Disclosed is a method for enhanced fuel combustion to maximize the capture of by-product carbon dioxide. According to various embodiments of the invention, a method for combusting fuel in a two-stage process is provided, which includes in-situ oxygen generation. In-situ oxygen generation allows for the operation of a second oxidation stage to further combust fuel, thus maximizing fuel conversion efficiency. The integrated oxygen generation also provides an increased secondary reactor temperature, thereby improving the overall thermal efficiency of the process. The means of in-situ oxygen is not restricted to one particular embodiment, and can occur using an oxygen generation reactor, an ion transport membrane, or both. A system configured to the second stage combustion method is also disclosed.

A method of treating a subject suffering from, or susceptible to, a condition that can be ameliorated by inhalation of gaseous nitrite comprises the use of an apparatus comprising an activating unit that includes a photosensitiser excitable by absorption of light to excite oxygen to a singlet state, and a light source arranged to illuminate the photosensitiser. Air is caused to flow through the activating unit while the photosensitiser is illuminated by the light source, and after passing through the activating unit, is directed to the respiratory tract of the subject.

One or more techniques and/or systems are disclosed for an integrated, dual-chamber, gas separator-receiver. The integrated, dual-chamber, gas separator-receiver can comprise a first and second column, which is integrated, and plumbed together. A source gas can be input through an inlet in the first column, and a target gas, separated from the source gas, can be output through an outlet in the second column. The first column can contain agents that dry the source gas, and separate the target gas from the source gas. The source gas can then be fed into the second column, where it is stored under pressure, at least until needed by some target operation that utilizes the target gas.

Methods and systems for emissions free dispatchable power supply, emissions free chemical energy storage, and emissions free chemical energy distribution are disclosed. Methods include providing water and/or carbon dioxide to an electrolyser; providing electricity from a regional electrical power grid to the electrolyser for electrolysis of the water and/or carbon dioxide to produce oxygen; and providing the oxygen from the electrolyser to a hydrocarbon oxidation device for the oxidation of a hydrocarbon.

The object of this patent is aimed at the production of OXIDIZING GAS CONTAINING 39% O.sub.2 AND 61% N.sub.2 BY WEIGHT, WITH N.sub.2 HAVING A PURITY LEVEL BETWEEN 95% AND 98%, whereby the water that will be deaerated is previously aerated at temperatures ranging from ambient down to 0 C., under pressures between 20.6 and 31 atm, only enough to dissolve all the volume of O.sub.2 in the air that is compressed upon it, along with the portion of N.sub.2 of the air, whose capture cannot be dissociated from the process. Afterwards, part of the air is recovered at the top of the deaeration tank, in the form of oxidizing gas, containing 39% O.sub.2 and 61% N.sub.2 by weight, with N.sub.2, which was originally part of the compressed air and was not solubilized in the water, being collected at the top of the aeration or gasification tank showing a purity level between 95% and 98%.

2ndunlike the State of the Art, which mandatorily requires high water temperature, up to its boiling point, the process degasification, object of the present invention, may be conducted by the preferred embodiment of its pieces of equipment simply by reducing degasification pressure in the degasification tank down to a little bit less than the atmospheric pressure to obtain the same oxidizing gas, and, following degasification, the process water keeps about 20 mg of air, per liter of water, dissolved in itself and, therefore, cannot be used as totally deaerated water.

3degasification may also be carried out by equipment as formed in the first construction variant of the object of this patent by reducing pressure and, at the same time, increasing the temperature, or sending it, in both embodiments, to the equipment, pre-existing in certain industries, which is used to fully deaerate water and, in these cases, produce the oxidizing gas and fully deaerated water.

A liquid treatment apparatus comprises: a first tank in which a first gas containing nitrogen and oxygen and a liquid are stored; a plasma generating apparatus, including a first electrode and a second electrode, which effects discharge between the first electrode and the second electrode and thereby generates plasma that makes contact with at least part of the liquid; and a gas supply apparatus that supplies a first part of the first gas from the first tank to the plasma generating apparatus.

Disclosed herein is a device that functions as a glucose sensor. The device has a reference electrode; a counter electrode, a working electrode; an electrically conducting membrane; an enzyme layer; a semi-permeable membrane; a first layer of a first hydrogel in operative communication with the working electrode; the first layer of the first hydrogel being operative to store oxygen; wherein the amount of stored oxygen is proportional to the number of freeze-thaw cycles that the hydrogel is subjected to; and a second layer of the second hydrogel. Disclosed too is a method that comprises using periodically biased amperometry towards interrogation of implantable glucose sensors to improve both sensor's sensitivity and linearity while at the same time enable internal calibration against sensor drifts that originate from changes in either electrode activity or membrane permeability as a result of fouling, calcification and/or fibrosis.

A process for something separating oxygen from air includes mixing the air with hydro fluoro ether in a closed vessel for a desired period of time so that the oxygen from the air is adsorbed into the hydro fluoro ether, discharging the oxygen-adsorbed hydro fluoro ether from the closed vessel, and flashing the oxygen-adsorbed hydro fluoro ether into a chamber so that so as to separate the oxygen from the hydro fluoro ether. Nitrogen is separated from the air as the oxygen is adsorbed in the hydro fluoro ether in the closed vessel. The step of flashing that includes passing the elevated pressure oxygen-adsorbed hydro fluoro ether across a restricting orifice so as to evaporate the oxygen from the hydro fluoro ether.

The invention relates to the use of biomethanol from the pulp industry in the production of biohydrogen. The preferred biomethanol comprises purified biomethanol derived from black liquor. The invention also relates to a process for the production of biohydrogen from crude biomethanol recovered from black liquor and to a process for producing hydrocarbon biofuel using such biohydrogen as a hydrogen source. The invention further relates to a biofuel production facility for producing fuel from biohydrogen and biohydrocarbon, and to biofuel so produced. The invention makes it possible to produce a biofuel, wherein 100% of the raw material stems from non-fossil sources.

A method and plant for discharging components that are less volatile than oxygen from an air separation plant that contains a main heat exchanger a side condenser and a two-column distillation column system for nitrogen-oxygen separation. The side condenser is constructed as a condenser-evaporator and is arranged in a vessel. A part of the feed air is cooled in the main heat exchanger and liquefied at least in part in the side condenser. A first oxygen fraction is withdrawn in the liquid state from the low-pressure column, introduced into the vessel of the side condenser and in part vaporized. A purge stream is taken off from the bottom of the vessel in the liquid state and discharged or withdrawn as end product. The vessel has a mass transfer section above the side condenser, which mass transfer section corresponds to more than one theoretical plate and fewer than 10 theoretical plates.