Abstract: A method for treating or preventing ischemia comprising administering to a patient by an intravascular route a gaseous mixture comprising nitric oxide (NO) and carbon dioxide (CO.sub.2), wherein the nitric oxide is present in an amount effective to treat or prevent ischemia.A gaseous mixture for treatment or prevention of ischemia comprising:(i) nitric oxide in an amount effective to prevent ischemia; and(ii) carbon dioxide.

Abstract: A process and installation for the separation of air in a cryogenic distillation apparatus (24) comprising a distillation column (30, 42) and in which the supplied air is separated to produce a fraction rich in oxygen and a fraction rich in nitrogen as products. The purities of these products are maintained substantially constant during variations of demand of either product or of the flow rate or of the pressure of the supplied air by introducing an excess of liquid rich in nitrogen into the distillation apparatus when the demand for the product or the flow rate of the supplied air increases, and by withdrawing an excess of liquid rich in nitrogen from the distillation apparatus, and storing this liquid, when the demand for the product or the flow rate of the supplied air decreases.

Abstract: The arc welding, with a refractory electrode, using alternating current, is performed with a gaseous protective mixture including at the location of the weld, at least 50%, typically between 60 and 80% of helium and at least 300 vpm, typically between 400 and 800 vpm, of nitrogen, the remainder being argon.Application to manual or automatic welding of aluminium components.

Abstract: The arc welding, with a refractory electrode, using alternating current, is performed with a gaseous protective mixture employing, at the location of the weld, at least 60%, typically between 70 and 80% of helium and more than 1000 vpm, typically between 1100 and 1200 vpm, of carbon dioxide, the remainder being argon.Application to manual or automatic welding of aluminium components.

Abstract: A process for the substantial elimination of at least one of the impurities carbon monoxide and hydrogen contained in a gaseous compound, according to which:(a) at least one of the impurities carbon monoxide and hydrogen contained in the gaseous compound is caused to react with oxygen, in contact with a catalyst comprising particles, on the one hand, (i) of gold, silver or gold and silver, and, on the other hand, (ii) of at least one metal of the platinum family, these particles being supported by a support to form, respectively, carbon dioxide and water;(b) as needed, the carbon dioxide and water are eliminated from the gaseous compound;(c) the gaseous compound is recovered substantially free from its impurities of carbon monoxide and/or hydrogen.

Abstract: PSA process for the separation of nitrogen from a gaseous mixture containing nitrogen by selective adsorption of nitrogen from the gaseous mixture in an adsorbent mass with cyclic pressure variations. At least one nitrogen adsorption phase is carried out at high pressure and at least one nitrogen desorption phase is carried out at low pressure. The adsorbent mass is arranged in a rotating adsorber and at least 50% of the adsorbent mass is constituted by a zeolite exchanged with lithium by more than 50%.

Abstract: A device for spreading a flame, comprises at least one principal nozzle (35) delivering a jet of combustible gas or combustion supporting gas (6); at least one secondary nozzle (8) delivering a jet of combustion supporting gas or combustible gas (12) which flows next to the principal jet and which has a substantially constant thickness. At least one curved surface (9) is disposed tangentially to the jet of secondary gas so as to deflect it by the Coanda effect, to draw in the principal jet of gas (6) and to mix the gas of the secondary jet (12) and the gas of the principal jet (6) to form a flame.

Abstract: The mouthpiece (2) of a respirator (1) is connected to a bottle (8) of a gaseous mixture containing nitric oxide by a line (10) comprising an electrovalve (18) controlled (17) by a signal representing a supply (7, 15, 12) of a flow of respiratory mixture by the respirator (1). The installation is controlled so as to supply, upon inhalation, a gaseous mixture comprising between 21 and 100% of oxygen and between 10 and 50 ppm of nitric oxide.

Abstract: In order to precool a flow of gas to be distilled, before a purification stage, it is sent into an exchanger (5) where it is cooled by heating a flow of refrigerant (13B). At least a part of this refrigerant has its pressure reduced before cooling the unpurified gas and may be a fraction of the gas to be distilled or a product of the distillation. It is preferably a cycle gas of the system. This arrangement makes it possible to obviate a refrigerating unit.

Abstract: A device for supplying gas to an analyzer for measuring traces of impurities in the gas comprising: (i) a source of pure gas; (ii) a set of at least first and second bypass gas lines, arranged in parallel and fed by the source of pure gas, the first and second bypass gas lines having a common gas entry and a common gas exit, the common gas exit being in communication with a feed line of the analyzer through a common gas exit line; (iii) a device for charging a gas in the first bypass gas line with a predetermined quantity of at least one impurity for forming a standardizing gas; (iv) a restriction disposed in each of the first and second bypass gas lines, each restriction being calibrated to divide the flow of pure gas feeding the set between the first and second bypass lines in a predetermined ratio; and (v) a flow regulator for regulating the flow of pure gas feeding the set of bypass gas lines, disposed between the source of pure gas and the common gas entry of the first and second bypass gas lines, wherei

Abstract: A device for separating at least one component from a gas mixture, comprising at least a pair of adsorber units, each adsorber unit comprising an envelope defining an inner volume having a lower end zone and an upper end zone. There is at least one adsorbent layer between the lower and upper end zones. A first conduit has one end communicating with the lower end zone, and a second conduit has one end communicating with the upper end zone. The adsorber units of the pairs are superposed and one of the first and second conduits of each adsorber includes a vertical central tube portion. The vertical central tube portions of the pair of adsorber units are mechanically interconnected in endwise abutting relationship. The adsorber units are superposed such that the envelopes of adjacent units leave an intermediate space therebetween. The first and second conduits each have an outer portion extending out of the envelope in the intermediate space.

Abstract: The plant comprises an adsorbent-filled tank (8) permanently interposed in the line (2), between the purification unit (3), operating by adsorption of solidifiable impurities from the gas mixture (5) containing carbon monoxide, and the cryogenic separation unit which delivers pure carbon monoxide at its outlet (6). The adsorbent in the tank (8), advantageously the same as the adsorbent in the adsorbers (4A, 4B) of the purification unit (3), has an affinity for carbon monoxide, thus making it possible to reduce the cyclic variations in the carbon monoxide production delivery rate which results from the cyclic operation of the adsorbers (4A, 4B) of the separation unit (3).

Abstract: A method for the control of the operation of an installation for the separation of air by cryogenic distillation comprising a double distillation column wherein the top of a medium pressure column and the base of a low pressure column are thermally interconnected by a vaporizer-condenser supplied with liquid oxygen from a bath of liquid oxygen in the base of the low pressure column. Liquid oxygen from the bath is continuously tested to detect the content of nitrous oxide in the bath, and upon the detection of a fall in the nitrous oxide content of the bath when the installation is operating under equilibrium conditions, the flow of liquid oxygen to the vaporizer-condenser is increased to raise the detected nitrous oxide content of the bath. But when the detected nitrous oxide level falls, then either a liquid oxygen purge line is opened farther, or else the operating time or pressure of switching adsorbers in the air supply is changed.

Abstract: Process for the production of oxygen by cryogenic distillation of a supply mixture containing oxygen and nitrogen in a double column (5) comprising a medium pressure column (6) and a low pressure column (7), in which there is partially condensed at least one fraction of the supply mixture in a condenser (8) by vaporization of liquid oxygen from the base of the low pressure column (7), said partially condensed mixture is sent to the medium pressure column (6), all the oxygen destined to form the gaseous production being withdrawn in liquid phase from the base of the low pressure column (7), and brought to its utilization pressure.

Abstract: The present invention relates to a solenoid-operated valve for a thermally insulated piping having a thermally insulated outer periphery suitable for transporting low-temperature fluid, high-temperature fluid or the like and relates also to an attachment construction for the valve.Conventionally, with this type of solenoid-operated valve for a thermally insulated piping, since it is necessary to to increase a magnetic flux density of the solenoid coil by increasing the number of turns of the oil or the electric current to be applied thereto, there has been the problem of high production costs and running costs.In the case of the solenoid-operated valve for a thermally insulated piping according to the present invention, inside a heat-insulating layer (6) surrounding flow passages (7, 20, 21, 26, 33) in the form of a pipe, there is provided a fixed core (23) constituting a magnetic circuit between a solenoid coil (17) and a movable coil (18).

Abstract: The cryobiological container comprises a double walled reservoir structure (1) comprising an internal shell (2) having a cylindrical side wall (4) and a bottom wall (5) and forming an internal volume accessible through an upper opening (6) of the same diameter as the cylindrical wall (4), the bottom wall (5) comprising a central support (7) adapted to receive a pivot (8) fixed to the bottom (9) of a rotatable storage container (10) adapted to be received within the internal shell (4) and having a cylindrical side wall (11) of a diameter slightly less than that of the lateral wall (4) of the internal shell (2) and provided at its periphery with a plurality of guiding and centering rollers (15) coacting with the side wall (4) of the internal shell (2). The access opening (6) is preferably closable by a plug carried by a cover structure pivotably mounted on the reservoir structure (1).

Abstract: An oxyburner (1) is associated with an opening (3) comprising a through passage (2) comprising a substantially cylindrical inlet region (5) receiving the downstream end of the oxyburner (1) and a substantially cylindrical outlet region (4) of a diameter D.sub.s and a length L.sub.s, the ratio D.sub.s /D.sub.e being comprised between 1.5 and 2.5 and the ratio L.sub.s /(D.sub.s -D.sub.e) comprised between 2 and 7. The speed of ejection of the oxygenated combustible gas is greater than 5 meters/second and the speed of ejection of the combustible gas is greater than the speed of the combustion-supporting gas.

Abstract: A method and unit for easily and continuously producing high pressure gaseous monosilane and high pressure liquid monosilane, each having an ultra high purity. In the ultra high purity monosilane producing method, a feed monosilane gas is pressurized, cooled down and subjected to a gas-liquid phase separation. The separated gas phase is introduced to a lower rectification column 1 so as to be rectified. The gas obtained through this rectification is introduced to an upper rectification column 2 so as to be rectified, wherein a gaseous monosilane product or liquid monosilane product having an ultra high purity is taken out of the bottom portion of the upper rectification column.

Abstract: Provided is a burner with external mixing which comprises, just below a drilled plate forming the nozzle, a homogenization chamber in which one of the components of the flame penetrates radially via orifices. The other component feeding the flame passes through the chamber via a series of axial tubes running out onto the front face of the drilled plate where the mixing of the components occur. The burner has application especially to the incineration of industrial waste with oxygen.

Abstract: Carbon monoxide is recovered by a cryogenic route from a gas mixture, for example from the tail gas of an operation for scrubbing with nitrogen in the preparation of an ammonia synthesis mixture, this mixture containing carbon monoxide, hydrogen and other constituents including nitrogen. The hydrogen is separated off by partial condensation and the other components by distillation of the condensate. The carbon monoxide is produced by distillation in two columns, of which only one has a head condenser fed with a flow of liquid carbon monoxide. A liquid flow is drawn at an intermediate level in the column with the head condenser and directed to the head of the other column.