A device for attaching connective tissue to bone has a longitudinal axis and comprises an annular toggle member and a body member disposed distally of the toggle member, such that there is an axial space between the toggle member and the body member. The toggle member is movable between an undeployed position wherein the toggle member has a smaller profile in a direction transverse to the axis and a deployed position wherein the toggle member has a larger profile in the direction transverse to the axis. When installed in a desired procedural site, in suitable bone, suturing material extends axially through a center aperture in the annular toggle member, without being secured to or contacting the toggle member. This approach permits a suture attachment which lies entirely beneath the cortical bone surface, and which further permit the attachment of suture to the bone anchor without the necessity for tying knots, which is particularly arduous and technically demanding in the case of arthroscopic procedures.

Method and apparatus for attaching connective tissues to bone using a knotless suture anchoring device

Provided are apparatus and systems having a poppet valve assembly and swing adsorption separation techniques related thereto. A poppet valve includes a valve body, a plurality of static valves fixedly secured to the valve body and a single dynamic poppet valve having a plurality of openings. The plurality of static valves align and mate with the plurality of openings. The single dynamic poppet valve reciprocates to selectively open and close the plurality of static valves.

Apparatus and systems having a reciprocating valve head assembly and swing adsorption processes related thereto

An adsorber with minimal dead volume especially suited to reverse-flow applications comprises: a) an adsorber body; b) a first head engaged with said adsorber body; c) a first conduit extending from outside said head to at least partially through said head; and d) a first valve in flow communication with said first conduit controlling fluid flow along a flow path extending from the first valve and through the adsorber body. The adsorber is especially suited for use in a process for swing adsorption separation processes.

Integrated Adsorber Head and Valve Design and Swing Adsorption Methods Related Thereto

A knotless suture lock and bone anchor wherein a suture, looped through a tissue, is threaded through a plurality of body holes in the anchor to cinch the suture and tissue to the anchor without tying a suture knot on the tissue, and wherein the anchor is adapted for embedding in a bone. The tissue is secured to the anchor by suturing the tissue without a suture knot, fastening the standing leg portion of the suture on a suture leg-anchoring structure, and threading the working leg portion of the suture through the body holes. Pulling on the working leg portion of the suture tightens the suture on the body structure and cinches the loop without a suture knot on the tissue. The bone-embedding structure comprises a plurality of barbs adapted to resist pullout of the anchor from the bone.

Knotless suture lock and bone anchor implant method

Carbon dioxide, water, nitrous oxide and optionally ethylene are removed from a feed air stream by a temperature swing adsorption using a first adsorbent such as alumina to adsorb water, a second adsorbent such as 13X zeolite to adsorb carbon dioxide, and a third adsorbent such as binderless calcium exchanged X zeolite to adsorb nitrous oxide and optionally ethylene, prior to cryogenic separation of the purified air stream.

Purification of air

Process for separating at least carbon dioxide (CO2) contained in a gas stream, preferably air, in which at least carbon dioxide is adsorbed on a zeolite-X having a Si/Al ratio of approximately 1 to 1.5 and containing at most 35% of K+ cations, between 1 and 99% of Na+ cations and at most 99% of Ca2+ cations. This process is carried out at a temperature ranging from −40° C. to +80° C. Optionally, impurities chosen from water vapour and hydrocarbons, particularly ethylene, are also removed. The air thus purified is then capable of being cryogenically distilled.

Process for purifying air by adsorption before cryogenic distillation

Process and apparatus for the purification of a gaseous flow containing at least one impurity which can be carbon dioxide, water vapor and/or hydrocarbon. The impurity is adsorbed on a bed of adsorbent containing at least one adsorbent material, it being possible to use stacked adsorbent beds. Atop the uppermost bed is a layer of particulate ballast having a density greater than that of the adsorbent. The bed of ballast exerts a mechanical pressure on the subjacent adsorbent and prevents fluidization of the upper portion of the subjacent adsorbent. As a result, the rate of gas flow through the adsorbent can be increased.

Process and device for purification of gas by adsorption with fixed horizontal beds

A process, particularly of the TSA type, for separating impurities of the nitrogen protoxide (N 2 O) and possibly carbon dioxide (CO 2 ) or ethylene (C 2 H 4 ) type which are contained in a gas stream, such as air. The impurities of nitrogen protoxide type are removed on a faujasite zeolite having a Si/Al ratio of 1 to 1.5 and containing from 0 to 35% of K + cations, between 1 and 99% of Na + cations and between 1 and 99% of Ca 2+ cations, preferably at least 50% of Ca 2+ cations. The separation is preferably carried out at a temperature of approximately −40° C. to +80° C., preferably at room temperature. Advantageously, the process is employed for prepurifying atmospheric air before cryogenic distillation of the air thus prepurified.

Process for purifying a gas stream of its N2O impurities

The invention concerns a method for producing a gas mixture containing hydrogen and carbon monoxide, and optionally nitrogen, from at least a hydrocarbon such as methane, propane, butane or LPG or natural gas, which consists in performing a partial catalytic oxidation (1) of one or several hydrocarbons, at a temperature of 500° C., at a pressure of 3 to 20 bars, in the pre of oxygen or a gas containing oxygen, such as air, to produce hydrogen and carbon monoxide; then in recuperating the gas mixture which can subsequently be purified or separated, by pressure swing adsorption, temperature swing adsorption of by permeation (3), to produce hydrogen having a purity of at least 80% and a residue gas capable of supplying a cogeneration unit In another embodiment, the gas mixture can subsequently be purified of its water vapour impurities and carbon dioxide to obtain a thermal treatment atmosphere containing hydrogen, carbon monoxide and nitrogen.

Process for production of hydrogen by partial oxidation of hydrocarbons

Process for the purification of an air flow containing carbon dioxide (CO2) and water vapor, in which at least part of the CO2 impurities and water vapor are removed by adsorption of said impurities on at least one calcined alumina containing at most 10% by weight of at least one alkali or alkaline earth metal oxide, said adsorption being carried out at a temperature between -10 ° C and 80 ° C.

Cyrille Millet

Papers

Process for purifying air by adsorption before cryogenic distillation

Process and device for purification of gas by adsorption with fixed horizontal beds

Process for purifying a gas stream of its N2O impurities

Process for production of hydrogen by partial oxidation of hydrocarbons

Process for eliminating CO2 and water from air by adsorption on calcined alumina