| Class / Patent application number | Description | Number of patent applications / Date published |
|---|
| 568895000 | Preparing by hydration of olefin | 21 |
| 20090253945 | METHOD FOR PRODUCING TERTIARY BUTYL ALCOHOL - Disclosed is a method for producing tertiary butyl alcohol through hydration reaction of isobutylene and water in the presence of a cation exchange resin by using a reactor having at least two reactor vessels provided in series. The method is characterized in that a fluid in a reactor vessel at the most downstream side forms a two-liquid phase and the reaction temperature of the reactor vessel is kept at 70° C. or lower, and a fluid in at least one reactor vessel other than the one at the most downstream side forms a homogeneous phase. | 10-08-2009 |
| 20100280288 | METHOD FOR RECOVERING A NATURAL GAS CONTAMINATED WITH HIGH LEVELS OF CO2 - The present invention provides a method for recovering a natural gas contaminated with high levels of carbon dioxide. A gas containing methane and carbon dioxide is extracted from a reservoir containing natural gas, where carbon dioxide comprises greater than 40 vol. % of the extracted gas. The extracted gas is scrubbed with a wash effective to produce a washed extracted gas containing less carbon dioxide than the extracted gas and at least 20 vol. % carbon dioxide. The washed extracted gas is oxidized with an oxygen containing gas in the presence of a partial oxidation catalyst to produce an oxidation product gas containing hydrogen, carbon monoxide, and carbon dioxide. The oxidation product gas is then utilized to produce a liquid methanol product. | 11-04-2010 |
| 20120172635 | Olefin Hydration Process - The invention is directed to improvements in the indirect hydration process for the production of alcohols that enable high alcohol yield by increasing ether recycle in an olefin hydration process, such as the hydration process to produce isopropyl alcohol (IPA) from propylene or the hydration process to produce sec-butyl alcohol (SBA) from butylene. | 07-05-2012 |
| 568896000 | Supported catalyst utilized | 3 |
| 20120245397 | Hydrated Niobium Oxide Nanoparticle Containing Catalysts for Olefin Hydration - An olefin hydration catalyst and method for producing same is provided. The olefin hydration catalyst can be prepared by contacting a niobium containing compound with a strong Bronsted acid, such as sulfuric or phosphoric acid, to produce niobium oxo sulfate or niobium oxo phosphate nanoparticles. The nanoparticles can be separated, dried and utilized in a reactor for the hydration of olefins to their corresponding alcohols. | 09-27-2012 |
| 20120016164 | Process for the Production of Lower Alcohols by Olefin Hydration - An improved process for the hydration of C | 01-19-2012 |
| 20120130134 | PROCESS FOR THE PREPARATION OF POLYETHEROLS FROM ALKYLENE OXIDES - A process for the preparation of polyetherols, comprising the following steps:
| 05-24-2012 |
| 568897000 | Aluminum containing catalyst utilized | 6 |
| 20130041186 | Olefin Hydration Process with an Integrated Membrane Reactor - An olefin hydration process and reactor are provided, wherein an integrated membrane selectively removes alcohol product from the reactor, thereby allowing for increased yields. | 02-14-2013 |
| 20100099926 | METHODS AND APPARATUS FOR SYNTHESIS OF ALCOHOLS FROM SYNGAS - This invention provides a method for producing ethanol and 2-propanol from syngas, the method comprising: (a) converting syngas into methanol using a methanol-synthesis catalyst; (b) converting methanol into ethylene and propylene using a methanol-to-olefins catalyst; and (c) hydrating ethylene into ethanol and propylene into 2-propanol. As taught herein, the combined yield of the ethanol and the 2-propanol from biomass can be at least 100 gallons per dry ton biomass. In certain embodiments, the yield of ethanol is at least 100 gallons per dry ton biomass. In some embodiments, the yield of 2-propanol is at least 50 gallons per dry ton biomass. | 04-22-2010 |
| 20100099925 | METHODS AND APPARATUS FOR SYNTHESIS OF ALCOHOLS FROM SYNGAS - This invention provides a method for producing ethanol and 2-propanol from syngas, the method comprising: (a) converting syngas into methanol using a methanol-synthesis catalyst; (b) converting methanol into ethylene and propylene using a methanol-to-olefins catalyst; and (c) hydrating ethylene into ethanol and propylene into 2-propanol. As taught herein, the combined yield of the ethanol and the 2-propanol from biomass can be at least 100 gallons per dry ton biomass. In certain embodiments, the yield of ethanol is at least 100 gallons per dry ton biomass. In some embodiments, the yield of 2-propanol is at least 50 gallons per dry ton biomass. | 04-22-2010 |
| 20130066118 | METHOD OF MAKING ALCOHOLS - Methods and systems for the synthesis of alcohol are described herein. The methods and systems include a method of hydrating an olefin that may include emulsifying an olefin gas in a water stream in a high shear device under high shear conditions to produce a dispersion; and contacting the dispersion with a catalyst to hydrate the olefin gas and form an alcohol. | 03-14-2013 |
| 20130102813 | METHODS AND APPARATUS FOR SYNTHESIS OF ALCOHOLS FROM SYNGAS - This invention provides a method for producing ethanol and 2-propanol from syngas, the method comprising: (a) converting syngas into methanol using a methanol-synthesis catalyst; (b) converting methanol into ethylene and propylene using a methanol-to-olefins catalyst; and (c) hydrating ethylene into ethanol and propylene into 2-propanol. As taught herein, the combined yield of the ethanol and the 2-propanol from biomass can be at least 100 gallons per dry ton biomass. In certain embodiments, the yield of ethanol is at least 100 gallons per dry ton biomass. In some embodiments, the yield of 2-propanol is at least 50 gallons per dry ton biomass. | 04-25-2013 |
| 20100099927 | METHODS AND APPARATUS FOR SYNTHESIS OF ALCOHOLS FROM SYNGAS - This invention provides a method for producing ethanol and 2-propanol from syngas, the method comprising: (a) converting syngas into methanol using a methanol-synthesis catalyst; (b) converting methanol into ethylene and propylene using a methanol-to-olefins catalyst; and (c) hydrating ethylene into ethanol and propylene into 2-propanol. As taught herein, the combined yield of the ethanol and the 2-propanol from biomass can be at least 100 gallons per dry ton biomass. In certain embodiments, the yield of ethanol is at least 100 gallons per dry ton biomass. In some embodiments, the yield of 2-propanol is at least 50 gallons per dry ton biomass. | 04-22-2010 |
| 568898000 | Phosphorus containing catalyst utilized | 4 |
| 20090124835 | PROCESSES FOR PRODUCTION OF ISOBUTENE AND TERTIARY BUTANOL - An object of the present invention is to provide, for the production of isobutene, a high-yielding, highly-selective, and long-term stable production process of isobutene from TBA. With respect to the production of TBA, an object of the present invention is to provide a TBA production process in which, through long-term stable maintenance of a high reaction activity, long-term continuous operation is enabled and the productivity is improved. The present invention discloses a process for producing isobutene that employs a dehydration temperature of from 200 to 450° C. in use of an alumina catalyst that contains a Na content of 0.6% by weight or less in terms of NaO | 05-14-2009 |
| 20130123551 | OLEFIN OLIGOMER COMPOSITION - Processes for the production of an alcohol, esters and aliphatic hydrocarbons are provided. In one embodiment, a process for the production of an alcohol comprises: oligomerizing an olefin or a mixture of olefins having the structural formula C | 05-16-2013 |
| 20090005613 | METHOD OF MAKING ALCOHOLS - Methods and systems for the synthesis of alcohol are described herein. The methods and systems incorporate the novel use of a high shear device to promote dispersion and solubility of olefins in water. The high shear device may allow for lower reaction temperatures and pressures and may also reduce reaction time. In an embodiment, a method of making an alcohol comprises introducing an olefin into a water stream to form a gas-liquid stream. The method further comprises flowing the gas-liquid stream through a high shear device so as to form a dispersion with gas bubbles having a mean diameter less than about 1 micron. In addition, the method comprises contacting the gas-liquid stream with a catalyst in a reactor to hydrate the olefin gas and form an alcohol. | 01-01-2009 |
| 20120232313 | METHOD OF MAKING ALCOHOLS - Methods and systems for the synthesis of alcohol are described herein. The methods and systems incorporate the novel use of a high shear device to promote dispersion and solubility of olefins in water. The high shear device may allow for lower reaction temperatures and pressures and may also reduce reaction time. In an embodiment, a method of making an alcohol comprises introducing an olefin into a water stream to form a gas-liquid stream. The method further comprises flowing the gas-liquid stream through a high shear device so as to form a dispersion with gas bubbles having a mean diameter less than about 1 micron. In addition, the method comprises contacting the gas-liquid stream with a catalyst in a reactor to hydrate the olefin gas and form an alcohol. | 09-13-2012 |
| 568899000 | Sulfur containing catalyst utilized | 2 |
| 20090137850 | Method for Hydrating Olefins - A novel olefin hydration method is provided for efficiently producing alcohols by hydration of olefins containing 2 to 5 carbon atoms in the presence of a catalyst. Thus, alcohols are produced by hydrating olefins containing 2 to 5 carbon atoms at reaction temperature of 100 to 250° C. in the presence of a solid acid catalyst consisting of carbonaceous materials containing sulfonic acid groups obtained from an organic matter by carbonization and sulfonation. In carrying out this method, the organic matter is preferably an aromatic hydrocarbon or a saccharide, the olefin is preferably propylene or a butenes, and the hydration reaction temperature is not lower than 120° C., more preferably not lower than 150° C. | 05-28-2009 |
| 20110251441 | METHOD OF MAKING ALCOHOLS - Methods and systems for the synthesis of alcohol are described herein. The methods and systems incorporate the novel use of a high shear device to promote dispersion and solubility of olefins in water. The high shear device may allow for lower reaction temperatures and pressures and may also reduce reaction time. In an embodiment, a method of making an alcohol comprises introducing an olefin into a water stream to form a gas-liquid stream. The method further comprises flowing the gas-liquid stream through a high shear device so as to form a dispersion with gas bubbles having a mean diameter less than about 1 micron. In addition, the method comprises contacting the gas-liquid stream with a catalyst in a reactor to hydrate the olefin gas and form an alcohol. | 10-13-2011 |
| 568900000 | Heavy metal containing catalyst | 3 |
| 20100197978 | IPA From Propylene Using Mixed Metal Oxides - The invention relates to the production of isopropyl alcohol (IPA) by direct hydration of propylene over mixed transition metal oxides co-precipitated with ZrO | 08-05-2010 |
| 568901000 | Chromium, molybdenum, or tungsten | 2 |
| 20090069609 | COBALT-MOLYBDENUM SULFIDE CATALYST MATERIALS AND METHODS FOR ETHANOL PRODUCTION FROM SYNGAS - The present invention provides methods and compositions for the chemical conversion of syngas to alcohols. The invention includes catalyst compositions, methods of making the catalyst compositions, and methods of using the catalyst compositions. Certain embodiments teach compositions for catalyzing the conversion of syngas into products comprising at least one C | 03-12-2009 |
| 20120226079 | REDUCTIVE HYDROFORMYLATION OF AN ALKYLENE TO AN ALKANOL - Convert an alkylene to a product stream that comprises an alkanol by subjecting a gaseous combination of a) an alkylene selected from ethylene, propylene or a combination thereof, b) carbon monoxide, c) hydrogen and, optionally, d) at least one hydrocarbon or gas diluent other than ethylene or propylene to reductive hydroformylation conditions in combination with a solid phase, sulfided, heterogeneous catalyst. | 09-06-2012 |
