Patent classifications
B01D2257/2064
PROCESS FOR PURIFYING A CO2 STREAM IN ORDER TO AVOID CORROSION BY HYDROCHLORIC ACID
A process for purifying a by-product stream comprising primarily CO2 that emanates from a an ethylene glycol plant, where the by-product stream may contain organic chlorides and water. The process employs an adsorbent to remove one or more organic chlorides from the by-product stream to produce pure or substantially pure CO2. To improve the efficiency of the organic chloride adsorbent, prior to the organic chloride adsorption process, a moisture adsorbent may be employed to remove at least some of the water from the by-product stream.
Organic-halogen-compound-absorbing agent, method for removing organic halogen compound from hydrocarbon gas in which said agent is used, device for absorbing halogen compound in which said method is used, and method for producing hydrocarbon gas
A process for treating a petroleum fraction and for efficiently absorbing an organic halogen compound from a fluid mixture of the organic halogen compound and an inorganic halogen compound derived from crude oil. Also disclosed is an improvement in absorption performance of a halogen-compound-absorbing material, thereby reducing the frequency with which the absorbing material is exchanged. The absorbing agent includes attapulgite (palygorskite) having high absorption performance with respect to organic halogen compounds. Also disclosed is an absorption column in which the aforementioned absorbing agent and a halogen-compound-absorbing agent, that includes zinc oxide, are disposed in series, thereby making it possible to raise the treatment performance with respect to a fluid that contains, in high concentrations, the organic halogen compound in addition to the inorganic halogen compound.
Fungi-bacteria composite microecologics and methods for preparing and using the same
A method for preparing a fungi-bacteria composite microecologics, including: cultivating and conducting high-density fermentations of Zoogloea sp. HJ1 which has been deposited in China Center for Type Culture Collection (CCTCC) with an accession number: CCTCC NO. M2012235, Pandoraea sp. FLX-1 which has been deposited in CCTCC with an accession number: CCTCC NO. M2011242, and Ophiostoma sp. LLC which has been deposited in CCTCC with an accession number CCTCC NO. M2014531 to obtain mixed strains; cultivating, fermenting, and vacuum drying the mixed strains to yield a resulting product which is ground into a powder; cultivating and conducting high-density fermentation of Aspergillus sp. HD-2 which has been deposited in CCTCC with an accession number: CCTCC NO. M2014175 and Trichoderma sp. LW-1 which has been deposited in CCTCC with an accession number: CCTCC NO. M2014176 to yield spores; and mixing the powder and the spores.
CARBON SORBENTS FOR THE REMOVAL OF NITROGEN OXIDES AND METHODS FOR MAKING THE SAME
Adsorbents including a sorbent, at least one metal additive and greater than about 5 wt. % triethylenediamine are described herein. Methods for making such adsorbents and filters comprising the adsorbents are also described.
Method and system for pressure swing adsorption
Disclosed is a method for recovering a volatile organic compound (VOC) using pressure swing adsorption carried out with two beds that includes feeding the VOC to the first bed for adsorption and, while the VOC is being adsorbed by the adsorbent material in the first bed, simultaneously extracting the VOC adsorbed by the adsorbent material in the second bed through executing a desorption step by reducing the pressure of the second bed to cause desorption of the VOC in the adsorbent material of the second bed, executing a reflux step by transferring gas to the second bed and removing the transferred gas from the second bed, and executing a repressurization step by increasing pressure of the second bed to a pressure suitable for adsorption of the VOC by the adsorbent material in the second bed.
MATERIALS AND METHODS FOR MITIGATING HALIDE SPECIES IN PROCESS STREAMS
Materials and methods for mitigating the effects of halide species contained in process streams are provided. A halide-containing process stream can be contacted with mitigation materials comprising active metal oxides and a non-acidic high surface area carrier combined with a solid, porous substrate. The halide species in the process stream can be reacted with the mitigation material to produce neutralized halide salts and a process stream that is essentially halide-free. The neutralized salts can be attracted and retained on the solid, porous substrate.
BASE METAL CATALYST FOR TREATMENT OF OZONE AND VOLATILE ORGANIC COMPOUNDS PRESENT IN AIR SUPPLY
Disclosed herein are base metal catalyst devices for removing ozone, volatile organic compounds, and other pollutants from an air flow stream. A catalyst device includes a housing, a solid substrate disposed within the housing, and a catalyst layer disposed on the substrate. The catalyst layer includes a first base metal catalyst at a first mass percent, a second base metal catalyst at a second mass percent, and a support material impregnated with at least one of the first base metal catalyst or the second base metal catalyst.
REHEATING COLLECTION DEVICE FOR GAS PHASE PROCESS
A reheating collection device for a gas phase process is provided with a container elongated in an axial direction along an axis to define a chamber, an inflow path and an exhaust path respectively in communication with the chamber and apart in the axial direction from each other, and a heater heating the chamber between the inflow path and the exhaust path.
Carbon sorbents for the removal of nitrogen oxides and methods for making the same
Adsorbents including a sorbent, at least one metal additive and greater than about 5 wt. % triethylenediamine are described herein. Methods for making such adsorbents and filters comprising the adsorbents are also described.
PROCESS FOR THE REMOVAL OF HEAVY METALS FROM FLUIDS
A process for removal of heavy metals and/or dioxins from a fluid including heavy metals, where the fluid is brought in contact with a mixture including between 30% vol. and 60% vol. of an activated carbon catalyst impregnated with sulfur, between 30% vol. and 60% vol. of an activated carbon catalyst impregnated with iron and between 5% vol. and 40% vol. of a filler material, the total of these three ingredients being 100% vol, where the fluid is left in contact with the mixture, the heavy metals and/or dioxins are absorbed onto the mixture to obtain a fluid with a depleted level of heavy metals, which fluid is then evacuated from the mixture.