 43 and 44), hexamantane #2, the second hexamantane to elute in our GC/MS assay, while hexamantane #8 is the eighth to elute.
[00069] FIG's. 43A and 43B illustrate the GC/MS total ion chromatogram and mass spectrum of a hexamantane #2 isolated by preparative capillary gas chromatography.
[00070] FIG's. 44A and 44B illustrate the GC/MS total ion chromatogram and mass spectrum of a hexamantane #8 highly concentrated by preparative capillary gas chromatography. A minor amount of a methylheptamantane (408 molecular weight) is present in this sample.
[00071] FIG. 45 illustrates a photomicrograph of hexamantane #2 crystals isolated from 2o Feedstock B by preparative gas chromatography (FIG. 42 and 44).
[00072] FIG. 46 illustrates a photomicrograph of hexamantane #8 crystals isolated from Feedstock B by preparative gas chromatography (FIG. 145 and 147).
[00073] FIG's. 47A and 47B illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of hexamantane #8 in ODS HPLC fraction #39.
[00074] FIG's. 48A and 48B illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of hexamantane #10 in ODS HPLC fraction #48.
[00075] FIG's. 49A and 49B illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of hexamantane #6 in ODS HPLC fraction #63.

[00076] FIG's. SOA and SOB illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of hexamantane # 2 greatly enriched in Hypercarb HPLC fraction #53.
[00077] FIG's. S 1A and S 1B illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of hexamantane # 13 isolated using two different HPLC columns.
[00078] FIG's. 52A and 52B illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of hexamantane # 7 isolated using two different HPLC columns.
[00079] FIG's. 53A and 53B illustrate GC/MS reconstructed ion chromatogram mlz and mass spectrum of a condensed "irregular" hexamantane (mol. wt. 382) in the saturated hydrocarbon fraction of the product of the pyrolytic processing of Feedstock B
distillation 1o fraction #6.
[00080] FIG's. 54A and 54B illustrate GC/MS reconstructed ion chromatogram m/z and mass spectrum of an irregular hexamantane (mol. wt. 382) in the ODS HPLC
fraction #36.
[0008I] FIG's. SSA and 55B illustrate GC/MS total ion chromatogram (TIC) and mass 15 spectrum of a methylhexamantane (mol. wt. 410) isolated in ODS HPLC
fraction #55.
[00082] FIG. 56 illustrates GC/MS total ion chromatogram (TIC) of cyolohexamantane and methylcyclohexamantane-containing ODS HPLC combined fractions #23-26.
[00083] FIG's. 57A and 57B illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of a methylcyclohexamantane #1 (mol. wt. 356) isolated using mufti-column 20 stationary phase HPLC (ODS followed by Hypercarb).
[00084] FIG's. S8A and 58B illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of a methylcyclohexamantane #2 (mol. wt. 356) isolated in high purity using multi-column stationary phase HPLC (ODS followed by Hypercarb).
[00085] FIG's. 59 and 60 show photomicrographs of crystals of 25 methylcyclohexamantane #1 and methylcyclohexamantane #2 isolated using two different HPLC columns.
[00086] FIG's. 61A and 61B illustrate the preparative capillary gas chromatographic data for heptamantane isolations. FIG. 61A, shows the first column cuts containing two of the heptamantanes from Feedstock B. FIG. 61B, shows the second column peaks isolated and sent to the traps. From this procedure pure heptamantane components were isolated (FIG 8 and 9) , heptamantane #1, the first heptamantane to elute in our GC/MS assay, and heptamantane #2 which is the second to elute.
[00087] FIG's. 62A and 62B illustrate the GC/MS total ion chromatogram and mass spectrum of a heptamantane #1 isolated by preparative capillary gas chromatography.
[00088] FIG's. 63A and 63B illustrate the GC/MS total ion chromatogram and mass spectrum of a heptamantane #2 highly concentrated by preparative capillary gas chromatography.
[00089] FIG. 64 illustrates photomicrographs of heptamantane #1 crystals isolated from Feedstock B by preparative gas chromatography (FIG's. 61 and 62).
[00090] FIG. 65 illustrates a photomicrograph of heptamantane #2 crystals isolated from Feedstock B by preparative gas chromatography (FIG's. 61 and 63).
[00091] FIG's. 66A and 66B illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of heptamantane component #1 in ODS HPLC fraction #45.
[00092] FIG's. 67A and 67B illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of heptamantane component #2 in ODS HPLC fraction #41.
[00093] FIG's. 68A and 68B illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of heptamantane component #9 in ODS HPLC fraction #61.
[00094] FIG's. 69A and 69B illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of heptamantane component #10 in ODS HPLC fraction #87.
[00095] FIG's. 70A and 70B illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of heptamantane # 1 greatly enriched in Hypercarb HPLC fraction #55.
[00096] FIG's. 71A and 71B illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of heptamantane #2 isolated using two different HPLC columns.
Heptamantane #2 was isolated from ODS HPLC fraction #41 (FIG. 67) using the Hypercarb HPLC
system.

[00097] FIG. 72 illustrates GC/MS reconstructed ion chromatogram m/z 420 showing a partially condensed heptamantane component (mol. wt. 420) in the ODS HPLC
fraction #61.
[00098] FIG. 73 illustrates the mass spectrum of the molecular weight 420 heptamantane in FIG. 72.
[00099] FIG's. 74A and 74B illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of a methylheptamantane component (mol. wt. 408) isolated in ODS HPLC
fraction #51.
[000100] FIG's. 75A and 75B illustrate the GC/MS total ion chromatogram and mass spectrum of octamantane #1 highly concentrated by high performance liquid chromatography.
[000101] FIG. 76 illustrates a photomicrograph of octamantane #1 crystals isolated from Feedstock B by high performance liquid chromatography.
[000102] FIG's. 77A and 77B illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of co-crystalline octamantane #3 and octamantane #5 (FIG. 78) grown from ODS
HPLC fraction #63.
[000103] FIG's. 78A and 78B illustrate photomicrographs of co-crystalline octamantane #3 and #5, crystal B was dissolved in cyclohexane and analyzed by GC/1VIS
(FIG. 77).
[000104] FIG's. 79A and 79B illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of octamantane #1 and octamantane #10 containing ODS HPLC fraction #80.
[000105] FIG's. 80A and 80B illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of an octamantane (molecular weight 500)-containing ODS HPLC fraction #92.
[000106] FIG's. 81A and 81B illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of a methyloctamantane (mol. wt. 460) in ODS HPLC fraction #94.
[000107] FIG's. 82A and 82B illustrate the GC/MS total ion chromatogram and mass spectrum of a nonamantane concentrated by high performance liquid chromatography.
[000108] FIG's. 83A and 83B illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of a nonamantane concentrated using two different HPLC columns.

[000109] FIG's. 84A and 84B illustrate a photomicrograph of a nonamantane crystal and a mass spectra of the dissolved crystal.
[000110] FIG's. 85A and 85B illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of a methylnonamantane (mol. wt. 512).
[000111] FIG's. 86A and 86B illustrate the GC/MS total ion chromatogram and mass spectrum of [ 1231241 (2)3], molecular weight 456, decamantane concentrated by high performance liquid chromatography.
[000112] FIG's. 87A and 87B illustrate GC/MS total ion chromatogram (TIC) and mass spectrum of [1231241(2)3], molecular weight 456, decamantane isolated using two different 1o HPLC columns.
[000113] FIG's. 88A and 88B illustrate a photomicrograph of [1231241(2)3], molecular weight 456, decamantane crystal and a mass spectra of the dissolved crystal.
[000114] FIG's. 89A and 89B illustrate GC/MS selected ion chromatogram (TIC) and mass spectrum of a decamantane (mol. wt. 496).
15 [000115] FIG's. 90A and 90B illustrate GC/MS total ion chromatogram (TIC) of two methyldecamantanes (mol. wt. 470), and the mass spectrum of the one eluting at 18.84 min.
in the GC/MS analysis.
[000116] FIG's. 91A and 91B illustrate illustrates the GC/MS selective ion chromatogram (mlz 508) and mass spectrum of pyrolysis product of Feedstock B atmospheric distillation 2o fraction #7 (Table 3) concentrating undecamantanes.
[000117] FIG's. 92A, 92B and 92C illustrate a GC/MS selected ion chromatogram (m/z 508) and mass spectrum of an undecamantane component (mol. wt. 508) eluting at 21.07 min. and the mass spectrum of a methylundecasnantane component (mol. wt. 522) eluting at 21.30 min.
25 [000118] FIG. 93 is a chart illustrating distillation cuts of a higher diamondoid-containing feedstock (Feedstock B, atmospheric distillation residue) showing cut selections to favor the enrichment of specific groups of higher diamondoids.

[000119] FIG. 94 shows the screw-like structures (right and left-handed) of [12341]
hexamantane.
DETAILED DESCRIPTION OF THE INVENTION
[000120] This Detailed Description is presented in the following subsections:
[000121] Definitions [000122] The Higher Diamondoids [000123] Feedstocks [000124] Isolation Processes to [000125] Utility [000126] Examples Definitions [000127] As used herein, the following terms have the following meanings.
[000128] The term "diamondoid" refers to substituted and unsubstituted caged compounds of the adamantine series including adamantine, diamantane, triasnantane, tetramantane, pentamantane, hexamantane, heptamantane, octamantane, nonamantane, decamantane, undecamantane, and the like and also including all isomers and stereoisomers thereof.
Substituted diamondoids preferably comprise from 1 to 10 and more preferably 1 to 4 alkyl substituents.
[000129] The teen "lower diamondoid components" or "adamantine, diamantane and triamantane components" refers to any and/or all unsubstituted and substituted derivatives of adamantine, diamantane and triamantane.
[000130] The term "higher diamondoid components" refers to any and/or all substituted and unsubstituted diamondoids corresponding to tetramantanes and above including tetramantanes, pentamantanes, hexamantanes, heptamantanes, octamantanes, nonamantanes, decamantanes, undecamantanes, and the like including all isomers and stereoisomers thereof.
Preferably, the higher diamondoids include substituted and unsubstituted tetramantanes, pentamantanes, hexamantanes, heptamantanes, octamantanes, nonamantanes, decamantanes and undecamantanes. FIG. 2 is a Table which shows representative higher diamondoids together with their molecular weights. The terms "diamondoid family", "tetramantane family" and the like are used to define a group of like "diamondoid components", having the same number of diamond crystal lattice cage units.
[000131] The term "tetramantane components" refer to any and/or all substituted and unsubstituted diamondoids corresponding to tetramantane.
to [000132] The term "pentamantane components" refer to any and/or all substituted and unsubstituted diamondoids corresponding to pentamantane.
[000133] The term "non-ionized diamondoid components" refers to higher diamondoid components which do not carry a charge such as a positive charge generated during mass spectral analysis wherein the phrase "higher diamondoid components" is as defined herein.
15 [000134] The term "non-ionized tetramantane components" refers to tetramantane components which do not carry a charge such as a positive charge generated during mass spectral analysis.
[000135] The term "non-ionized pentamantane components and diamondoid components higher than pentamantane" refers to pentamantane components and higher diamondoid 2o components larger than pentamantane which do not carry a charge such as a positive charge generated during mass spectral analysis.
[000136] The terms "selected higher diamondoid components" and the like refers to one or more substituted or unsubstituted higher diamondoids that are desired to be isolated or "enriched" in a product.
25 [000I37] The terms "nonselected higher diamondoid components" and the like refer to those higher diamondoids that are not "selected higher diamondoids".
[000138] The term "enriched" when used to describe the state of purity of one or more higher diamondoid components refers to such materials at least partially separated from the feedstock, and in the case of "enriched" individual higher diamondoid components, concentrated at least 25 and preferably at least 100 times the original concentration exhibited in the feedstock. Preferably "enriched" higher diamondoid or "enriched" higher diamondoid components make up at least 25%, especially at least 50% (i.e., 50-100%), more preferably at least 75% and yet more preferably at least 95% or even at least 99% by weight of the overall material in which they are present or in other words exhibit a weight purity of at least 25%, 50%, 75%, 95% or 99% of such material.
[000139] The term "feedstock" or "hydrocarbonaceous feedstock" refers to hydrocarbonaceous materials comprising recoverable amounts of higher diaxnondoids.
Preferably, such feedstocks include oil, gas condensates, refinery streams, oils derived from l0 reservoir rocks, oil shale, tar sands, and source rocks, and the like. Such components typically, but not necessarily, comprise one or more lower diamondoid components as well as non-diamondoid components. The latter is typically characterized as comprising components having a boiling point both below and above the lowest boiling point tetramantane which boils at about 350°C at atmospheric pressure.
Typical feedstocks may 15 also contain impurities such as sediment, metals including nickel, vanadium and other inorganics. They may also contain heteromolecules containing sulfur, nitrogen and the like.
All of these nondiamondoid materials are included in "nondiamondoid components" as that term is defined herein.
[000140] The term "nonselected materials" refers to the collection of feedstock 2o components that are not "selected higher diamondoids" and include "nondiamondoid components", "lower diamondoids" and "nonselected higher diamondoid" as these terms are defined herein.
[000141] The term "remove" or "removing" refers to processes for removal of non-diamondoid components and/or lower diamondoid components and/or nonselected higher 25 diamondoid components from the feedstock. Such processes include, by way of example only, size separation techniques, distillation, evaporation either under normal or reduced pressure, well head separators, sorption, chromatography, chemical extraction, crystallization and the like. For example, Chen, et a1.4 disclose distillation processes for removing adamantine, substituted adamantine, diamantane, substituted diamantane, and triamantane 3o from a hydrocarbonaceous feedstock. Size separation techniques include membrane separations, molecular sieves, gel permeation, size exclusion chromatography and the like.

[000142] The terms "distillation" or "distilling" refers to the fractionation processes in which materials are separated based on differences in vapor pressures, with high vapor pressure materials being taken overhead. Distillation can be carried out on hydrocarbonaceous feedstocks and on fractions otherwise obtained during the processing of hydrocarbonaceous feedstocks. In this context, most commonly, distillations are conducted under vacuum but also could be at atmospheric or even elevated pressures.
[000143] The terms "fractionation" and "fractionating" refer to processes in which materials in a mixture are separated from each other such as by differential solubility, differential vapor pressure, differential chromatographic affinity and the like.
to [000144] The terms "pyrolysis" and "thermal treating to pyrolyze" and the like refer to either atmospheric, reduced pressure or elevated pressure heating of the feedstock or a feedstock fraction to thermally degrade a portion of one or more components in the feedstock.
[000145] The term "non-diamondoid components of a feedstock" refers to components of 15 the feedstock or a feedstock fraction which are not diamondoid in character wherein the term "diamondoid" is as defined herein.
[000146] The term "retained" refers to retention of at least a portion of the higher diamondoid components found in the recovered feedstock when compared to the amount of such diamondoids found in the original feedstock. In a preferred embodiment, at least about 20 10 weight percent of the higher diamondoid components are retained in the recovered feedstock; more preferably, at least about 50 weight percent of the higher diamondoid components are retained in the recovered feedstock; and still more preferably, at least about 90 weight percent of the higher diamondoid components are retained in the recovered feedstock; each based on the total amount of such diamondoids found in the feedstock prior 25 to treatment.
[000147] The term "chromatography" refers to any of a number of well known chromatographic techniques including, by way of example only, column or gravity chromatography (either normal or reverse phase), gas chromatography, high performance liquid chromatography, and the like.

[000148] The term "alkyl" refers to straight and branched chain saturated aliphatic groups typically having from 1 to 20 carbon atoms, more preferably 1 to 6 atoms ("lower allcyls"), as well as cyclic saturated aliphatic groups typically having from 3 to 20 carbon atoms and preferably from 3 to 6 carbon atoms ("lower alkyls" as well). The terms "alkyl" and "lower alkyl" are exemplified by groups such as methyl, ethyl, propyl, butyl, isopropyl, isobutyl, sec-butyl, t-butyl, n-heptyl, octyl, cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl and the like.
The Higher Diamondoids [000149] As shown in FIG. 1, higher diamondoids are bridged-ring cycloalkanes that have to carbon-atom frameworks that can be superimposed on the diamond crystal lattice (FIG's. 1 and 4). They are the tetramers, pentamers, hexamers, heptamers; octamers, nonamers, decamers, etc. of adamantine (tricyclo[3.3.1.13'7]decane) or CloHI6 in which various adamantine units are face-fused. The higher diamondoids can contain many alkyl substituents. These compounds have extremely rigid structures and have the highest stability 15 of any compound with their formula. There are four tetramantane structures (FIG' S. 2 and 3); iso-tetramantane [1(2)3], ahti-tetramantane [121] and two enantiomers ofskew-tetramantane [123] (FIG. 3) with the more general bracketed nomenclature for these diamondoids in accordance to a convention by Balaban et al.ls There are ten pentamantanes (FIG. 5), nine have the molecular formula Cz6Hsa (molecular weight 344), and among these 2o nine there are three pairs of enantiomers represented by: [12(1)3], [1234], [1213] with the non-enantiomeric pentamantanes represented by: [12(3)4], [1(2,3)4], [1212].
There also exists a more strained pentamantane, [1231], represented by the molecular formula C25H3o (molecular weight 330). See FIG. 4. Hexamantanes exist with thirty-nine different structures (FIG. 6), twenty-eight having the molecular formula C3oH36 (molecular weight 25 396) and of these, six are aclural; ten more strained hexamantanes have the molecular formula Ca9H34 (molecular weight 382) and the remaining hexamantane [12312]
has the molecular formula C26H3p (molecular weight 342), also called cyclohexamantane because of its highly condensed circular structure. Heptamantanes are postulated to exist in one hundred and sixty possible structures; with eighty-five having the molecular formula C34H40 30 (molecular weight 448) (FIG. 7) and of these, seven are achiral, having no enantiomers.
Only one of each of the two enantiomer structures of the chiral heptamantanes is shown in FIG. 7. Of the remaining heptamantanes, sixty-seven have the molecular formula (molecular weight 434), and six have the molecular formula C32H36 (molecular weight 420).
These two heptamantane families have structures showing greater internal bond strain, with correspondingly lower stabilities and are not shown in FIG. 7. The remaining two have the molecular formula C3oH3~ (molecular weight 394) (FIG. 7). Octamantanes possess eight of the "diamond crystal cage units" and exist within five families of different molecular weight core structures (FIG. 2). Among the octamantanes, eighteen have the molecular formula C34H3g (molecular weight 446). FIG. 8 show, each of the 446 molecular weight octamantane isomers. Other octamantanes have the molecular formula C3gH44 (molecular weight 500). The remaining octamantane families, C37H4a (molecular weight 486), C36H4o l0 (molecular weight 472) and C33H3s (molecular weight 432) show greater bond strain and correspondingly lower stability. Nonamantanes exist within six families of different molecular weights having the following molecular formulas: C42H48 (molecular weight 552), C41H46 (molecular weight 538), C4oH44 (molecular weight 524), C38H42 (molecular weight 498), C37H4o (molecular weight 484) and C34H36 (molecular weight 444).
Additionally, decamantane exists within families of seven different molecular weights. Among the decamantanes, there is a single decamantane having the molecular formula C3sH36 (molecular weight 456) which is structurally compact in relation to the other decamantanes and has low internal bond strain. The other decamantane families have the molecular formulas: C46Hs2 (molecular weight 604), C4sHso (molecular weight 590), C44H48 (molecular 2o weight 576), C4zHq6 (molecular weight 550), C41H44 (molecular weight 536) and C38H4o (molecular weight 496). Undecamantanes (FIG. 11) exist as molecular formulas CsoHss (molecular weight 656), C49Hs4 (molecular weight 642), C48Hs2 (molecular weight 628), C46H50 (molecular weight 602), C4sH48 (molecular weight 588), C4aH44 (molecular weight 548), C41H42 (molecular weight 534), C39H4o (molecular weight 508). More preferred and less preferred higher diamondoids (FIG. 2) are based on their internal bond strain and corresponding stabilities which is reflected by their relative concentrations in the various feedstocks.
Feedstocks [000150] The higher diamondoids provided by this invention only exist in dilute 3o concentrations in solution in petroleum feedstocks.

[000151] In the processes of this invention, a feedstock is selected such that said feedstock comprises recoverable amounts of one or more selected higher diamondoid components.
Preferably, such feedstock comprises at least about 1 ppb of one or more higher diamondoid components, more preferably, at least about 25 ppb and still more preferably at least about 100 ppb. It is understood, of course, that feedstocks having higher concentrations of higher diamondoid components facilitate recovery of these components.
[000152] Preferred feedstocks include, for example, natural gas condensates and refinery streams having high concentrations of higher diamondoids. With regard to the latter, such refinery streams include hydrocarbonaceous streams recoverable from cracking processes, l0 distillations, coking and the lilce. Particularly preferred feedstocks include gas condensates recovered from the Norphlet Formation in the Gulf of Mexico and from the LeDuc Formation in Canada.
[000153] In one embodiment, the feedstocks used in the processes of this invention typically comprise non-diamondoid components having boiling points both below and above 15 the lowest boiling point higher diamondoid component selected for recovery as well as one or more lower diamondoid components. These feedstocks will usually contain a mixture of higher diamondoids. Depending upon which higher diamondoids are selected, some of these higher diamondoids may have boiling points below the selected higher diamondoid's boiling point. Typically, the lowest boiling point higher diamondoid component selected for 2o recovery will have a boiling point of greater than about 335°C. In typical feedstocks, the concentration of lower diamondoids to higher diamondoids is generally about 250:1 or higher. Moreover as illustrated in FIG. 18, typical feedstocks comprising higher diamondoid components also comprise non-diamondoid components.
[000154] In such feedstocks, selected higher diamondoid components often cannot be 25 effectively recovered directly from the feedstock because of their low concentrations relative to the nonselected components. Accordingly, the processes of this invention may entail removal of a sufficient amount of these contaminants from the feedstock under conditions to provide a treated feedstock from which the selected higher diamondoid components can be recovered.

Isolation Processes [000155] The general isolation processes of higher diamondoids are shown in FIG. I2.
[000156] In one embodiment, the removal of contaminants includes distillation of the feedstock to remove non-diamondoid components as well as lower diamondoid components and in some cases other nonselected higher diamondoids having boiling points less than that of the lowest boiling point higher diamondoid component selected for recovery.
[000157] In a particularly preferred embodiment, the feedstock is distilled to provide cuts above and below about 335°C, atmospheric equivalent boiling point and, more preferably, above and below about 345 °C atmospheric equivalent boiling point. In either instance, the to lower cuts, which are enriched in lower diamondoids and low boiling point non-diamondoid components are taken overhead and discarded and the higher boiling cut, which is enriched in higher diamondoids, is retained. It is understood, of course, that the temperature for the cut point during distillation is a function of pressure and that the above temperatures are referenced to atmospheric pressure. A reduced pressure will result in a lower distillation 15 temperature to achieve the same cut point whereas an elevated pressure will result in a higher distillation temperature to achieve the same cut point. The correlation of pressure/temperature from atmospheric distillation to either reduced pressure or elevated pressure distillation is well within the skill of the art.
[000158] Distillation can be operated to fractionate the feedstocks and provide several cuts 2o in a temperature range of interest to provide the initial enrichment of the selected higher diamondoids or groups of selected higher diamondoids. The cuts, which are enriched in one or more selected diamondoids or a particular diamondoid component of interest, are retained and may require further purification. The following Table illustrates representative fractionation points that may be used to enrich various higher diamondoids in overheads. In 25 practice it may be advantageous to make wider temperature range cuts which would often contain groups of higher diamondoids which could be separated together in subsequent separation steps.

Fractionation Points Most Preferred Preferred Lower Cut Higher Lower Cut Higher Cut Cut TemperatureTemperatureTemperatureTemperature Higher Diamondoid(C) (C) (C) (C) Tetramantanes349 382 330 400 Pentamantanes385 427 360 450 Cyclohexamantanes393 466 365 500 Hexamantanes 3i)3 466 365 500 Heptamantanes432 504 395 540 Octamantanes .154 527 420 560 Nonamantanes 463 549 425 590 Decamantanes 472 571 435 610 Undecamantanes499 588 455 62S

Useful Lower Cut Higher Cut TemperatureTemperature Higher Diamondoid(C) (C) Tetramantanes300 430 Pentamantanes330 490 Cyclohexamantanes330 550 Hexamantanes 330 550 Heptamantanes350 600 Octamantanes 375 610 Nonamantanes 380 650 Decamantanes 390 660 Undecamantanes400 675 [000159] It shall be understood that substituted higher diamondoids may accordingly shift these preferred cut-point temperatures to higher temperatures due to the addition of substituent groups. Additional temperature refinements will allow for higher purity cuts for l0 the diamondoid of interest. FIG. 93 provides further illustrations of how fractionation can provide cuts enriched in individual or multiple higher diamondoid components.
[000160] It will be further understood that fractionation can be stopped before a selected higher diamondoid is taken overhead. In this case the higher diamondoid can be isolated from the fractionation bottoms.

[000161] Other processes for the removal of lower diamondoids, unselected higher diaanondoids, if any, and/or hydrocarbonaceous non-diamondoid components include, by way of example only, size separation techniques, evaporation either under normal or reduced pressure, crystallization, chromatography, well head separators, reduced pressure and the like. Removal processes can utilize the larger sizes of the higher diamondoids to effect separation of lower diamondoids therefrom. For example, size separation techniques using membranes will allow a feedstock retained in the membrane to selectively pass lower diamondoids across the membrane barrier provided that the pore size of the membrane barrier is selected to differentiate between compounds having the size of higher diamondoid l0 components as compared to lower diamondoid components. The pore size of molecular sieves such as zeolites and the like can also be used to effect size separation.
[000162] In a preferred embodiment, the removal process provides for a treated feedstock having a ratio of lower diamondoid components to higher diamondoid components of no greater than 9:1; more preferably, no greater than 2:1; and even more preferably, the ratio is no greater than 1:1. Even more preferably, after removal of the lower diamondoid components) from the feedstock, at least about 10%, more preferably at least 50% and still more preferably at least 90% of the higher diamondoid components are retained in the feedstock as compared to that amount found in the feedstock prior to the removal.
[000163] When recovery of hexamantane and higher diamondoid components is desired 2o and when the feedstock contains non-diamondoid contaminants, the feedstock will also be generally subj ected to pyrolysis to effect removal of at least a portion of the hydrocaxbonaceous non-diamondoid components from the feedstock. The pyrolysis effectively concentrates the amount of higher diamondoids in the pyrolytically treated feedstock thereby rendering their recovery possible (FIG. 18).
[000164] Pyrolysis is effected by heating the feedstock under vacuum conditions or in an inert atmosphere, at a temperature of at least about 390°C and, preferably, from about 400 to about 550°C, more preferably from about 400 to about 450°C , and especially 410 to 430°C;
for a period of time to effect pyrolysis of at Least a portion of the non-diamondoid components of the feedstock. The specific conditions employed are selected such that 3o recoverable amounts of selected higher diamondoid components are retained in the feedstock. The selection of such conditions is well within the skill of the art.

[000165] Preferably, pyrolysis is continued for a sufficient period and at a sufficiently high temperature to thermally degrade at least about 10% of the non-diamondoid components (more preferably at least about 50% and even more preferably at least about 90%) from the pyrolytically treated feedstock based on the total weight of the non-diamondoid components in the feedstock prior to pyrolysis.
[000166] In yet another preferred embodiment, after pyrolysis of the feedstock, at least about 10%, more preferably at least about 50%, and still more preferably at least about 90%
of the higher diamondoid components are retained in the feedstock after pyrolytic treatment compared to that amount found in the feedstock prior to pyrolytic treatment.
l0 [000167] In a preferred embodiment, removal of lower diamondoids and low boiling point ~hydrocarbonaceous non-diamondoid components from the feedstock precedes pyrolytic treatment. However, it is understood, that the order of these procedures can be inverted such that pyrolysis occurs prior to removal of lower diamondoids from the feedstock.
[000168] The pyrolysis procedure, while a preferred embodiment, is not always necessary.
15 Tlus arises because the concentration of higher diamondoids can be sufficiently high in certain feedstocks that the treated feedstock (after removal of the lower diamondoid components) can be used directly in purification techniques such as chromatography, crystallization, etc. to provide higher diamondoid components. However, when the concentration or purity of higher diamondoid components in the feedstock is not at the level 2o to effect such a recovery, then a pyrolytic step should be employed.
[000169] Even when pyrolysis is employed, it is preferred to further purify the recovered feedstock using one or more purification techniques such as chromatography, crystallization, thermal diffusion techniques, zone refining, progressive recrystalization, size separation and the like. In a particularly preferred process, the recovered feedstock is first subjected to 25 gravity column chromatography using silver nitrate impregnated silica gel followed by HPLC using two different columns of differing selectivities to isolate the selected diamondoids and crystallization to provide crystals of the highly concentrated target higher diamondoids. Where lugher diamondoid concentrations are not high enough for crystallization to occur, further concentration by, for example, preparative capillary gas 3o chromatography may be necessary.

[000170] Enantioselective (chiral) stationary phases have been applied in chromatographic methods to effectuate further separations. High performance liquid chromatography methods also offer the possibility of using chiral solvents or additives to achieve resolution of enantiomers.
[000171] For example, separation of enantioneric forms of the high diamondoids can be achieved using several approaches. One such approach is spontaneous crystallization with resolution and mechanical separation. This approach to enantiomer resolution can be enhanced by preparation of derivatives or by the use of additives, chiral solvents, or various types of seed crystals. Another resolution option is chemical separation under kinetic or l0 thermodynamic control. Other suitable processes for enantiomer resolution include chiral separations, which can be performed using a gas chromatographic (GC) see "Chiral Chromatography", T.E. Beesley, et. al, Wiley, Johnson & Sons, January 1998, incorporated herein by references, by high performance liquid chromatographic (HPLC) and by supercritical fluid chromatographic (SFC) techniques, see Supercritical fluids in Chromatography and Extraction", R.M. Smith, Elsevier Science, December 1997, incorporated herein by references.
Utility [000172] The processes of this invention provide compositions enhanced in higher diamondoids. These higher diamondoids are useful in micro- and molecular-electronics and nanotechnology applications. In particular, the rigidity, strength, stability, thermal conductivity, variety of structural forms and multiple attachment sites shown by these molecules makes possible accurate construction of robust, durable, precision devices with nanometer dimensions. FIG. 15 shows the size and shapes of selected higher diamondoids relative to molecular components (Buckminsterfullerene and carbon nanotubes) employed in the development of molecular electronic devices.
[000173] The higher diamondoids are three-dimensional nanometer-sized units showing different diamond lattice arrangements. This translates into a great variety of shapes and sizes of these extremely rigid nanostructures, for example, [121(3)4]
hexamantane is "T"
shaped, [12134] is "L" shaped, and [1(2)3(1)2] is flat with four lobes.
[12(3,4)12]
3o heptamantane has a cross-shaped structure while [121234] is "L" shaped.
[12312]
hexamantane has a disc-like structure. [121321] heptamantane is disc-shaped with one co-planar lobe, while [1213(1)21] octamantane is disc-shaped with two, opposing, co-planar lobes. [1232(1)3] octamantane is wedge-shaped. [121(2)32(1)3] nonamatane has a triangular plate-like structure. [1231241(2)3] decamantane is a perfect octagon, while [121231212]
decamantane is rectangular plate-like structure. [123(1,2)42143] undecamantane is an elongated pyramid. A variety of other shapes exist among the higher diamondoids which may serve in applications in nanotechnology and nano-structured materials which depend upon specific geometries. The carbon-framework structures of the tetramantanes to the undecamantanes are shown in FIG's 3 to 11.
[000174] Higher diamondoids also include a series of rod-like structures of varying to lengths. The tetramantane with the sequence "121" is the first member of this rod-shaped structural series, [ 1212] pentamantane is next, followed by [ 12121 ]
hexasnantane, and so on.
Each added diamond cage increases the length of the rod by about 0.3 nm, with [1212]
pentamantane having a length of about 1.1 nm.
[000175] The [1(2)3] tetramantane begins a more compact series, a flat-topped, pyramid-15 like structure (FIG. 3). [1(2,3)4] pentamantane (FIG. 5) follows this trend, being a perfect tetrahedral pyramid.
[000176] Higher diamondoids also include screw-like structures of varying lengths. The first chiral diamondoid is the tetramantane with sequence 123. We have specified the two enantiomers of 123 tetramantane as A and B. Their structures can also be implied by the 2o sequences 123 and 124 by a modification of the Balaban nomenclature. These two diamondoids have left (counter-clockwise), i.e., tetramantane A, and right (clockwise) (tetramantane B)-hand helix or screw-like structures, both representing a partial-turn of the helix. Unfortunately, the Balaban nomenclature does not provide a way of specifying the left and right helical forms, only demonstrating that there exists two forms. This sequence 25 continues with the progression 1234 and 1243 (i.e., A and B) for pentamantane (FIG. 5), 12341 and 12431 (again, A and B), for hexamantane (FIG. 6), and so on. The hexamantane members complete one full turn of a right and a left-handed helix for these screw-shaped nanostuctures (FIG 94).
[000177] These special structural characteristics set higher diamondoids apart from acyclic 30 molecules, from condensed-ring systems and even from bridged-ring counterparts. The great stability, nanometer size, variable yet rigid geometry, well defined distances for places of attachment, nonplanar bridgeheads lead to their unique features. I~ue to the rigidity, specialized geometry, 3-dimensional shape and nanometer size of the higher diamondoid components, it is expected that molecular aggregates and building blocks comprising them will enable construction and synthesis of a unprecedented array of desirable materials that will find applications in molecular electronic computing devices, reduced-size machines such as molecular robots and self replicating manufacturing systems. Alternatively, the higher diamondoids may be used as novel materials of construction with special chemicals, optical, electric and thermal conductivity properties for coatings, film layering and other applications taking advantage of the diamond-like properties, etc. Novel uses of higher diamondoid-to containing materials in the field of microelectronics are disclosed.
Embodiments include, but not limited to, thermally conductive films in integrated circuit packaging, low-k dielectric layers in integrated circuit multilevel interconnents, thermally conductive adhesive films, thermally conductive films in thermoelectric cooling devises, passivation films for integrated circuit devices (ICs), and field emission cathodes.
[000178] In addition, these higher diamondoids can also be used in a high quality lubricating fluid which exhibits a high Viscosity Index and a very low pour point.l3 When so employed, these fluids comprise a fluid of lubricating viscosity and from about 0.1 to 10 weight percent diamondoids.
[000179] Still further, these higher diamondoids can be used as high density fuels in the manner described by Chung, et a1.14, incorporated herein by reference.
[000180] The following examples are offered to illustrate this invention and are not to be construed in any way as limiting the scope of this invention. Unless otherwise stated, all temperatures axe in degrees Celsius.

EXAMPLES
[000181] As used herein and in the Figures, the following abbreviations have the following meanings. Any abbreviation not defined below has its generally accepted meaning.
API = American Petroleum Institute ~

atm eqv - atmospheric equivalent btms - bottoms FOR Traps - end of run traps 1o fid = flame ionization detector g - grams GC = gas chromatography GC/MS - gas chromatography/mass spectroscopy h - hour HPLC - high performance liquid chromatography HYD RDG - hydrometer reading L - liter min = minute mL = milliliters 2o mmol - millimols N - normal pA = pico amps ppb = parts per billion ppm= parts per million RI - refractive index SIM DIS - simulated distillation ST = start TIC = total ion current TLC - thin layer chromatography VLT - vapor line temperature VOL PCT - volume percent v/v = volume to volume wt - weight WT PCT - weight percent Introduction [000182] The steps used in the various Examples are shown schematically in FIG. 12.
[000183] Example 1 describes a most universal route for isolating higher diamondoids components which can be applied to all feedstocks. This process uses HPLC
(Step 7, FIG.
12) as its final isolation step.

[000184] Example 2 describes a variation of the process of Example 1 in which preparative gas chromatography (Step 7', FIG. 12) replaces HPLC as the final isolation step.
[000185] Example 3 describes a variation of the process of Example 1 in which the pyrolysis (Step 5, FIG. 12) is omitted. As shown optionally in FIG. 12, the liquid chromatographic step (Step 6, FIG. 12) is also omitted. These variations generally have applicability only with selected feedstocks and generally when tetramantanes, pentamantane and cyclohexamantane are the target higher diamondoids.
[000186] Example 4 describes yet another process variation in which the final products of Examples 1 and 3 are subjected to preparative gas chromatography purification to give to further separation of higher diamondoid components (Step 8, FIG. 12).
[000187] Example 5 describes the enrichment and isolation of the tetramantane components.
[000188] Example 6 describes the enrichment and isolation of the pentamantane components.
[000189] Example 7 describes the enrichment and isolation of the hexamantane components.
[000190] Example 8 describes the enrichment and isolation of the heptamantane components.
[000191] Example 9 describes the enrichment and isolation of the octamantane components.
[000192] Example 10 describes the enrichment and isolation of the nonamantane components.
[000193] Example 11 describes the enrichment.and isolation of the decamantane components.
[000194] Example 12 describes the enrichment and isolation of the undecamantane components.

[000195] It will be understood that it is possible to vary the order of the various distillation, chromatography and pyrolysis steps, although the order set forth in Example 1 has given the best results.

[000196] This Example has seven steps (see Flow Chart in FIG. 12).
[000197] Step 1. Feedstock selection [000198] Step 2. GCMG assay development [000199] Step 3. Feedstock atmospheric distillation l0 Step 4. Vacuum fractionation of atmospheric distillation residue Step 5. Pyrolysis of isolated fractions Step 6. Removal of aromatic and polar nondiamondoid components [000203] Step 7. Multi-column HPLC isolation of higher diamondoids a) First column of first selectivity to provide fractions enriched in specific higher diamondoids.
b) Second column of different selectivity to provide isolated higher diamondoids.
[000204] This example is written in terms of isolating several hexamantanes.
As will be shown in Examples 5-12 it can be easily adapted to isolate the other higher diamondoids.
Step 1- Feedstock Selection [000205] Suitable starting materials were obtained. These materials included a gas condensate, Feedstoclc A (FIG. 16), and a gas condensate containing petroleum components, Feedstock B. Although other condensates, petroleums, or refinery cuts and products could have been used, these two materials were chosen due to their high diamondoid concentration, approximately 0.3 weight percent higher diamondoids, as determined by GC and GCIMS.
Both feedstocks were light colored and had API gravities between 19 and 20° API.
Step 2 - GC/MS Assay Development [000206] Feedstock A was analyzed using gas chromatography/mass spectrometry to confirm the presence of target higher diamondoids and to provide gas chromatographic retention times for these target materials. This information is used to track individual target higher diamondoids through subsequent isolation procedures. FIG. 13A is a table that lists typical GC/MS assay information for the hexamantanes (GC retention times, mass spectral molecular ion (M+) and base peak). This table (FIG. 13A) also contains similar GC/MS
assay information for other higher diamondoids. While relative GC retention times are approximately constant, non-referenced GC retentions vary with time. It is recommended that GC/MS assay values be routinely updated especially when GC retention time drift is l0 detected.
Step 3 - Feedstock Atmospheric Distillation [000207] A sample of Feedstock B was distilled into a number of fractions based on boiling points to separate the lower boiling point components (nondiamondoids and lower diamondoids) and for further concentration and enrichment of particular higher diamondoids i5 in various fractions. The yields of atmospheric distillate fractions of two separate samples of Feedstock B are shown in Table 1, below and are contrasted to simulated distillation yields.
As seen from Table 1, the simulated distillation data is in agreement with the actual distillation data. The simulated distillation data were used to plan subsequent distillation processes.

TABLE l: Yields of Atmospheric Distillation Fractions from Two Separate Runs of Feedstock B
Cut (F) Sim Dis Feedstock B (RunDifference Est.'d Yields 2) (Wt Yields (Wt %) To 349 8.0 7.6 0.4 349 to 491 57.0 57.7 -0.7 491 to 643 31.0 30.6 0.4 643 and hi 4.0 4.1 -0.1 her Cut (F) Sim Dis Feedstock B (RunDifference Est.'d Yields 1) (Wt Yields (Wt %) %

To 477 63.2 59.3 3.9 477 to 515 4.8 7.3 -2.5 S15 to 649 28.5 31.2 -2.7 649 and hi 3.5 2.1 1.4 her Step 4 - Fractionation of Atmospheric Distillation Residue by Vacuum Distillation [000208] The resulting Feedstock B atmospheric residium from Step 3 (comprising 2-4 weight percent of the original feedstock) was distilled into fractions containing higher diamondoids as shown in FIG's. 17 and 93). The feed to this high temperature distillation l0 process was the atmospheric 650 °F + bottoms. Complete Feedstock B
distillation reports are given in Tables 2A and 2B. Tables 3A and 3B illustrate the distillation reports for Feedstock B 650°F + distillation bottoms.

N ~ O ~ NO

O U N Q ~ O
O M ~ M

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V oo M o~ o H v M G1 l~ ~ ~ O 01O

p O M ~ NO

N

g ~ 0 0 OU . o 00 ~ N O M O

In N O
E.., o 'c 'D C O o, o U ' 0 ~

Z ~ ~ t( M O d O

H
' w ~ o O N N M M
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~r O

w ~ O

U r.~ O oo r.,vo vo 'r?
~

OW O v0 O

W

..r ~ ~ O
~

r.y ~ O ~ O ~ N O M O GMT M01 ~

~ i~ A
~

d~
N

r, t f1 H

a ~ A ~ w o c o U, o N r,, O y 00 ~,C
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-, N M ~ ~.. p ., W

o ° ~ ,-: W o U?
M N ~ ~ ~ H
H
a$
O O ~ O ~ O O O
0°0 0°0 ~ ° ~ 0°0 P~ ~C
''' ° a o N
M N ~ ~ O ~ N
x o U' U' ~ o ~ ~ ~° ° N .,..,, ~c o d.
~~' O~ ~°n e~ ON ° °MO°°oo°,N
a w x~

w a~~ ° ~a ~ ° °
~a x ~°
°
A
O r-I N ~ ~ M .~
x A ~ "~ ~ ~ ~ ~ o ~~ ~~~aA A
M M M ~ ~ M M ~
c~ ~ H
m p a ~ ~~-' ~ U O ~ ~ ~ U A
0 0 °o, '.~ o 0 H a~ ~ ~ ~°n v°~ ,°,~ ''3 0 0 U w W ~ N N M ~ M
O
'' 00 r1 00 ~ I~ M
O7 . 1/j 01 O ~ I~ M
F~ U ~ ~ O ~ W N M '~ V 'Md' A
M N M

TABLE 3A: Vacuum Distillation Report for Feedstock B
Feedstock B - Atmospheric distillation resid 650°F + bottoms Column Used: Sarnia Hi Vac TEMP PRESSUREREFLUX CUT VOLUME WEIGHT API
ERATURE ml G GRAVITIES
DEGREESF

VAPOR POT TORR RATIO NO OBSERVED GO
F

EQV. RDG F

315 601.4350 5.000 START
OVERHEAD

344 636.8382 5.000 300 READING

342 644.9389 4.000 500 READING

344 656.3395 3.300 1 639 666.4 7.8 138.04.1 353 680.1411 2.500 400 READING

364 701.6430 2.100 2 646 G6G.9 9.4 138.05.G

333 736.0419 0.400 200 READING

336 751.9432 0.300 3 330 334.3 12.4 139.08.3 391 799.9468 0.500 4 173 167.7 19.0 139.014.5 411 851.6500 0.270 5 181 167.3 26.8 139.021.7 460 899.8538 0.360 G 181 167.1 27.0 139.021.9 484 950.3569 0.222 7 257 238.4 26.2 139.021.2 Shut down distillation to check of tem erature limits with customer.
(Drained tra material 5.3 rams) 472 935.7576 0.222 START
OVERHEAD

521 976.3595 0.340 8 91 85.4 23.7 139.018.9 527 999.9610 0.235 9 85 80.8 23.0 139.018.2 527 1025.6624 0.130 10 98 93.8 21.6 139.016.9 Drained rams remainin (--4 tra rams material of of water) 16.5 MID END OF 20 17.8 (mathematically AND RUN combined) TRAPS

DISTILLED

COLUMN 4 4.0 0.0 0.0 3.4 HOLDUP

BOTTOMS 593 621.8 11.0 214.03.4 RECOVERED 3298 3311.7 FEED 3298 3326.3 18.0 234.08.G
CHARGED

LOSS -5 14.6 ~n o a E"~~ lNpGV7O OC ~O0000N G v-I ~ M

o,osoN 'nv~oor vios~ y o, o '"' P~I~ ~ ~V7V7V7l~N NN O ~ O H ~

O
O O O'V'M NL~t MN N ~ et ~ 'et 0 0 0 o o,~V;rroo,~ ~ ~ ~ d;

PIN N r-IV7N V7l~N NN O r1 O O~O~1 O
M ~' ~ r N

G Vo o oN V w,~ ~ ~o , ~ o o 'v'v , , -, ~ ~ e-HInInInl N NN O H O rl ~ ~ o0 0 oN ~ ~M ~ r ~

N N ~ ~ o O ~ O
O

inIri~l N NN

G

O

V1~ NN ~OetI~00NM 01 O\ O 01 WM N NO~M N\OO ~f7M 00 00 O M

0 0 00~10N10N1~ 0~10~10~0 O O O

W r1v-Ir-1b O ~O O OO v--1v-1 r1 rl O O

~

O o ,.W .-i~ N I O~N O~NOy ~

y O~'N 00H N NN ~ ~~ M M 00 O~

O o W w ~

'-W D

c~n I~ 00 M
N O vC\\OOM r-1e-1l M 01 01 i-a M e1'Mt~0000N r-~i17OG O~ O N N
~O\OMv-1r-1r-1N 0100O~<t ~ N M ~M

O

M ~ ~ H

a ~ ~ ~ z ~

; <rO~Ml M e-~et~:~00 00 o0 ~ ~ON
~ ~Dv0t~ r r00 H
d V c ~O~Oe~D~O~DM M OM O N l~ M ~tM A
' V~~D~OM~ ~ ~N 00000~'ct'~D ~ M OM
M

~ ~

H
~

~ H

~ON NO N OO ~OpN

O M O InO N O~ t~OO
~O ~

H

~ i ii i~ i i~

~ I i C/W-I~ONN O NO O \D N
o v~o~ o ~o inr V

~D~Dl~l~0000OvO~01 ~ V~
<",q o A U' ~ rn a~ . W U
U ~", f=

, O O W
~

U r-~N M'd'~ \Ol 0001~ ~ W H O~
r.~

TABLE 4: Elemental Composition of Feedstock S
Anal ses on ock Feedst B
650+F
Resid Measured Value Nitrogen 0.991 wt%

Sulfur 0.863 wt%

Nickel 8.61 ppm -.

Vanadium < 0.2 ppm [000209] Table 4 illustrates the partial elemental composition of Feedstock B
atmospheric distillation (650°F) residue including some of the identified impurities. Table 4 displays the weight percent nitrogen, sulfur, nickel and vanadium in Feedstoclc B
atmospheric distillation residue. Subsequent steps remove these materials.
Step 5 - Pyrolysis of Isolated Fractions [000210] A high-temperature reactor was used to pyrolyze and degrade a portion of the nondiamondoid components in various distillation fractions obtained in Step 4 (FIG. 12) thereby enriclung the diamondoids in the residue. The pyrolysis process was conducted at l0 450 °C for 19.5 hours. The gas chromatogram (FID) of fraction #6 (Table 3B) is shown in FIG. 18A. FIG. 18B is the chromatogram for the product of pyrolysis. A
comparison of these chromatograms shows that pyrolysis has removed major nondiamondoid hydrocarbons and has significantly increased the higher diamondoid concentration, especially the hexamantanes. A 500 mL PARR~ reactor from PARR Instrument Company, Moline, 15 Illinois was used in this pyrolysis step.
Step 6 - Removal of Aromatic and Polar Nondiamondoid Components [000211] The pyrolysate produced in Step 5 was passed through a silica-gel gravity chromatography column (using cyclohexane elution solvent) to remove polar compounds and asphaltenes (Step 6, FIG. 12). The use of a silver nitrate impregnated silica gel (10 2o weight percent AgN03) provides cleaner diamondoid-contaiung fractions by removing the free aromatic and polar components. While it is not necessary to use this chromatographic aromatic separation method, it facilitates subsequent steps.
Step 7 - Multi-column HPLC Isolation of Higher Diamondoids [000212] An excellent method for isolating high-purity higher diamondoids uses two or more HPLC columns of different selectivities in succession.
[000213] The first HPLC system consisted of two Whatman M20 10/50 ODS columns operated in series using acetone as mobile phase at 5.00 mL/min. A series of HPLC
fractions were taken (see FIG. 19). Fractions 36 and 37 were combined and taken for further purification on a second HPLC system. This combined fraction (36 and 37) contained hexamantanes #7, #11 and #13. (FIG. 19, also see FIG. 13B).
[000214] Further purification of this combined ODS HPLC fraction was achieved using a Hypercarb stationary phase HPLC column having a different selectivity in the separation of l0 various hexamantanes than the ODS column discussed above. FIG. 20 shows elution times of the individual hexamantanes on the Hypercarb HPLC column (with acetone as a mobile phase).
[000215] The differences in elution times and elution order of hexamantanes on ODS and Hypercarb HPLC columns are seen by comparing these two FIG's. 19 and 20. For example, 15 Hexamantanes #11 and #13 elute together on the ODS HPLC system (FIG. 19) but in separate fractions (fractions 32 and 27, respectively) on the Hypercarb system (FIG. 20).
[000216] The different elution orders and times of selected higher diaxnondoids on these two systems can be used to separate co-eluting higher diamondoids. It can also be used to remove impurities. Using this method on combined ODS HPLC fractions 36 & 37, 2o appropriate Hypercarb HPLC fractions were taken thus providing high-purity hexamantane #13 (FIG'S. 51A and S1B). Other ODS HPLC fractions and Hypercarb HPLC cut points could be used to isolate the remaining hexamantanes. This isolation strategy is also applicable to the other higher diamondoids although elution solvent compositions can vary.
[000217] The ODS and Hypercarb columns can also be used in reverse order for these 25 isolations. By using similar methodology as above, i.e. fractionating hexamantane-containing ODS fractions using the Hypercarb or other suitable column and collecting at corresponding elution times can lead to the isolation of the remaining hexamantanes in high purity. This is also true of the other higher diamondoids from tetramantanes to undecamantanes, including substituted forms.

[000218] Steps 1, 2, 3, 4, 5 and 6 of Example 1 were repeated (FIG. 12). The following variation of Step 7 was then carried out.
Step 7':
[000219] A two-column preparative capillary gas chromatograph was used to isolate hexamantanes from the product of Example 1, Step 6. The cut times for the hexamantanes were set for the first preparative capillary the GC column, methyl silicone DB
-1 equivalent, using the retention times and patterns from GC/MS assay (Example 1, Step 2).
The results are shown in FIG. 42A, two cuts identified as "peaks cut and sent to column 2", were taken l0 which contains two of the hexamantane components from Feedstock B. The preparative capillary gas chromatograph used was manufactured by Gerstel, Zizc., Baltimore, Maryland, USA.
[000220] The first column was used to concentrate the higher diamondoids, such as hexamantanes by taking cuts that were then sent to the second column (see FIG.

illustrated for hexamantane #2 and #8). The second column, phenyl-methyl silicone, a DB-17 equivalent, further separated and purified the hexamantanes and then was used to isolate peaks of interest and retain them in individual traps (traps 1-6). GC trap fraction 1 contained crystals of hexamantane #2. GC trap fraction 3 contained crystals of hexamantane #8.
Subsequent GC/MS analysis of trap #1 material (FIG. 43A and B) showed it to be high 2o purity hexamantane #2 based upon the GC/MS assay of Step 2. Similarly, the GC analysis of trap #3 material (FIG. 44A and B) showed it to be primarily hexamantane #8.
Photomicrographs of hexamantane #2 and #8 crystals (analyzed in FIG's. 43 and 44) axe shown in FIG's. 45 and 46. This procedure could be repeated to isolate the other hexamantanes. This is also true of the other higher diamondoids.

[000221] Steps 1, 2, 3; and 4 (FIG. 12) of Example 1 were repeated using Feedstock A.
Feedstock A is especially low in nondiamondoids in the atmospheric residue fraction recovered in Step 4. The pyrolysis Step (5) of Example 1 may be omitted especially when the higher diamondoids being sought are tetramantanes, pentamantanes and cyclohexamantane. In this case the fractions removed in Step 4 go directly to Steps 6 and 7 in Example 1 or directly to Step 7 in Example 2 (FIG. 12). This process variation can be applied to lower-boiling tetramantane-containing fractions of Feedstock B as well. However, pyrolysis is highly desirable where significant nondiamondoid components are present.
[000222] A fraction corresponding in cutpoint to fraction #1 of Step 4 (see distillation Table 3, Example 1 and FIG. 17) was taken from this feedstock. This fraction was further fractionated by preparative capillary gas chromatography similar to the processing shown in Step 7' of Example 2 (FIG. 12).
[000223] -A two-column preparative capillary gas chromatograph was then used to isolate the target tetramantanes from the distillate fraction cleaned-up by column chromatography l0 (Step 6, FIG. 12). Using the retention times and patterns from the GC/MS
assay (from Step 2 of Example 1), the cut times for the target diamondoids (e.g., tetramantanes) were set for the first preparative capillary GC column, methyl silicone DB-1 equivalent.
The results are shown on the top of FIG. 21 identified as cuts 1, 2 and 3.
[000224] The first column was used to concentrate the target diamondoids (e.g., tetramantanes) by taking cuts that were then sent to the second column (phenyl-methyl silicone, a DB-17 equivalent) (see the bottom of FIG. 21). The second column further separated and purified the target diamondoids and then sent them into individual traps (traps 1-6). GC traps 2, 4 and 6 contained the selected tetramantanes (FIG. 21).
[000225] The highly concentrated tetramantane higher diamondoids were then allowed to 2o crystallize in the trap or dissolved and recrystallized from solution.
Under the microscope at 30X magnification, crystals of the tetramantanes were visible in preparative GC traps 2, 4, and 6 (see FIG. 22). Where concentrations were not high enough for crystallization to occur, further concentration by preparative GC was necessary. The process would also work to isolate other higher diamondoids from Feedstock A.

EXAMPLE 4: Preparative GC of HPLC Fractions [000226] With the heptamantanes, octamantanes and higher diamondoids, etc., it may be desirable to further fractionate the HPLC products obtained in Example 1, Step 7. This can be carried out using preparative capillary gas chromatography as described in Example 2, Step 7'.
[000227] The following higher diamondoid components were isolated and crystallized: all of the tetramantanes from both Feedstocks A and B, all pentamantanes (mol. wt.
344) isolated from Feedstock B; two hexamantane crystals (mol. wt. 396) isolated from Feedstock B; and, two heptamantane crystals (mol. wt. 394) isolated from Feedstock B, octamantane 1o crystal (mol. wt 446) isolated from Feedstock B. As well as a nonamantane crystal (mol. wt.
498) and a decamantane crystal (mol. wt. 456) isolated from Feedstock B. The other higher diamondoid components could also be isolated using the procedures set forth in these examples.
EXAMPLE SA: Isolation of Tetramantanes [000228] The general processes of Examples 1 and 2 were used to enrich and isolate the tetramantanes.
[000229] In this example, pyrolysis Step 5 (FIG. 12) was not employed and the product of Step 4 went directly to column chromatography (Step 6 of Example 1). The column 2o chromatography product was then treated as follows:
[000230] The eluent from the column chromatography of Step 6 was analyzed by GC/MS
to determine the approximate GC retention times of tetramantane isomers.
Individual tetramantanes were assigned a number according to their elution order in the GC/MS
analysis. This reference number was used to identify individual tetramantanes in subsequent steps. Note that enantiomeric pairs are not resolved in this analysis and so these enantiomers (racemic mixtuxes) were assigned a single number for these purposes. GC
retention times vary with changing columns and GC conditions and new reference retention time tables were prepared as needed using this procedure. Below is a table used in Example SD
procedures below.

Tetramantane Reference # 1 2 3 GCMS Retention Times in. 11.28 11.84 12.36 [000231] A two-column preparative capillary gas chromatograph was then used to isolate tetramantanes from the distillate fractions cleaned-up by column chromatography. The results are shown in FIG. 21, identified as cuts 1, 2 and 3.
[000232] The first column was used to concentrate the tetramantanes by taking cuts that were then sent to the second column (see FIG. 21). The second column, phenyl-methyl silicone a DB-17 equivalent, further separated and purified the tetramantanes and then sent them into individual vials (traps 1-6). GC trap fractions 2, 4 and 6 were collected and further processed.
[000233] The highly concentrated tetramantanes were then allowed to crystallize from solution. Under the microscope at 30X magnification, crystals were visible in preparative GC trap fractions 2, 4, and 6 (see FIG. 22). Where concentrations were not high enough for crystallization to occur, further concentration by preparative GC was necessary. FIG.'s 22A, B and C illustrate photomicrographs of tetramantane crystals isolated from Feedstock A
in trap, #2, #4 and #6 corresponding to tetramantane #1, #2, and #3 (respectively).
[000234] After obtaining crystals of suitable size, material could be sent for structural determination using X-ray diffraction. Enantiomeric tetramantanes can undergo further separations to resolve their two components as discussed previously.
2o E~~AMPLE 5B: Enrichment of Tetramantanes Using Pyrolysis.
[000235] This example shows that pyrolysis (Step 5, Example 1, FIG. 12) can be useful in the isolation of tetramantanes.
[000236] Prior to pyrolysis, nondiamondoid components are present (FIG. 23A) in a tetramantane-containing fraction (distillation hold-up fraction similar in composition to Cut 1, FIG. 17). Pyrolysis degraded the nondiamondoid components to easily removable gas and coke-like solids. As shown in FIG. 23B, the nondiamondoid peaks axe gone after pyrolysis.

[000237] Pyrolysis was conducted by heating the tetramantane-rich distillation cut under vacuum in the reactor at 450 °C for 20.4 hours.
EXAMPLE SC: Isolation of Tetramantanes Using a Single HPLC System.
Isolations of diamondoids using HPLC
[000238] In addition to the gas chromatographic and pyrolysis methods described above, HPLC was also shown to provide sufficient enrichments of the tetramantanes to allow for their crystallization. Suitable columns for use are well known to those skilled in the art. In some cases, reverse-phase HPLC with acetone as mobile phase can be used to effect this purification. A preparative HPLC run of a Feedstock A, gas condensate, distillate fraction corresponding in cut point to Cut #1 (FIG. 17) was performed and the HPLC
chromatogram recorded. Nine fractions where taken during the run. The HPLC columns used were two 25cm x lOmm LD. Vydac octadecyl silane ODS columns operated in series (Vydac columns are manufactured by The Separations Group, Inc., CA, USA). A 20 microliter sample of a solution of the tetramantane-containing fraction at a concentration of 55 mg/mL was injected into the columns. The columns were set-up using acetone at 2.00 ml/min as a mobile phase carver.
[000239] FIG. 24 (A,B) compares the gas chromatogram of the starting material (FIG.
24A) and HPLC fraction #6. HPLC Fraction #6 is significantly enriched in tetramantane FIG. 24B compared to the starting material (FIG. 24B compared to the starting material (FIG. 24A)). Tetramantane #2 in HPLC Fraction #6 is approaching a concentration sufficient to bring about its crystallization.
EXAMPLE SD: Isolation of Individual Tetramantane Isomers by HPLC Using Multiple Columns with Different Selectivities [000240] As shown in Example SC, tetramantanes can be isolated using HPLC
methods.
In this example, HPLC columns of different selectivities were used to isolate single tetramantane isomers. FIG. 25 shows a preparative separation of the tetrasnaiitanes using an octadecyl silane (ODS) HPLC column with acetone as a mobile phase. The distillation product used as starting material in Example 5B was the feedstock.
Specifically, preparative HPLC fractionation of the holdup fraction from Feedstock B atmospheric distillation taken at about 650°F were performed. The first column consisted of two Whatman M20 10/50 (x2) ODS columns operated in series using acetone at 5.00 ml/min as mobile phase (@590 psi), 0.500 ml injection containing 56 mg/ml of the holdup fraction in acetone. The resulting chromatogram is shown on FIG. 25. Tetramantane #1 elutes first, tetramantane #3 elutes second and tetramantane #2 elutes last on the HPLC system (FIG. 25). The detector used was a differential refractometer. From this run, fraction 12 (FIG. 25) was taken for further purification.
[000241] Further purification of fraction 12 was achieved using Hypercarb-S
HPLC
colurmls which have a different specificity than the ODS column above, to isolate tetramantane #2 (FIG. 26). Two Hypercarb-S columns (manufactured by Thermo Hypersil, Penn, USA), 4.6mm LD. x 250 mm, operated in series using acetone at 1.00 mL/min as is mobile phase (@180 psi), 50 microliter injection of 4 mg/ml in acetone also using a differential refractometer. Tetramantane #3 elutes first, tetramantane #1 elutes second and tetramantane #2 elutes last on this Hypercarb HPLC system (FIG. 14).
Tetramantane #2 was cut from this HPLC run (FIG. 26) and its purity illustrated in FIG.'s 28A and B. Hypercarb HPLC runs on ODS HPLC cut led to isolation of all the tetramantanes (enantiomers are 2o separatable by chiral HPLC methods).
[000242] FIG. 27A shows the GC/MS total ion chromatogram (TIC) of an HPLC
fraction containing tetramantane #1; and below it, FIG. 27B shows its mass spectrum.
FIG. 29A
shows the GC/MS total ion chromatogram (TIC) of an HPLC fraction containing isolated tetramantane #3; and below FIG. 29B shows the mass spectrum.
EXAMPLE SE: Isolation of Substituted Tetramantanes [000243] Alkyltetramantanes can be purified using methodologies described for nonalkylated tetramantanes given in Examples 5A to 5D. FIG. 30 shows an isolated monomethylated tetramantane with molecular weight of 306 yielding a mass spectrometric molecular ion of m/z 306, and shows a mass spectrometric loss of the methyl group giving the m/z 291 mass spectrometric fragment ion (indicative of a tetramantane moiety). This alkylated compound was isolated by Hypercarb HPLC and shows a retention time of 11.46 minutes in our GC/MS system (FIG. 30). It may be necessary to use additional HPLC
separations or preparative GC (as is Examples 3 and 4) to isolate some alkyltetramantanes.
EXAMPLE 6A: Isolation of Pentamantanes by Preparative Gas Chromatography [000244] Steps 1-4 of Example 1 (FIG. 12) were repeated. In Step 5, 5.2 g. of Feedstock B 650°F + bottoms distillation cut 5 (Table 3, FIG. 18) was pyrolyzed under vacuum at 450°C for 16.7 hours. This product was then treated in accord with Example 1 Step 6.
[000245] The eluent from the column chromatography (Step 6) was analyzed by GC/MS
to to determine the GC retention times of pentamantane isomers. Individual pentamantane components with molecular weight 344 were assigned a number according to their elution order on this GC/MS analysis.
[000246] The two-column preparative capillary gas chromatograph was then used to isolate pentamantanes from the product of Step 6 above. An exemplary result is shown for 15 pentamantane #1 in FIG. 31. The pentamantane #1-containing GC peak on the first column is identified as "peak cut and sent to column 2" in FIG. 31A.
[000247] The first column was used to concentrate the pentamantane by taking a cut that was then sent to the second column. The second column, phenyl-methyl silicone, a DB-17 equivalent, fiuther separated the pentamantane #1 from other materials. The material in the 20 peak of interest identified as "peak sent to trap" was sent to GC trap fraction 6 where crystals of pentamantane #1 accumulated (see FIG. 31B). GCMS analysis of trap #6 material (FIG.
32) showed it to be pentamantane #1 (in the pentamantane reference GCMS
retention time system set-up for this preparative GC procedure, the first eluting pentamantane (#1) showed a retention time of 16.233 min. FIG's. 32A and B show the high purity of pentamantane #1 25 removed from GC trap 6. This procedure could be repeated to isolate the four other pentamantanes and three enantiomeric pairs which could be separated using chiral HPLC or other resolution techniques.
[000248] The highly concentrated pentamantanes crystallize either directly in the trap or from solution. Under the microscope at 30X magnification, crystals of pentamantane #1 were visible in preparative GC trap 6 (see FIG. 33A). These crystals were perfectly clear and showed high refractive index. Crystals of pentamantane #1 had never existed before this isolation. Where concentrations are not high enough for crystallization to occur, ftirther concentration by preparative GC may be necessary. FIG. 33B is a photomicrograph of two pentamantanes that co-crystallized in a preparative GC trap.
[000249] After obtaining crystals of suitable size, non-enantiomeric pentamantane materials could be sent for structural determination using X-ray diffraction.
Enantiomeric pentamantanes can undergo further separations to resolve their two components.
1o EXAMPLE 6B: Isolation of Pentamantanes by HPLC
[000250] Steps 1-6 of Example 6A were repeated. GCIMS assay reference numbers and retention times for the 344 molecular pentamantanes were as follows:
Pentamantane Reference 1 2 3 4 5 6 #

GCMS

Retention 13.68 15.26 15.31 15.72 15.85 16.06 Times* (min.) *(HP-SMS, 0.25 micron film, 0.25 mm LD. x 30 m, helium carrier gas) [000251] Pentamantane #1-containing ODS HPLC fractions indicated in FIG. 34 were 15 ftu-ther purified using Hypercarb HPLC (FIG. 35) to isolate pentamantane #l. FIG. 14 shows how ODS HPLC and Hypercarb HPLC can be used together to isolate the remaining pentamantanes. The ODS and Hypercarb columns can also be used in reverse order for this isolation. FIG. 36 shows the GC/MS total ion chromatogram (TIC) of the isolated pentamantane #1. The lower half of FIG. 36 illustrates the mass spectrum of the 2o pentamantane #1 GC/MS peak. As indicated in FIG's. 14 and 34, the various remaining ODS HPLC fractions contain other pentamantanes. By using similar methodology as above, i.e. fractionating pentamantane containing ODS fractions using the Hypercarb (as indicated in FIG. 14) or another suitable column, and collecting at corresponding elution times, leads to the isolation of the remaining pentamantanes in high purity as shown in FIG's 37-41.
25 Specifically, FIG. 37 illustrates GC/MS total ion chromatogram (TIC) and mass spectrum of pentamantane #2 isolated using two different HPLC columns; FIG. 38 illustrates GC/MS
total ion chromatogram (TIC) and mass spectrum of pentamantane #3 isolated using two different HPLC columns; FIG. 39 illustrates GC/MS total ion chromatogram (TIC) and mass spectrum of pentamantane #4 isolated using two different HPLC columns; FIG. 40 illustrates GC/MS total ion chromatogram (TIC) and mass spectrum of pentamantane #5 isolated using two different HPLC columns; and FIG. 41 illustrates GC/MS total ion chromatogram (TIC) and mass spectrum of pentamantane #6 isolated using two different HPLC
columns. The enantiomeric pentamantanes are not resolved in GS/MS and therefore, these enantiomeric pairs are referenced witlun a single number. These enantiomers can be separated by chiral separation methods. In addition, as previously noted, there is a condensed isomer of pentamantane having a molecular weight of 330 which is more sterically strained and this appears in significantly lower concentrations. This pentamantane component has been observed in GC/MS analyses of distillation cut 5 pyrolysis product cleaned up using Step 6 of Example 1 (FIG. 12). This pentamantane component eluted at 14.4 minutes in the analysis of Example 1, Step 4 and could be isolated using procedures in this Example.
EXAMPLE 6C: Purification of Substituted Pentamantane [000252] Substituted pentamantanes are present in Feedstocks A and B.
Substituted pentamantanes can be enriched from these feedstocks and purified using methodologies described for nonalkylated pentamantanes in Examples 1-4. The monomethylated pentamantane enriched in this instance has a molecular weight of 358 (yielding a mass spectrometric molecular ion of m/z 358, and shows a mass spectrometric loss of the methyl group giving the m/z 343 mass spectrometric fragment ion indicative of a pentamantane moiety). This alkylated compound was enriched in ODS HPLC fraction #31 and could be further purified to form a crystal by an additional HPLC separation, or alternatively by a preparative GC procedure (as is Example 3).
EXAMPLE 7A: Isolation of Hexamantane Components [000253] The purpose of this example is to demonstrate procedures which can be used for the enrichment and isolation of the thirty-nine hexamantane components. The process of Example 1 was repeated with the following changes. In Step 5, 34.4 g, of Feedstock B 650°F
bottoms distillation cut #6 (Table 3, FIG. 18) was pyrolyzed under vacuum at 450°C for 17.3 hr.

[000254] The eluent from the column chromatography (Step 6) was analyzed by GC/MS
to determine the GC retention times of hexamantanes. Individual hexamantane components with molecular weight 396 were assigned a number according to their elution order on this GC/MS assay. These hexamantanes were the most abundant and selected for convenience.
Similar assays could be prepared for the other molecular weights. Hexaxnantane elution times ran between 17.88 min. (hexamantane #1) and 19.51 min. (hexamantane #7) in this GC/MS assay. Retention times vary with changing GC columns and conditions requiring remeasurement of retention times. FIG. 13A lists another GC/MS assay result for the hexamantane components, [000255] A two-column preparative capillary gas chromatograph was used to isolate hexamantanes from the distillate fractions cleaned-up by column chromatography. The cut times for the hexamantanes were set for the first preparative capillary GC
column, methyl silicone DB -1 equivalent, using the retention times and patterns from GC/MS
assay. The results are shown in FIG. 42A, identified as "peak cut and sent to column 2"
which contains two of the hexamantane fractions.
[000256] The first column was used to concentrate the hexamantanes by taking cuts that were then sent to the second column (see FIG. 42 illustrated for hexamantane #2 and #8).
The second column, phenyl-methyl silicone a DB-17 equivalent, further separated and purified the hexamantanes and then was used to isolate peaks of interest and retain them into individual traps (traps 1-6). GC trap fraction 1 was collected and further processed for the separation of hexamantane #2. GC trap fraction 3 was collected and further processed for the separation of hexamantane #8. Subsequent GC/MS analysis of trap #1 material (FIG.
43) showed it to be hexamantane #2 based upon the earlier run GC/MS assay.
Similarly, the GC analysis of trap #3 material (FIG. 44) showed it to be primarily hexamantane #8. This procedure could be repeated to isolate the other hexamantanes.
[000257] The highly concentrated hexamantanes were then allowed to crystallize either directly in the trap or from solution. Under the microscope at 30X
magnification, crystals were visible in preparative GC trap fraction 1 (see FIG. 45). These crystals were perfectly clear and showed high refractive index. Crystals of hexamantane #2 had never existed before this isolation. Where concentrations are not high enough for crystallization to occur, further concentration by preparative GC may be necessary. FIG. 46 is a photomicrograph of hexamantane #8 that crystallized in preparative GC trap 3. Crystals of hexamantane #8 had never existed before this isolation.
[000258] After obtaining crystals of suitable size, non-enantiomeric hexamantane components could be sent for structural determination using X-ray diffraction.
Enantiomeric hexamantanes must undergo further separations to resolve the two components.
EXAMPLE 7B: Isolation of Hexamantanes Using a Single HPLC System.
to [000259] The HPLC coluzr~ns used were two SOcm x 20mm LD. Whatman octadecyl silane (ODS) columns operated in series (Whatman columns are manufactured by Whatman Inc., USA). A 500 microliter sample of a solution of the cut 6 pyrolysis product saturated hydrocarbon fraction (54 mg), the product of Example 1, Step 6, was injected into the columns. The columns were setup using acetone at 5.00 ml/min as the mobile phase. Some 15 of the HPLC fractions reached the purity necessary for individual hexamantanes to crystallize as shown for Hexamantane # 8 in ODS HPLC fraction # 39 (FIG. 47), Hexamantane # 10 in ODS HPLC fraction # 48 (FIG. 48) and Hexamantane # 6 in ODS
HPLC fraction # 63 (FIG. 49). Alternatively a Hypercarb column (manufactured by Thermo Hypersil, Perm, USA) or other suitable column could be used to purify hexamantanes to 20 concentrations necessary for them to crystallize. A preparative Hypercarb HPLC run of Feedstock B distillate cut~6 pyrolysis product saturated hydrocarbon fraction was performed and the HPLC chromatogram recorded using a differential refractometer.
Fractions (e.g., FIG. 50) where taken during the run and showed that most hexamantanes display different elution times (verified by GC/MS analysis) from one another on the Hypercarb HPLC
25 system (FIG. 20).

EXAMPLE 7C: Isolation of Hexamantanes Using Multiple HPLC Columns of Differing Selectivities [000260] Hypercarb HPLC fractions were taken to obtain high purity hexamantane #13 demonstrated in FIG. 51. Other ODS HPLC fractions and Hypercarb HPLC cut points could be used to isolate the remaining hexamantanes. The ODS and Hypercarb columns can also be used in reverse order for this isolation. FIG. 52 shows the GC/MS total ion chromatogram (TIC) of the hexamantane #7 containing Hypercarb HPLC fraction.
The lower half of FIG. 52 illustrates the mass spectrum of the GC/MS peak, demonstrating the high purity of the isolated hexamantane #7.
[000261] The various remaining ODS HPLC fractions (FIG. 19) containing other hexamantanes could be separated in the same way. By using similar methodology as above, i.e. fractionating hexamantane-containing ODS fractions using the Hypercarb or other suitable column and collecting at corresponding elution times can lead to the isolation of the remaining hexamantanes in high purity. This is also true of the hexamantanes with molecular weights of 382, "irregular" hexamantanes, that are in much lower abundance in our feedstocks than hexamantanes showing molecular weight of 396. FIG.'s 53 and 54 present reconstructed ion chromatograms for m/z 382 showing hexamantanes running at 18.30 min. and 18.07 min., respectively. FIG.'s 53 and 54 also show the corresponding mass spectra for these 18.30 min. and 18.07 min. peaks, demonstrating the presence of 2o hexamantanes with a 382 molecular weight in the saturated hydrocarbon fraction from the product of pyrolytic processing of Feedstock B distillation fraction #6. The 382 molecular weight hexamantanes show internal bond strain, lower stability, and correspondingly lower concentrations than the 396 molecular weight hexamantanes, making the 382 molecular weight hexamantanes the less preferred hexamantanes.
[000262] The enantiomeric hexamantanes are not resolved in GS/MS and therefore, these enantiomeric pairs are referenced within a single number. These enantiomers can be isolated by chiral separation methods.

EXAMPLE 7D: Isolation of Substituted Hexamantanes [000263] Substituted hexamantanes including alkylhexamantanes also are present in Feedstock A and B. These natural substituted hexamantanes have uses similar to the unsubstituted hexamantanes, can act as useful intermediates in various hexamantane applications (e.g., polymer production) and can be de-alkylated to yield the corresponding underivatized hexamantane. Accordingly, methods for the isolation of individual substituted hexamantane were devised and exemplified by the isolation of alkyl substituted components.
Substituted hexamantanes, including alkylhexamantanes, can be isolated in high purity using a single HPLC separation of appropriate distillation cuts as exemplified by FIG. 55. FIG. 55 l0 shows that fraction #55 from an ODS HPLC separation of the saturated hydrocarbon fraction from Feedstock B, distillation fraction 6 pyrolysis contains a methylated hexamantane in high purity. Monomethylated hexamantanes have a molecular weight of 410 (yielding a mass spectrometric molecular ion of m/z 410, and show a mass spectrometric loss of the methyl group giving the m/z 395 fragment ion (FIG. 55B)). Isolation of substituted ' hexamantane components by HPLC may require multiple columns with different selectivities. For example, the ODS and Hypercarb HPLC columns were run in succession to isolate the methylcyclohexamantane components (methyl-substituted mol.
weight 342 hexamantane) from distillation cut 6-pyrolysis product saturated hydrocarbon fraction. From the first ODS HPLC run, fractions #23-26 were combined and taken for further purification on a second HPLC system. This combined fraction (FIG. 56) contained a mixture of hexamantane (mol. weight 342 referred to as cyclohexamantane), eluting on our GC/MS
system at 12.31 minutes as well as three methylcyclohexamantanes (#1-3) eluting at 12.56, 12.72 and 13.03 minutes, respectively. Further purification of this mixture (i.e. combined ODS HPLC fractions #23-26) was aclueved using a Hypercarb stationary phase HPLC
column. A 50 microliter sample of approximately 1 mg of this combined fraction in acetone was injected into the Hypercarb column, 10 mm LD. x 250 mm, operated using acetone at 3.00 mL/min as mobile phase (@480 psi) using a differential refractometer detector. In this Hypercarb system methylcyclohexamantane #1 elutes primarily in fractions 18-22 and methylcyclohexamantane #2 elutes primarily in fractions 23-25.
Methylcyclohexamantane #1 and #2 where isolated in sufficient purity to form crystals. A GC/MS total ion chromatogram and mass spectrum of these compounds is illustrated in FIG.'s 57 and 59 and illustrated as crystals in photomicrographs in FIG's. 59 and 60. FIG. 59 illustrates a methylcyclohexamantane crystal precipitated from Hypercarb HPLC fractions #19-21 and FIG. 60 illustrates a methylcyclohexamantane crystal precipitated from Hypercarb HPLC
fractions #23.
[000264] Enantiomeric pairs must undergo further separations to resolve the two components. After obtaining crystals of suitable size, non-enantiomeric allcylhexamantanes can be sent for structural determination by x-ray crystallography.
EXAMPLE 8A: Isolation of Heptamantane Components [000265] The eluent from the column chromatography (Step 6, FIG. 12) was analyzed by GC/MS to determine the GC retention times of heptamantanes. Individual heptamantane to components with molecular weight 394 and 448 were assigned a number according to their elution order on our GC/MS assay (see FIG. 13A for representative assay values). Molecular weight 448 heptamantanes, the most abundant heptamantane family, were selected for convenience in this Example. Similar assays could be prepared for the other molecular weight heptamantanes.
15 [000266] A two-column preparative capillary gas chromatograph was then used to isolate heptamantanes from the distillate fractions cleaned-up by column chromatography. The cut times for the heptamantanes were set for the first preparative capillary GC
column, methyl silicone DB -1 equivalent, using the retention times and patterns from GC/MS
assay (from Step 2 above, FIG. 12). An exemplary result is shown in the top of FIG. 61, identified as 20 "peak cut and sent to column 2" which contains two of the heptamantanes from Feedstock B.
[000267] The first column was used to concentrate the heptamantanes by taking cuts that were then sent to the second column (see FIG. 61 illustrated for heptamantanes #1 and #2).
The second column, phenyl-methyl silicone a DB-17 equivalent, further separated and purified the heptamantane components and then was used to isolate peaks of interest and 25 retain them in individual vials (traps 1-6). GC trap fraction 2 was collected and further processed for the separation of heptamantane #1. GC trap fraction 4 was collected and further processed for the separation of heptamantane #2. Subsequent GC/MS
analysis of trap #2 material (FIG. 62) showed it to be heptamantane #1 based upon the earlier run GC/MS
assay of step 4. Similarly, the GC analysis of trap #4 material (FIG. 63) showed it to be heptamantane #2. This procedure could be repeated to isolate the other heptamantane components.
[000268] The highly concentrated heptamantanes were then allowed to crystallize either directly in the trap or from solution. Under the microscope at 30X
magnification, crystals were visible in preparative GC trap fraction 2 (see FIG. 64). These crystals were perfectly clear and showed high refractive index. Crystals of heptamantane component #1 had never existed before this isolation. Where concentrations are not high enough for crystallization to occur; further concentration by preparative GC may be necessary. FIG. 65 is a photomicrograph of heptamantane component #2 that crystallized in preparative GC trap 4.
l0 Crystals of heptamantane component #2 had never existed before this isolation.
[000269] After obtaining crystals of suitable size, heptamantane materials could be sent for structural determination using X-ray diffraction. Enantiomeric heptamantanes can undergo further separations to resolve their two components.
EXAMPLE 8B: Purification of Single Heptamantane Isomers [000270] HPLC was also shown to provide sufficient enrichments of some heptamantanes to allow for their crystallization.
[000271] The HPLC columns used were the same as those given in the other examples (ODS and Hypercarb). A 500 microliter sample of a solution of the cut 7 pyrolysis product 2o saturated hydrocarbon fraction (product of Step 6, FIG. 12) was injected into the ODS
columns. Pyrolysis of Cut 7 used 25.8 g. heated at 450°C for 16 hrs.
Some of the ODS
HPLC fractions reached the purity necessary for individual heptamantanes to crystallize as shown for heptamantane # 1 in ODS HPLC fraction # 45 (FIG. 66). Others, such as heptamantane # 2 in ODS HPLC fraction # 41 (FIG. 67), heptamantane # 9 in ODS
HPLC
fraction # 61 (FIG. 68), and heptamantane #10 in ODS HPLC fraction # 87 (FIG.
69), may require further separation on HPLC systems with different selectivities.
Running the ODS
fractions (FIG. 13B) on a Hypercarb column resulted in the purity necessary for individual heptamantane components to crystallize as shown for heptamantane component # 1 in Hypercarb HPLC fraction # 55 (FIG. 70) and heptamantane #2 (FIG. 71). The higher 3o diamondoids in various HPLC fractions could be separated using further chromatographic techniques including preparative gas chromatography and additional HPLC runs using columns of different selectivity as outlined below. Additionally other techniques known in the crystallization art could be utilized including but not limited to fractional sublimation, progressive recrystalization or zone refining could be used to purify the heptamantanes.
[000272] By using similar methodology as above, i.e. fractionating heptamantane-containing ODS fractions using the Hypercarb or other suitable columns and collecting at corresponding elution times can lead to the isolation of the remaining heptamantanes. This is also true of the heptamantanes with molecular weights of 420 and 434, that are in much lower abundance in our feedstocks than heptamantane components showing molecular to weights of 394 and 448. A heptamantane component of molecular weight 420 shows up in ODS HPLC fraction #61 (FIG. 73A) with a very strong molecular ion in the mass spectrum (in this case m/z 420, FIG. 73B) for the m/z 420 component running at 16.71 min. The mass spectrum, with its prominent molecular ion and low number and abundance of fragments is characteristic of a diamondoid component.
EXAMPLE 8C: Isolation of Substituted Heptamantanes [000273] Substituted heptamantanes including alkylheptamantanes also are present in Feedstock A and B. Alkylheptamantanes can be purified by removal of nondiamondoid impurities from feedstocks using pyrolysis as shown above. Certain alkylheptamantanes survive pyrolysis processing, as do the heptamantane components previously identified.
Substituted heptamantanes including alkylheptamantanes can be isolated in high purity using a single HPLC separation as exemplified by FIG. 74. Monomethylated heptamantanes have a molecular weight of 408 (yielding a mass spectrometric molecular ion of m/z 408, and show a mass spectrometric loss of the methyl group giving the m/z 393 mass spectrometric fragment ion indicative of a heptamantane moiety (FIG. 74B).
EXAMPLE 9A: Isolation of Octamantane Components [000274] An octamantane-enriched fraction from Step 6 was subjected to reverse-phase HPLC. In some cases, reverse-phase HPLC with acetone as mobile phase can be used to effect this purification. A preparative ODS HPLC run of Feedstock B distillate cut 7 pyrolysis product saturated hydrocarbon fraction (used in Example 8A) was performed and the HPLC chromatogram recorded using a differential refractometer. HPLC
fractions were analyzed by GC/MS to determine octamantane HPLC elution times and monitor purity (see FIG. 13A for representative assay values). The HPLC columns used were the same ODS and Hypercarb systems used in previous examples. A 500 microliter sample of an acetone solution of the cut 7 pyrolysis product saturated hydrocarbon fraction (25 mg) was injected into the ODS columns. While using this HPLC system, some octamantanes reached purity needed for individual octamantanes to crystallize. For example, FIG. 75 illustrates a GC/MS
total ion chromatogram and mass spectra of an HPLC fraction in which octamantane #1 has l0 been purified to the point where it formed crystals (see FIG. 76). HPLC
Fraction 63 yielded octamantane #3 and #5 together (FIG. 77), which co-crystallized from the fraction (FIG. 78).
[000275] For isolation in high purity of other octamantane components (for example FIG.'S 79 and 80), multiple columns can be employed, e.g. Hypercarb.
EXAMPLE 9B: Isolation of Substituted Octamantane Components [000276] Alkyloctamantanes can be purified using methodologies described for non-alkylated octamantanes given in Examples 1 and 3. FIG. 81 (A/B) shows that ODS
HPLC
fraction 94 contains a methylated octamantane in high purity. Monomethylated octamantanes have a molecular weight of 460 (yielding a mass spectrometric molecular ion of m/z 460, and show a mass spectrometric loss of the methyl group giving the mlz 445 mass spectrometric fragment ion indicative of an octamantane moiety (FIG. 81B).
Also, where more than one alkyloctamantane is present in an ODS or Hypercarb HPLC
fraction, an additional HPLC separation of that fraction or preparative GC procedure (as in Example 3) can yield high purity alkyloctamantanes.
EXAMPLE 10A: Isolation of Nonamantane Components [000277] A preparative ODS HPLC run of Feedstock B distillate cut 7 pyrolysis product saturated hydrocarbon fraction was performed (material described in Example 8A) and the HPLC fractions were analyzed by GC/MS to determine nonamantane HPLC elution times (FIG. 82) and monitor purity. A 500 microliter sample of an acetone solution of the cut 7 pyrolysis product saturated hydrocarbon fraction (25 mg) was injected into the columns. The columns were set-up using acetone at 5.00 ml/min as a mobile phase carrier.
[000278] For isolation of nonamantane components in lugh purity, multiple HPLC
columns can be employed. To illustrate this methodology, HPLC columns of different selectivities ODS and Hypercarb (as described in previous examples) were used in succession to isolate a single nonamantane. From the ODS HPLC run, the nonamantane containing fractions 84-88 (FIG. 13B) were combined for further purification on a Hypercarb HPLC system.
[000279] We injected a 50 microliter sample of approximately 1 mg of ODS HPLC
combined fraction (84-88) in methylene chloride onto two Hypercarb columns, two 4.6 mm LD. x 200 mm, operated in series using methylene chloride at 1.30 mL/min as mobile phase.
[000280] FIG. 83 shows the GC/MS total ion chromatogram (TIC) of the concentrated nonamantane containing Hypercarb HPLC fraction. The lower half of FIG. 83 illustrates the mass spectrum of the GC/MS peak. Nonamantane was isolated by a third HPLC run using the same Hypercarb stationary phase column but with a solvent consisting of methylene chloride/acetone (70:30 volume percent operating at 1.00 ml/min). The resulting isolated nonamantane crystal and corresponding mass spectrum are shown in FIG. 84.
[000281] By using a similar methodology as above, i.e. fractionating nonamantane containing ODS HPLC fractions using columns with different selectivities, such as the 2o Hypercarb or other suitable columns, we isolated a molecular weight 498 nonamantane in high purity. This method could be repeated to isolate the nonamantanes with molecular weights of 552, and the nonamantanes of molecular weights 538, 484 and 444, which respectively are in lower abundance in our feedstocks. Note that enantiomeric nonamantanes are not resolved in GS/MS, however these enantiomers can be isolated by chiral separation methods.

EXAMPLE 10B: Isolation of Substituted Nonamantanes [000282] Substituted rionamantanes also are present in Feedstock A and B.
Alkylnonamantanes can be purified using methodologies described for non-alkylated nonamantanes. FIG. 85(AB) shows methylated nonamantane in a pyrolysis product of distillate fraction #7. One type of monomethylated nonamantane has a molecular weight of 512 (yielding a mass spectrometric molecular ion of m/z 512, and show a mass spectrometric loss of the methyl group giving the m/z 497 mass spectrometric fragment ion indicative of a nonamantane moiety (FIG. 85B). More than one alkylnonamantane is present and these could be isolated using ODS or Hypercarb columns, an additional HPLC
separation, or by 1o preparative GC to yield high purity alkylnonarnantanes.
EXAMPLE 11A: Isolation of Decamantane Components [000283] A preparative ODS HPLC run of Feedstock B distillate cut 7 pyrolysis product saturated hydrocarbon fraction was performed and HPLC fractions were analyzed by GC/MS
to determine decamantane HPLC elution times (FIG. 86) and monitor purity. The HPLC
columns used were two SOcm x 20mm LD. Whatman octadecyl silane (ODS) columns operated in series. A 500 microliter sample of an acetone solution of the cut 7 pyrolysis product saturated hydrocarbon fraction (25 mg) was injected into the columns.
The columns were set-up using acetone at 5.00 ml/min as a mobile phase carrier.
2o [000284] For isolation of decamantane components in high purity, multiple HPLC
columns can be employed. To illustrate this methodology, HPLC columns of different selectivities were used in succession to isolate a single decamantane. The first HPLC system consisted of the same ODS columns described previously. From this HPLC run, the decamantane containing fractions 74-83 were combined for further purification on a second HPLC system. Five such runs were completed and all decamantane containing fractions from the runs were combined. This combined fraction contained a molecular weight 456 decamantane and various impurities.
[000285] To purify the combined HPLC fractions 74-83 from the ODS HPLC
separation, we injected a 50 microliter sample of approximately 1 mg of ODS HPLC combined fraction in acetonelmethylene chloride (70:30 volume percent) onto two Hypercarb columns, 4.6 mm LD. x 200 mm, operated in series using acetone/methylene chloride (70:30 volume percent) at 1.00 mL/min as mobile phase (@480 psi).
[000286] FIG. 87 shows the GC/MS total ion chromatogram (TIC) of the concentrated decamantane-containing Hypercarb HPLC fraction eluting at 18.55 minutes. The lower half of FIG. 87 illustrates the mass spectrum of the GC/MS peak with a prominent peak at m/z 456. The resulting [1231241(2)3] molecular weight 456 decamantane crystal and mass spectrum are shown in FIG. 88. The 456 decamantane elutes before pentamantane #3 on the Hypercarb HPLC system due to its compact, low-surface area structure (FIG.

10). This property of 456 molecular weight decamantane makes possible its isolation in very high 1o purity.
[000287] By using a similar methodology as above, i.e. fractionating decamantane-containing ODS HPLC fractions using columns with different selectivities, such as the Hypercarb or other suitable columns, we isolated a molecular weight 456 decamantane in high purity. This method could be repeated to isolate the decamantanes with molecular weights of 496 (shown in FIG. 89 in the saturated fraction of the pyrolysis product of distillate fraction #7) as well as molecular weights 550 or 604, and the decamantanes of molecular weights 536, 576 and 590, which respectively are in lower abundance in our feedstocks. Note that enantiomeric decamantanes are not resolved in GS/MS, however these enantiomers can be isolated by chiral separation methods.
EXAMPLE 11B: Isolation of Substituted Decamantanes [000288] Substituted decamantanes also are present in Feedstock A and B.
Alkyldecamantanes can be purified using methodologies described for non-alkylated decamantanes. FIG. 90 shows that saturated fraction of the pyrolysis product of distillate fraction #7 contains methylated decamantanes. One type of monomethylated decamantane has a molecular weight of 470 (yielding a mass spectrometric molecular ion of m/z 470).
Also, where more than one allcyldecamantane is present in an ODS or Hypercarb HPLC
fraction, an additional HPLC separation of that fraction or an alternative preparative GC
procedure can yield high purity alkyldecamantanes.

EXAMPLE 12: Isolation of Undecamantane Components [000289] For isolation of undecamantane components in high purity, multiple HPLC
columns can be employed. This methodology was demonstrated using decamantane with HPLC columns of different selectivities used in succession to isolate a single decamantane (Example 11). An appropriate starting material, Feedstock B, distillation cut 7 pyrolysis product is shown to contain undecamantanes (FIG. 91).
[000290] The concentrated undecamantane from ODS HPLC fraction 100+ (FIG. 13B) is shown in FIG. 92. This fraction could be purified on a Hypercarb HPLC using a system (similar to that explained in Example 11) to isolate undecamantane. This method could be l0 repeated to isolate the undecamantanes with molecular weights of 656 and/or 602, as well as molecular weights 642,628, 588, 548 or 534 which respectively are anticipated to be in lower abundance in our feedstocks.

Claims (141)

WHAT IS CLAIMED IS:

1. An enriched selected higher diamondoid component neither including enriched unsubstituted anti-tetramantane, nor enriched cyclohexamantane.

2. The enriched selected higher diamondoid component of Claim 1, exhibiting a purity of at least 25% by weight.

3. A composition enriched in one or more selected higher diamondoid components, subject to the proviso that when there is only one selected higher diamondoid component it is neither unsubstituted anti-tetramantane nor unsubstituted cyclohexamantane.

4. The composition of Claim 3, wherein the one or more selected higher diamondoid components comprises at least 1 % by weight of the composition.

5. The composition of Claim 3, wherein the one or more selected higher diamondoid components comprise at least 10% by weight of the composition.

6. The composition of Claim 3, containing from 50 to 100% by weight of one or more selected higher diamondoid components.

7. The composition of Claim 3, containing from 70 to 100% by weight of one or more selected higher diamondoid components.

8. The composition of Claim 3, containing from 95 to 100% by weight of one or more selected higher diamondoid components.

9. The composition of Claim 3, containing from 99 to 100% by weight of one or more selected higher diamondoid components.

10. The composition of Claims 3-9, wherein the one or more selected higher diamondoid components are a single selected higher diamondoid component.

11. A composition comprising diamondoids enriched in one or more selected higher diamondoid components relative to the total amount of diamondoid, subject to the proviso that when there is only one selected higher diamondoid component, it is neither unsubstituted anti-tetramantane nor cyclohexamantane.

12. The composition of Claim 11, wherein at least about 25% weight percent of the total amount of diamondoids is the one or more selected higher diamondoids.

13. The composition of Claim 12, wherein the one or more selected higher diamondoid components are a plurality of the components in a single diamondoid family.

14. The composition of Claim 12, wherein the one or more selected higher diamondoid components are a single selected higher diamondoid component.

15. The composition of Claims 1-14, wherein the selected higher diamondoid components comprise one or more tetramantane components.

16. The composition of Claim 15, wherein the one or more tetramantane components are a single tetramantane component.

17. The composition of Claim 16, wherein the single tetramantane component is iso-tetramantane.

18. The composition of Claim 16, wherein the single tetramantane component is skew-tetramantane.

19. The composition of Claim 16, wherein the single tetramantane component is a single enantiomer of skew-tetramantane.

20. The composition of Claim 15, wherein the tetramantane components comprise substituted tetramantane components.

21. Enriched iso-tetramantane.

22. Enriched skew-tetramantane enantiomer A.

23. Enriched skew-tetramantane enantiomer B.

24. The enriched tetramantane component of Claims 21-23, exhibiting a purity of at least 25%.

25. The enriched tetramantane component of Claims 21-23, in crystalline form.

26. The composition of Claims 1-14, wherein the selected higher diamondoid components comprise one or more pentamantane components.

27. The composition of Claim 26, wherein the one or more pentamantane components are a single pentamantane component.

28. The composition of Claim 26, wherein the one or more pentamantane components are isolated optical isomers.

29. The composition of Claim 26, wherein the one or more pentamantane components are isomeric pentamantane components.

30. The composition of Claim 26, wherein the one or more pentamantane components is the nonisomeric pentamantane component represented by the formula C25H30.

31. An enriched pentamantane component.

32. The enriched pentamantane component of Claim 31, exhibiting a purity of at least 25% by weight.

33. The enriched pentamantane component of Claim 31, in crystalline form.

34. The enriched pentamantane component of Claim 31, wherein the pentamantane component is [1231] pentamantane.

35. The enriched pentamantane component of Claim 31, wherein the pentamantane component is [1213] enantiomer A pentamantane.

36. The enriched pentamantane component of Claim 31, wherein the pentamantane component is [1213] enantiomer B pentamantane.

37. The enriched pentamantane component of Claim 31, wherein the pentamantane component is [1234] enantiomer A pentamantane.

38. The enriched pentamantane component of Claim 31, wherein the pentamantane component is [1234] enantiomer B pentamantane.

39. The enriched pentamantane component of Claim 31, wherein the pentamantane component is [12(1)3] enantiomer A pentamantane.

40. The enriched pentamantane component of Claim 31, wherein the pentamantane component is [12(1)3] enantiomer B pentamantane.

41. The enriched pentamantane component of Claim 31, wherein the pentamantane component is [1212] pentamantane.

42. The enriched pentamantane component of Claim 31, wherein the pentamantane component is [1(2,3)4] pentamantane.

43. The enriched pentamantane component of Claim 31, wherein the pentamantane component is [12(3)4] pentamantane.

44. The enriched pentamantane component of Claim 31, wherein the pentamantane component is an unsubstituted pentamantane component.

45. The enriched pentamantane component of Claim 31, wherein the pentamantane component is a substituted pentamantane component.

46. The composition of Claims 1-14, wherein the selected higher diamondoid components comprise one or more hexamantane components.

47. The composition of Claim 46, wherein the one or more hexamantane components are a single hexamantane component.

48. The composition of Claim 46, wherein the one or more hexamantane components are isolated optical isomers.

49. The composition of Claim 46, wherein the one or more hexamantane components are isomeric hexamantane components.

50. The composition of Claim 46, wherein the one or more hexamantane components are one or more of the hexamantane components represented by the formula C30H36.

51. The composition of Claim 46, wherein the one or more hexamantane components are one or more of the hexamantane components represented by the formula C29H34.

52. An enriched hexamantane component represented by the formulas C30H36 or C29H34 with and without substitution.

53. The enriched hexamantane component of Claim 52, exhibiting a purity of at least 25% by weight.

54. The enriched hexamantane component of Claim 52, in crystalline form.

55. The enriched hexamantane component of Claim 52, represented by the formula C29H36.

56. The enriched hexamantane component of Claim 52, represented by the formula C30H36.

57. The enriched hexamantane component of Claim 56, selected from the group consisting of [1(2)314] enantiomer A hexamantane [1(2)314] enantiomer B hexamantane [12(1)32] enantiomer A hexamantane [12(1)32] enantiomer B hexamantane [12(1)34] enantiomer A hexamantane [12(1)34] enantiomer B hexamantane [12(1,3)4] hexamantane [12(3)14] enantiomer A hexamantane [12(3)14] enantiomer B hexamantane [121(2)3] enantiomer A hexamantane [121(2)3] enantiomer B hexamantane [12123] enantiomer A hexamantane [12123] enantiomer B hexamantane [12131] enantiomer A hexamantane [12131] enantiomer B hexamantane [12134] enantiomer A hexamantane [12134] enantiomer B hexamantane [12324] enantiomer A hexamantane [12324] enantiomer B hexamantane [12341] enantiomer A hexamantane [12341] enantiomer B hexamantane [1(2)3(1)2] hexamantane [12(3)12] hexamantane [121(3)4] hexamantane [12121] hexamantane [12321] hexamantane [1(2)3(1)4] enantiomer A hexamantane [1(2)3(1)4] enantiomer B hexamantane

58. The enriched hexamantane component of Claim 52, wherein the hexamantane component is an unsubstituted hexamantane component.

59. The enriched hexamantane component of Claim 52, wherein the hexamantane component is a substituted hexamantane component.

60. The enriched substituted cyclohexamantane component.

61. The composition of Claims 1-14, wherein the selected higher diamondoid components comprise one or more heptamantane components.

62. The composition of Claim 61, wherein the one or more heptamantane components are a single heptamantane component.

63. The composition of Claim 61, wherein the one or more heptamantane components are isolated optical isomers.

64. The composition of Claim 61, wherein the one or more heptamantane components are isomeric heptamantane components.

65. The composition of Claim 61, wherein the one or more heptamantane components are one or more isomeric heptamantane components represented by the formula C30H34.

66. The composition of Claim 61, wherein the one or more heptamantane components are one or more isomeric heptamantane components represented by the formula C32H36.

67. The composition of Claim 61, wherein the one or more heptamantane components are one or more isomeric heptamantane components represented by the formula C33H38.

68. The composition of Claims 61, wherein the one or more heptamantane components are one or more isomeric heptamantane components represented by the formula C34H40.

69. An enriched heptamantane component.

70. The enriched heptamantane component of Claim 69, exhibiting a purity of at least 25% by weight.

71. The enriched heptamantane component of Claim 69, in crystalline form.

72. The enriched heptamantane component of Claim 69, wherein the heptamantane component has a molecular weight of 394.

73. The enriched heptamantane component of Claim 69, wherein the heptamantane component is [121321] heptamantane.

74. The enriched heptamantane component of Claim 69, wherein the heptamantane component is [123124] heptamantane.

75. The enriched heptamantane component of Claim 69, wherein the heptamantane component is an unsubstituted component.

76. The enriched heptamantane component of Claim 69, wherein the heptamantane component is an substituted component.

77. The composition of Claims 1-14, wherein the selected higher diamondoid components comprise one or more octamantane components.

78. The composition of Claim 77, wherein the one or more octamantane components are a single octamantane component.

79. The composition of Claim 77, wherein the one or more octamantane components are isolated optical isomers.

80. The composition of Claim 77, wherein the ene or more octamantane components are isomeric octamantane components.

81. The composition of Claim 77, wherein the one or more octamantane components are one or more isomeric octamantane components represented by the formula C33H36.

82. The composition of Claim 77, wherein the one or more octamantane components are one or more isomeric octamantane components represented by the formula C34H38.

83. The composition of Claim 77, wherein the one or more octamantane components are one or more isomeric octamantane components represented by the formula C36H40.

84. The composition of Claim 77, wherein the one or more octamantane components are one or more isomeric octamantane components represented by the formula C37H42.

85. The composition of Claim 77, wherein the one or more octamantane components are one or more isomeric octamantane components represented by the formula C38H44.

86. An enriched octamantane component.

87. The enriched octamantane component of Claim 86, exhibiting a purity of at least 25% by weight.

88. The enriched octamantane component of Claim 86, in crystalline form.

89. The enriched octamantane component of Claim 86, wherein the octamantane component is an unsubstituted octamantane component.

90. The enriched octamantane component of Claim 86, wherein the octamantane component is a substituted octamantane component.

91. The composition of Claims 1-14, wherein the selected higher diamondoid components comprise one or more nonamantane components.

92. The composition of Claim 91, wherein the one or more nonamantane components are a single nonamantane component.

93. The composition of Claim 91, wherein the one or more nonamantane components are isolated optical isomers.

94. The composition of Claim 91, wherein the one or more nonamantane components are isomeric nonamantane components.

95. The composition of Claim 91, wherein the one or more nonamantane component is the isomeric nonamantane component represented by the formula C34H36.

96. The composition of Claim 91, wherein the one or more nonamantane components are one or more isomeric nonamantane components represented by the formula C37H40.

97. The composition of Claim 91, wherein the one or more nonamantane components are one or more isomeric nonamantane components represented by the formula C38H42.

98. The composition of Claim 91, wherein the one or more nonamantane components are one or more isomeric nonamantane components represented by the formula C40H44.

99. The composition of Claim 91, wherein the one or more nonamantane components are one or more isomeric nonamantane components represented by the formula C41H46.

100. The composition of Claim 91, wherein the one or more nonamantane components are one or more isomeric nonamantane components represented by the formula C42H48.

101. An enriched nonamantane component.

102. The enriched nonamantane component of Claim 101, exhibiting a purity of at least 25% by weight.

103. The enriched nonamantane component of Claim 101, in crystalline form.

104. The enriched nonamantane component of Claim 101, wherein the nonamantane component is an unsubstituted nonamantane component.

105. The enriched nonamantane component of Claim 101, wherein the nonamantane component is a substituted nonamantane component.

106. The composition of Claims 1-14, wherein the selected higher diamondoid components comprise one or more decamantane components.

107. The composition of Claim 106, wherein the one or more decamantane components are a single decamantane component.

108. The composition of Claim 106, wherein the one or more decamantane components are isolated optical isomers.

109. The composition of Claim 106, wherein the one or more decamantane components are isomeric decamantane components.

110. The composition of Claim 106, wherein the one or more decamantane components is the nonisomeric decamantane component represented by the formula C35H36.

111. The composition of Claim 106, wherein the one or more decamantane components are one or more of the isomeric decamantane components represented by the formula C38H40.

112. The composition of Claim 106, wherein the one or more decamantane components are one or more of the isomeric decamantane components represented by the formula C41H44.

113. The composition of Claim 106, wherein the one or more decamantane components are one or more of the isomeric decamantane components represented by the formula C42H46.

114. The composition of Claim 106, wherein the one or more decamantane components are one or more of the isomeric decamantane components represented by the formula C44H48.

115. The composition of Claims 106, wherein the one or more decamantane components are one or more of the isomeric decamantane components represented by the formula C45H50.

116. The composition of Claim 106, wherein the one or more decamantane components are one or more of the isomeric decamantane components represented by the formula C46H52.

117. An enriched decamantane component.

118. The enriched decamantane component of Claim 117, exhibiting a purity of at least 25% by weight.

119. The enriched decamantane component of Claim 117, in crystalline form.

120. The enriched decamantane component of Claim 117, wherein the decamantane component is [1231241(2)3] decamantane.

121. The enriched decamantane component of Claim 117, wherein the decamantane component is an unsubstituted decamantane component.

122. The enriched decamantane component of Claim 117, wherein the decamantane component is a substituted decamantane component.

123. The composition of Claims 1-14, wherein the selected higher diamondoid components comprise one or more undecamantane components.

124. The composition of Claim 123, wherein the one or more undecamantane components are a single undecamantane component.

125. The composition of Claim 123, wherein the one or more undecamantane components are isolated optical isomers.

126. The composition of Claim 123, wherein the one or more undecamantane components are isomeric undecamantane components.

127. The composition of Claim 123, wherein the one or more undecamantane component are one or more isomeric undecamantane components represented by the formula C39H40.

128. The composition of Claim 123, wherein the one or more undecamantane components are one or more isomeric undecamantane components represented by the formula C41H42.

129. The composition of Claim 123, wherein the one or more undecamantane components are one or more nonisomeric undecamantane components represented by the formula C42H44.

130. The composition of Claim 123, wherein the one or more undecamantane components are one or more nonisomeric undecamantane components represented by the formula C45H48.

131. The composition of Claim 123, wherein the one or more undecamantane components are one or more nonisomeric undecamantane components represented by the formula C46H50.

132. The composition of Claim 123, wherein the one or more undecamantane components are one or more nonisomeric undecamantane components represented by the formula C48H52.

133. The composition of Claim 123, wherein the one or more undecamantane components are one or more nonisomeric undecamantane components represented by the formula C49H54.

134. The composition of Claim 123, wherein the one or more undecamantane components are one or more nonisomeric undecamantane components represented by the formula C50H56.

135. An enriched undecamantane component.

136. The enriched undecamantane component of Claim 135, exhibiting a purity of at least 25% by weight.

137. The enriched undecamantane component of Claim 135, in crystalline form.

138. The enriched undecamantane component of Claim 135, wherein the undecamantane component is an unsubstituted undecamantane component.

139. The enriched undecamantane component of Claim 135, wherein the undecamantane component is a substituted undecamantane component.

140. A process for recovering a composition enriched in higher diamondoid components, which process comprises:
a. selecting a feedstock comprising recoverable amounts of higher diamondoid components;
b. removing a sufficient amount of components from the feedstock having a boiling point less than the lowest boiling higher diamondoid component of interest under conditions to provide a treated feedstock from which higher diamondoid components can be recovered; and c. recovering higher diamondoid components from said treated feedstock by separation techniques selected from the group consisting of chromatographic techniques, thermal diffusion techniques, zone refining, progressive recrystalization and size separation techniques.

141. A process for recovering an enriched higher diamondoid of Claim 1, which comprises:

a. selecting a feedstock comprising recoverable amounts of a higher diamondoid component or components selected for recovery, nondiamondoid components and components having a boiling point less than the lowest boiling point higher diamondoid component selected for recovery;

b. removing from the feedstock a sufficient amount of components having a boiling point less than the lowest boiling point higher diamondoid component selected for recovery under conditions wherein recoverable amounts of the higher diamondoid component or components selected for recovery are retained in the treated feedstock;
and c. thermally treating the feedstock recovered in b) above to pyrolyze at least a sufficient amount of nondiamondoid components therefrom to permit recovery of the selected higher diamondoid component or components from the pyrolytically treated feedstock wherein the pyrolysis is conducted under conditions to provide a treated feedstock retaining recoverable amounts of the selected higher diamondoid component or components.

d. recovering selected higher diamondoid components from said treated feedstock by separation techniques selected from the group consisting of chromatographic techniques, thermal diffusion techniques, zone refining, progressive recrystalization and size separation techniques.