US 4,171,257 Petroleum Distillate Upgrading Process 2. US 4,251,348 Petroleum Distillate Upgrading Process 3. US 4,282,085 Petroleum Distillate Upgrading Process 4. US 4,347,121 Production of Lubricating Oils 5. US 4,390,413 Hydrocarbon Upgrading Process 6. US 4,436,614 Process for Dewaxing and Desulfurizing Oils 7. US 4,502,945 Process for Preparing Olefins at High Pressure 8. US 5,955,641 Method of manufacture of dimethylnaphthalenes 9. US 6,225,359 Process for conversion of natural gas and light hydrocarbons to salable products. 10. US 6,359,018 Process for Upflow Hydroprocessing of Fischer Tropsch Wax 11. US 6,369,286 Conversion of Syngas from Fischer Tropsch Products via Olefin Metathesis 12. US 6,392,108 Inhibiting oxidation of a Fischer Tropsch product using temporary antioxidants 13. US 6,392,109 Synthesis of alkylbenzenes and synlubes from Fischer Tropsch products 14. US 6,398,946 Process for making lube base stock from lower molecular weight feedstocks 15. US 6,441,263 Ethylene manufacture by use of molecular redistribution on Feedstock C3-5 components 16. US 6,455,595 Methods for optimizing Fischer Tropsch synthesis 17. US 6,518,321 Method for transporting Fischer-Tropsch products 18. US 6,541,524 Method for transporting Fischer Tropsch products 19. US 6,562,230 Synthesis of narrow lube cuts from Fischer Tropsch products 20. US 6,566,569 Conversion of refinery C5 paraffins into C4 and C6 paraffins 21. US 6,569,909 Inhibition of biological degradation in Fischer Tropsch products 22. US 6,620,091 Underwater scrubbing of CO2 from CO2-containing hydrocarbon resources 23. US 6,626,122 Deactivatable biocides in ballast water 24. US 6,627,779 Lube base oils with improved yield 25. US 6,635,171 Process for upgrading of Fischer Tropsch products 26. US 6,667,347 Scrubbing CO2 from methane-containing gases using an aqueous stream 27. US 6,682,711 Protection of Fischer Tropsch catalysts from traces of sulfur 28. US 6,686,511 Process for making a lube base stock from a lower molecular weight feedstock using at least two oligomerization zones 29. US 6,693,138 Reduction of carbon dioxide emissions from Fischer Tropsch GTL facility by aromatics production 30. US 6,703,429 Process for converting synthesis gas into hydrocarbonaceous products 31. US 6,706,936 Process for making a lube base stock from a lower molecular weight feedstock 32. US 6,713,657 Condensation of olefins in Fischer Tropsch tail gas 33. US 6,720,359 Scrubbing CO2 from a CO2-containing gas with an aqueous stream 34. US 6,723,756 Aqueous separation of syngas components 35. US 6,743,962 Preparation of high octane alkylate from Fischer Tropsch olefins 36. US 6,759,438 Use of oxygen analysis by GC-AED for control of Fischer Tropsch process and product blending 37. US 6,768,035 Manufacture of high octane alkylate 38. US 6,768,037 Process to upgrade Fischer Tropsch products and form light olefins 39. US 6,773,578 Process for preparing lubes with high viscosity index values 40. US 6,774,148 Process for conversion of LPG and CH4 to syngas and higher valued products 41. US 6,776,897 Thermally stable blends of highly paraffinic distillate fuel component and conventional distillate fuel component 42. US 6,784,329 Olefin production from low sulfur hydrocarbon fractions 43. US 6,800,101 Deactivatable biocides for hydrocarbonaceous products 44. US 6,806,087 Use of microchannel reactors in combinatorial chemistry 45. US 6,806,237 Lube base oils with improved stability 46. US 6,822,006 Methods of controlling the temperature of an exothermic reaction 47. US 6,824,574 Process for improving production of Fischer Tropsch distillate fuels 48. US 6,833,065 Lube base oils with improved yield 49. US 6,833,484 Inhibiting oxidation of a Fischer Tropsch product using petroleum-derived products 50. US 6,841,711 Process for making a lube base stock from a lower molecular weight feedstock in a catalytic distillation unit 51. US 6,846,402 Thermally stable jet prepared from highly paraffinic distillate fuel component and conventional distillate fuel component 52. US 6,846,404 Reducing CO2 levels in CO2-rich natural gases converted into liquid fuels 53. US 6,849,664 Process for disposing biocide-containing cooling water 54. US 6,863,802 Upgrading Fischer Tropsch and petroleum-derived naphthas and distillates 55. US 6,864,398 Conversion of syngas to distillate fuels 56. US 6,872,752 High purity olefinic naphthas for the production of ethylene and propylene 57. US 6,878,854 Temporary antioxidants for Fischer Tropsch products 58. US 6,881,760 Methods for monitoring solids content in Fischer Tropsch products 59. US 6,890,423 Distillate fuel blends from Fischer Tropsch products with improved seal swell properties 60. US 6,890,962 Gas-to-liquid CO2 reduction by use of H2 as a fuel 61. US 6,896,707 Methods of adjusting the Wobbe Index of a fuel and compositions thereof 62. US 6,900,365 Process for converting heavy hydrocarbon feeds to high octane gasoline, BTX and other valuable aromatics 63. US 6,900,366 Process for upgrading of Fischer Tropsch products 64. US 6,992,114 Control of CO2 emissions from a Fischer Tropsch facility by use of multiple reactors 65. US 6,992,113 Control of CO2 emissions from a Fischer Tropsch facility by use of dual functional syngas conversion 66. US 6,979,755 Olefin production from low sulfur hydrocarbon fractions 67. US 6,933,323 Production of stable olefinic Fischer Tropsch fuels with minimum hydrogen consumption 68. US 6,924,404 Inhibition of biological degradation of Fischer Tropsch products 69. US 7,018,525 Processes for producing lubricant base oils with optimized 70. US 7,033,484 Thermally stable blends of highly paraffinic distillate fuel component with conventional distillate fuel component 71. US 7,033,552 Upgrading Fischer-Tropsch and petroleum-derived naphthas and distillates 72. US 7,087,804 Use of waste nitrogen from air separation units for blanketing cargo and ballast tanks 73. US 7,150,821 High purity olefinic naphthas for the production of ethylene and propylene 74. US 7,179,311 Stable olefinic, low sulfur diesel fuels 75. US 7,179,364 Production of stable olefinic Fischer Tropsch fuels with minimum hydrogen consumption 76. US 7,320,748 Thermally stable jet prepared from highly paraffinic distillate fuel component and conventional distillate fuel component 77. US 7,354,462 Systems and methods of improving diesel fuel performance in cold climates 78. US 7,374,657 Production of low sulfur, moderately aromatic distillate fuels by hydrocracking of combined Fischer Tropsch and petroleum streams 79. US 7,402,187 Recovery of alcohols from Fischer Tropsch naphtha and distillate fuels containing the same 80. US 7,404,888 Reducing metal corrosion of hydrocarbons using acidic Fischer Tropsch products 81. US 7,416,656 Process for removing aluminum contaminants from Fischer Tropsch feed streams using dicarboxylic acid 82. US 7,431,821 High purity olefinic naphthas for the production of ethylene and propylene 83. US 7,479,168 Stable low-sulfur diesel blend of an olefinic blend component, a low-sulfur blend component, and a sulfur-free antioxidant 84. US 7,479,216 Fischer-Tropsch wax composition and method of transport 85. US 7,488,411 Fischer-Tropsch wax composition and method of transport 86. US 7,501,019 Granular solid wax particles 87. US 7,608,181 Distillate fuel blends from Fischer Tropsch products with improved seal swell properties 88. US 7,744,742 Integration of molecular redistribution and hydroisomerization processes for the production of paraffinic base oil 89. US 7,754,065 Wax transport process 90. US 7,754,066 Method of making base oil from transported wax 91. US 7,785,378 Fischer-Tropsch derived turbine fuel and process for making same 92. US 7,838,696 Hydroconversion process employing multi-metallic catalysts and method for making thereof 93. US 7,862,893 Paraffinic wax particle coated with a powder coating 94. US 7,884,138 Process for making Fischer-Tropsch olefinic naphtha and hydrogenated distillates 95. US 7,909,894 Systems and methods of improving diesel fuel performance in cold climates 96. US 7,951,287 Production of low sulfur, moderately aromatic distillate fuels by hydrocracking of combined Fischer-Tropsch and petroleum streams 97. US 7,951,759 Fischer-Tropsch wax composition and method of transport 98. US 8,076,121 Integrated process for conversion of hydrocarbonaceous assets and photobiofuels production 99. US 8,076,122 Process for integrating conversion of hydrocarbonaceous assets and photobiofuels production using an absorption tower 100. US 8,324,413 Low melting point triglycerides for use in fuels 101. US 8,361,172 Low melting point triglycerides for use in fuels 102. US 8,523,959 Paraffinic biologically-derived distillate fuels with bio-oxygenates for improved lubricity and methods of making same 103. US 8,658,847 Processes and compositions for the incorporation of biologically-derived ethanol into gasoline 104. US 8,685,686 Biofuels processes integrating photobioreactors with anaerobic digestion 105. US 8,721,873 Process, method, and system for removing heavy metals from fluids 106. US 8,721,874 Process, method, and system for removing heavy metals from fluids 107. US 8,728,303 Process, method, and system for removing heavy metals from fluids 108. US 8,753,500 Process and system for blending synthetic and natural crude oils derived from offshore produced fluids 109. US 8,790,427 Process, method, and system for removing mercury from fluids 110. US 8,840,691 Process, method, and system for removing mercury from fluids 111. US 8,906,228 Process, method, and system for removing heavy metals from fluids 112. US 8,992,769 Process, method, and system for removing heavy metals from fluids 113. US 9,023,123 Process, method, and system for removing heavy metals from fluids 114. US 9,023,196 Process, method, and system for removing heavy metals from fluids 115. US 9,028,680 Method and system for processing viscous liquid crude hydrocarbons 116. US 9,169,445 Process, method, and system for removing heavy metals from oily solids 117. US 9,181,491 Process and system for blending synthetic and natural crude oils and blends made thereby 118. US 9,181,491 Process, method, and system for removing mercury from fluids 119. US 9,199,898 Process, method, and system for removing heavy metals from fluids 120. US 9,234,141 Process, method, and system for removing heavy metals from oily solids 121. US 9,404,049 System for blending synthetic and natural crude oils derived from offshore produced fluids 122. US 9,446,998 Paraffinic jet and diesel fuels and base oils from vegetable oils via a combination of hydrotreating, paraffin disproportionation and hydroisomerization 123. US 9,447,674 In-situ method and system for removing heavy metals from produced fluids 124. US 9,447,675 In-situ method and system for removing heavy metals from produced fluid 125. US 9,523,043 Process, method, and system for removing heavy metals from fluids 126. US 9,598,648 Process, method, and system for removing heavy metals from fluids 127. US 9,902,909 Process, method, and system for removing mercury from pipelines 128. US 9,926,775 Process for mercury removal 129. US 9,975,082 Process, method, and system for removing mercury from fluids 130. US10,093,556 Processes for removing metal particles from water 131. US10,179,879 Method for removing mercury from crude oil 132. US10,179,880 Process, method, and system for removing heavy metals from fluids 133. US11,817,610 Carbon-neutral Process for Generating Electricity
