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Results 1-10 of 46,544 for Criteria: Office(s):all Language:EN Stemming: true maximize
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TitleCtrPubDate
1. WO/2015/025193 TIDAL ENERGY SEAWATER DESALINATION SYSTEMWO26.02.2015
C02F 1/44
PCT/IB2013/056767SANFT, WilliamSANFT, William
A submerged Bladder with a floor level fixed to a height the same as or just below the lowest low tide level has flexible side-walls and a ceiling which is fixed to a floating Buoy. The Bladder flexible walls have a height that is slightly over the length of the lowest low tide level and the highest high tide level. Seawater desalination membranes are fixed under the floor or integrated into the floor. As the tide rises, the Buoy rises with it. The rising Buoy causes the Bladder to open up. As the Bladder opens up, seawater is pulled into the Bladder to fill the new space available inside the Bladder. The seawater is desalinated as it travels through the membranes, and enters the Bladder as desalinated potable water. At peak high tide mark, the Bladder outlet pipe is opened to drain the contents of the Bladder to an on-shore Reservoir. During the draining process, an air-lock valve on top of the Bladder is opened to aid drainage of water. This operation takes place twice a day consistent with tidal flow, every day, for any volume of water, with no cost for external power source.

2. WO/2015/025624 EXHAUST PURIFICATION SYSTEM OF INTERNAL COMBUSTION ENGINEWO26.02.2015
F01N 3/08
PCT/JP2014/067849TOYOTA JIDOSHA KABUSHIKI KAISHAHABA, Yuki
In an internal combustion engine, a hydrocarbon feed valve (15) and an exhaust purification catalyst (13) are arranged in an engine exhaust passage. A first NOX removal method which injects hydrocarbons from the hydrocarbon feed valve (15) within a predetermined range of period so that the reducing intermediate generated thereby reduces the NOX contained in the exhaust gas and a second NOX removal method which makes the air-fuel ratio of the exhaust gas flowing into the exhaust purification catalyst (13) a first target rich air-fuel ratio by a period which is longer than this predetermined range are used. When the NOX removal method is switched from the second NOX removal method to the first NOX removal method, the air-fuel ratio of the exhaust gas flowing into the exhaust purification catalyst (13) is made a second target air-fuel ratio which is smaller than the first target rich air-fuel ratio.

3. WO/2015/025179 IMPROVED PROCESS INCLUDING A CARBONATATION STEPWO26.02.2015
C13B 20/06
PCT/GB2014/052584T&L SUGARS LIMITEDKERR, John
The invention relates to a process for the removal of contaminants from a liquor, the process comprising: introducing a metal or ammonium hydroxide into the liquor; introducing the liquor into a reaction vessel; bubbling a carbon dioxide gas comprising at least 25% carbon dioxide through the liquor within the reaction vessel; and separating the precipitate formed by the carbonatation of the metal hydroxide from the liquor, the precipitate comprising at least some of the contaminants from the liquor; wherein, on average, the liquor is resident within the reaction vessel for a period of no more than about 60 minutes and wherein the size of the precipitate may be at least partially controlled or controllable by altering the residence time of the liquor in the reaction vessel or the p H of the liquor in the reaction vessel. The invention also relates to a process for the removal of contaminants from a liquor, the process comprising: introducing a metal or ammonium hydroxide into the liquor and bubbling a carbon dioxide gas comprising at least 25% carbon dioxide through the liquor to form a precipitate by carbonatation in a period of no more than about 60 minutes and wherein the size of the precipitate may be at least partially controlled or controllable by altering the residence time of the liquor in the reaction vessel or the p H of the liquor in the reaction vessel. The carbonatation processes may be included in sugar refining or water softening and/or decontamination processes. A use of a carbon dioxide gas comprising at least 25% carbon dioxide in a carbonatation process for removing contaminants from a hydroxide-treated liquor is also provided, wherein the process forms a precipitate in a period of no more than about 60 minutes and wherein the size of the precipitate may be at least partially controlled or controllable by altering the residence time of the liquor in the reaction vessel or the p H of the liquor in the reaction vessel.

4. WO/2015/027031 CATALYSTS FOR OXIDATION OF CARBON MONOXIDE AND/OR VOLATILE ORGANIC COMPOUNDSWO26.02.2015
B01J 23/38
PCT/US2014/052036BASF CORPORATIONYANG, Xiaolin
This application discloses catalysts and methods of making the catalysts. In one embodiment, a catalyst comprising: a reduced precious group metal in an amount greater than about 30 wt% based on the total precious group metal weight in the catalyst, wherein the catalyst oxidizes volatile organic compounds and/or carbon monoxide at a temperature of about 150°C or lower, is disclosed. In another embodiment, a catalyst for oxidation of formaldehyde, methanol, formic acid, and/or carbon monoxide to form carbon dioxide at a temperature of from about 20°C to about 45°C and at about atmospheric pressure, the catalyst comprising: a reduced precious group metal dispersed on a support selected from the group consisting of CeO2, TiO2, ZrO2, AI2O3, SiO2, and combinations thereof, is disclosed.

5. WO/2015/026599 METHOD AND DEVICE FOR IMPROVING EFFICIENCY OF SPONGE OIL ABSORPTIONWO26.02.2015
B01D 53/14
PCT/US2014/050865UOP LLCLADKAT, Kiran
A method for improving efficiency of sponge absorption includes providing cold flash drum liquid to an inlet of a cold stripper to produce a cold stripper net overhead vapor stream rich in liquid petroleum gas, and separately providing hot flash drum liquid to an inlet of a hot stripper to produce a hot stripper net overhead vapor stream rich in hydrogen. The cold stripper net overhead vapor stream and the hot stripper net overhead vapor stream are separately routed to a sponge absorber to recover a liquid petroleum gas output stream using sponge oil. In particular, the cold stripper net overhead vapor stream and the hot stripper net overhead vapor stream are separately routed to the sponge absorber at different tray locations

6. WO/2015/022477 APPARATUS AND METHOD FOR OFFSHORE PRODUCTION OF HYDROCARBONSWO19.02.2015
B63B 35/44
PCT/GB2013/052169SELWA, RichardSELWA, Richard
An apparatus (1) for offshore production of hydrocarbon fluids comprises a buoyant structure (2) connectable to a subsea well (3) via a riser (4). The buoyant structure comprises a storage reservoir for storing hydrocarbon fluid delivered from the subsea well. The storage reservoir constitutes an integral part of the buoyant structure and is adapted to allow stabilisation of the fluid delivered from the well to take place in the storage reservoir. The buoyant structure comprises processing equipment for processing the fluid delivered from the well.

7. WO/2015/022616 DEVICE AND METHOD FOR INDICATING A FILL LEVEL OF A SORPTION STOREWO19.02.2015
B01D 53/02
PCT/IB2014/063841BASF SEWEICKERT, Mathias
A process for indicating a fill level of a sorption store (1), wherein at least one gas adsorbent medium (5) is disposed within at least one vessel (3) and wherein a total amount (ntotal) of a gas (15) stored in the sorption store (1) is computed based on at least one measured temperature value and at least one measured pressure value.

8. WO/2015/022480 WATER TREATMENTWO19.02.2015
C09K 8/52
PCT/GB2014/000318HYDRAFACT LIMITEDANDERSON, Ross
The present invention relates to a method of treating aqueous fluid and apparatus therefor. The method comprises adding an organic compound to a mass of aqueous fluid comprising at least one Kinetic Hydrate Inhibitor (KHI). The organic compound comprises a hydrophobic tail and a hydrophilic head. The hydrophobic tail comprises at least one C-H bond and the hydrophilic head comprises a carboxyl (-COOH) group.

9. WO/2015/024014 CO2 CAPTURE SYSTEM AND METHODWO19.02.2015
B01D 53/02
PCT/US2014/051500ECO POWER SOLUTIONS (USA) CORP.LITTLEFORD, Wayne, S.
A method for removing contaminants from industrial exhaust gas includes contacting the exhaust gas with granular activated carbon, contacting the exhaust gas with a water mist to capture C02 in the water mist, and extracting the captured C02.

10. WO/2015/022716 METHOD FOR THE REMOVAL OF AMMONIACAL AND TOTAL NITROGEN AND FOR THE STABILISATION AND IMPROVEMENT OF THE CHARACTERISTICS OF FILTERABILITY OF AN ANAEROBICAL DIGESTATE THROUGH THE USE OF OZONEWO19.02.2015
C02F 1/78
PCT/IT2014/000218ENEA - AGENZIA NAZIONALE PER LE NUOVE TECNOLOGIE, L'ENERGIA E LO SVILUPPO ECONOMICO SOSTENIBILE LUNGOTEVERE G.A.IZZO Giulio
The present invention concerns a method for the removal of ammoniacal and total nitrogen and for the stabilisation and improvement of the characteristics of filterability of an anaerobical digestate through the use of ozone, wherein it is not provided for any step of nitrification/denitrification and wherein said sludge is treated with ozone in an amount preferably comprised between 24 and 60 mgO3/gTS, at such an amount said sludge releasing ammonia in the gaseous state, which is alternatively conveyed to an acid solution, so as to form an acid salt and precipitate, which is extracted as such, or is split into hydrogen and nitrogen by means of a thermochemical process of membrane separation.


Results 1-10 of 46,544 for Criteria: Office(s):all Language:EN Stemming: true
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