L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des

L'air Liquide, Societe Anonyme a Directoire Et Conseil De Surveillance Pour L'etude Et L'exploitation Des Procedes Georges Claude

L'air Liquide, Soci&#xe9;t&#xe9; Anonyme Pour L'etude Et L'exploitation Des Proc&#xe9;d&#xe9;s Georges Claude

American Air Liquide, Inc.

Xavier Vigor

Pierre Petit

Serge Moreau

Lionel Barry

Antoine Willemot

Jean-Marc Scudier

Jerome Jutard

Christian Monereau

Dominique Jouvaud

Christian Barbe

Mindi Xu

Pierre Bodelin

Pierre Gauthier

Leon Hay

Patrick Bacot

Bernard Sardan

Christine Marot

Wilfrid Petrie

Anne Dubois

Michel Poteau

Christophe Charrier

Patrice Ollivier

Sylvain Fourage

Jérôme Bres

Anne Barbier

Michel Boudet

Patrick Dilly

Michel Eclancher

Franck-Stephane Durtschi

Olivier Bomard

V&eacute;ronique Dulphy Vigor

Franck-Stéphane Durtschi

The invention relates to a device including: at least one fluid-using apparatus; at least one movable tank capable of and intended for providing at least the fluid and connected, via pipes, to the fluid using apparatus, the movable tank containing, at the outset, a given initial amount of the gas; and a means for assessing amounts of the fluid that are used by the fluid using apparatus from the movable tank, the assessment means being rigidly connected to the fluid-using apparatus.

Method and device for tracking content of a movable fluid tank

The gas separation apparatus comprises a flexible wall which is maintained in a placed position on an upper end of an adsorbant material; the volume between the wall and an upper dome communicates with one of inner and outer chambers on both sides of the adsorbant (). The invention can be used to separate air components.

Apparatus for the separation of at least one constituent of a gas mixture by pressure swing adsorption

An oxygen concentrator portable by a patient, permitting producing a flow of gas containing 50% to 95% of oxygen from air, comprising air compression device, elements for gas separation by adsorption with pressure variations, and electrical energy storage unit keeping its charge for at least 30 minutes, the concentrator having a total weight less than 10 kg. Preferably, the gas separation elements are a PSA system using a zeolite X exchanged with lithium, as the adsorbent.

Portable oxygen concentrator

The invention relates to a device for measuring the fluid consumption of a user over a given measurement time, including a volumetric meter ( ) connected to a central information processing unit ( ). This unit is designed to take a series of readings at successive intervals in said measurement time, so as to compare each reading with a reference value that corresponds to a predetermined nominal consumption threshold and thus from this deduce the quantity consumed over said measurement time corresponding to consumption with a flow rate higher than the nominal consumption threshold.

Device for measuring the fluid consumption of a user over a given time

In this process, the apparatus for separating the feed gas is connected to the delivery side of at least one variable-rotation-speed compressor, whose speed is controlled on the basis of the measurement of a parameter representative of the flow of gas product. The process is useful in the production of nitrogen from atmospheric air.

Process and plant for producing a variable gas output

Briefly, this invention uses one or more pressure vessels having installed therein on its inside a balloon of flexible and non-expandable wall to smoothly and continuously deliver a chemical to any end user without contamination and gas dissolution. Since the balloon installed inside the pressure vessel isolates a high pressure gas from the chemicals, gas dissolution in the chemical and the resulted gas bubble problems are effectively eliminated. Further, contaminants in the high pressure gas which fills the balloon will not be transferred into the chemical and the extremely toxic chemical will not be transferred into the gas to be exhausted as a serious environmental issue. Unlike the vacuum/pressure system, the contamination by the ambient air leaking into the system is avoided because the disclosed delivery system is always with the pressure higher or equal to the ambient pressure.

Methods and systems for distributing liquid chemicals

The plant comprises, on site, a compressed-air provision and distribution system (L.sub.A) with at least one dedicated air compressor (CO2, CO3), an air-gas production and provision system (L.sub.G) comprising an air treatment unit (S), with a reservoir R of the said air gas and normally fed by a compressor (CO1). In temporary operating mode, with one air compressor (CO2) off-line, the compressed air from the compressor (CO1) of the air gas provision system (S) is at least in part diverted (C), typically with pressure reduction (D), to sustain the production of the compressed air system (L.sub.A), the air gas then being at least in part provided by the reservoir (R).

Combined process and plant for producing compressed air and at least one

Steel-making method and plant

Method for purifying hydrogen based gas mixture using a lithium-

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%.

Process for the separation of nitrogen from a gaseous mixture by

In a 'vacuum' type cycle, the depressurization of a first adsorber at the high pressure of the cycle is effected by placing it in communication with the outlet of a second adsorber at the low pressure of the cycle. This communication takes place simultaneously with countercurrent pumping in a first stage for the second adsorber and in a second stage for the first adsorber, the recompression to the high pressure of the cycle being effected by production gas. Used for the production of oxygen from air.

Process for the production of a gas by adsorption

A process for treating a gaseous mixture, particularly air, by pressure swing adsorption (PSA), of the type in which three adsorbers (1 to 3) are used in each of which is carried out, for a given nominal production, a cycle comprising the following successive stages, the cycle being offset from one adsorber to the other by a third of the nominal duration (T) of the cycle:

Process for the treatment of a gaseous mixture by adsorption with

Rotatable device for the separation by adsorption of at least one

An adsorber having an upright longitudinal extent includes two perforated parallel panels extending within the vessel formed therein and spaced apart defining an adsorbent mass chamber. The adsorbent mass is in two longitudinal parts having a first part of fine particles and a second part of larger particles. The gas to be treated is circulated horizontally between the two perforated panels. This device allows the treatment cycle to be less than 60 seconds with the same or better performance. This adsorber and process are preferably used for the separation of oxygen from air.

Adsorber and process for the separation by adsorption

A process for the separation by adsorption of at least a component of a gaseous mixture whereby the gas mixture is circulated through an adsorbent mass. A plurality of adsorbent mass compartments are provided and are arranged sectorially about and fixed to a support shaft rotating about an axis, and collection chambers are provided radially internally and externally of each adsorbent compartment. Gas circulation is provided radially through each adsorbent compartment as it rotates about a stationary gas distribution unit.

Process and apparatus for separating a at least a component of a gaseous

Growing community of inventors

Paris, France

Xavier Vigor