| Invention Title |
Patent Number |
| Oxidizer and oxidation process for a desulphurization process |
7,344,682 |
| Oxidizer and oxidation process for a desulphurization process |
7,279,148 |
| Oxidizer and oxidation process for a desulphurization process |
7,226,883 |
| Composition and control method for treating hydrocarbon |
7,029,573 |
| Continuous liquid hydrocarbon treatment method |
7,014,751 |
| Naphtha desulfurization method |
6,960,291 |
| Liquid hydrocarbon treatment method |
6,860,999 |
| Indirect heating furnace |
6,749,425 |
| A Method for Continuously Producing Thiosulfate Ions. |
6,083,472 |
| Process for treating an effluent alkaline stream having sulfur-containing and phenolic compounds |
5,997,731 |
| Treatment of sour hydrocarbon distillate with continuous recausticization |
5,961,819 |
| Indirect-fired, all ceramic pyrochemical reactor |
5,846,072 |
| Recovery of para-ethylphenol |
5,744,654 |
| Removal of acidic organic contaminants from refinery waste water |
5,705,074 |
| Sulfur Separation System with Interface Control |
5,651,896 |
| Process and apparatus for oxidizing industrial spent caustic and effecting gas-liquid mass transfer and separation |
5,395,517 |
| Process and apparatus for oxidizing industrial spent caustic and effecting gas-liquid mass transfer and separation |
5,354,482 |
| Removal of hydrogen sulfide from sour water |
5,286,389 |
| Removal of guaiacol from cresylic acid by heating with a strong base |
5,254,750 |
| Method and Apparatus for Removal of H2S from a process gas, including thiosulfate and/or cyanide salt decomposition |
5,215,728 |
| Removal of guaiacol from cresylic acid feedstreams by heating with a strong acid |
5,177,269 |
| Removal of guaiacol from cresylic acid feedstreams |
5,171,895 |
| Process and Apparatus for Removal of H2S from a process gas including polyvalent metal removal and decomposition of salts and complexes |
5,167,940 |
| Continuous Autocirculation, Multiple Zone Mass Transfer Apparatus and Method |
5,160,714 |
| Pyrolysis of naturally occurring cresylic acid mixtures |
5,146,010 |
| Continuous Process for Mass Transfer of a Liquid Reagent with Two Different Gases |
5,139,753 |
| Process and Apparatus for Removal of H2S with Separate Absorber and Oxidizer and a Reaction Chamber Therebetween |
5,126,118 |
| Method and Apparatus for Removing H2S from a Process Gas and Recovering Sulfur |
5,122,351 |
| Neutral oil recovery process for the production of naphthenic acids |
5,011,579 |
| Method of impregnating a support material |
4,956,325 |
| Packing Support Grid |
4,865,819 |
| Removal of hydrogen sulfide from sour water |
4,784,775 |
| 1,333,103 |
| Treatment of sour hydrocarbon distillate |
4,746,494 |
| Method and apparatus for melting and recovering sulfur in aqueous slurries |
4,730,369 |
| 1,260,230 |
| 249,671 |
| Treatment of sour hydrocarbon distillate |
4,675,100 |
| Process for regenerating an alkaline stream containing mercaptan compounds |
4,666,689 |
| Hydrogen Sulfide Removal |
4,622,212 |
| 1,227,783 |
| Method for preparing elemental sulfur as a diffusion-resistant gas and methods for its use in making lime, sulfur dioxide and sulfuric acid from waste gypsum |
4,520,002 |
| Autocirculation Apparatus |
4,482,524 |
| Method of stabilizing chelated polyvalent metal solutions |
4,455,287 |
| Composition and method for removing H2S from gases (Use of Surfactants) |
4,374,104 |
| Autocirculation Process and Apparatus |
4,238,462 |
| 2,084,043 |
| 1,159,434 |
| Liquid sealing apparatus for sealing vapors in a tank |
1,105,680 |
| 2,013,099 |
| 4,193,967 |
| Catalytic removal of H2S from gases (Basic LO-CAT® Process) |
4,189,462 |
| Chelate oxidation of H2S in sour water |
4,076,621 |
| 1,538,925 |
| 1,285,741 |
| 1,071,613 |
| DE2606277 |
| Process for the removal of H2S and mercaptans from liquid and gaseous streams |
4,036,942 |
| Process for the removal of H2S from gases (For Claus process tail gas) |
4,014,983 |
| Method of controlling the removal of H2S from gases |
4,011,304 |
| Process for the removal of H2S from gaseous streams by catalytic oxidation of H2S to sulfur |
4,009,251 |
| Mass transfer apparatus |
3,992,156 |
| Liquid-liquid mass transfer apparatus |
3,977,829 |
| Composition for catalytic removal of H2S from gases (Basic LO-CAT® CATALYST Formula) |
1,285,741 |
