초록 ▼

An apparatus and method for adsorption of organic and inorganic volatile compounds in gas flows by continuous and simultaneous distribution of a plurality of primary and secondary flows, through particular distribution and shut-off devices, to a plurality of chambers, in which the individual energy

An apparatus and method for adsorption of organic and inorganic volatile compounds in gas flows by continuous and simultaneous distribution of a plurality of primary and secondary flows, through particular distribution and shut-off devices, to a plurality of chambers, in which the individual energy and mass transfer operations associated with such adsorption occur. High flow-rate and/or concentration are accommodated, following a cyclic adsorption/regeneration process, in which a part of the adsorbent material is used to separate the compounds in gas flows, while the rest of the material sequentially undergoes two or more desorption steps in a stabilized atmosphere suitable to carry the desorbed compounds at very high concentrations, and a final cooling step in a stabilized atmosphere, for preparing the material for continuing the process.

대표청구항 ▼

1. An apparatus for distributing a plurality of fluid flows through a plurality of chambers, the apparatus comprising: a plurality N of process chambers adapted to contain adsorbent material each chamber having a first and a second fluid lines coupled thereto;a first and a second flow distribution d

1. An apparatus for distributing a plurality of fluid flows through a plurality of chambers, the apparatus comprising: a plurality N of process chambers adapted to contain adsorbent material each chamber having a first and a second fluid lines coupled thereto;a first and a second flow distribution device each of said distribution devices comprising: a plurality P of fluid lines;a plurality X of synchronized distribution valves where X=P, each coupled to a plurality Y of fluid lines where Y=N, and a respective one of said plurality P of fluid lines, wherein said distribution valves are constructed to sequentially provide selective fluid coupling between the respective P line, and at least one of each of said Y lines;wherein said plurality X of distribution valves being operable simultaneously;a plurality Z of manifolds where Z=N, each having a plurality A of fluid lines where A=P, wherein each of said plurality A of fluid lines is coupled to the respective Y fluid line of each of said X distribution valves, and wherein the manifold provides fluid communication therebetween;wherein each of said first lines of said N process chambers is coupled to a respective manifold of said Z manifolds of said first distribution device, and each of said second lines of said N process chambers is coupled to a respective manifold Z of said second distribution device; and,wherein said first distribution device and said second distribution device are operated synchronously. 2. An apparatus as claimed in claim 1, wherein said plurality of distribution valves of each of said distribution devices comprises plugs, and wherein the plugs of each distribution device rotate about a common axis. 3. An apparatus as claimed in claim 2, wherein said plugs are driven by a drive system comprising a ratchet. 4. An apparatus as claimed in claim 2, wherein each distribution valve of said first and second distribution devices has a wall with a plurality Y of ports formed therein, and wherein each plug being slidlingly movable along the wall, to selectively close at least one of said ports. 5. An apparatus as claimed in claim 1, wherein each of said N process chambers contains adsorbent material retained in said process chambers by meshes. 6. An apparatus as claimed in claim 1 wherein P=4 and N=8. 7. A method for purification of a gas flow containing polluting compounds, comprising the steps of: Providing an apparatus for distributing a plurality of fluid flows through a plurality of chambers, the apparatus comprising: a plurality N of process chambers adapted to contain adsorbent material each chamber having a first and a second fluid lines coupled thereto;a first and a second flow distribution device each of said distribution devices comprising: a plurality P of fluid lines;a plurality X of synchronized distribution valves where X=P, each coupled to a plurality Y of fluid lines where Y=N, and a respective one of said plurality P of fluid lines, wherein said distribution valves are constructed to sequentially provide selective fluid coupling between the respective P line, and at least one of each of said Y lines;wherein said plurality X of distribution valves being operable simultaneously;a plurality Z of manifolds where Z=N, each having a plurality A of fluid lines where A=P, wherein each of said plurality A of fluid lines is coupled to a respective Y fluid line of said X distribution valves, and wherein the manifold provides fluid communication therebetween;wherein each of said first lines of said N process chambers is coupled to a respective manifold of said Z manifolds of said first distribution device, and each of said second lines of said N process chambers is coupled to a respective manifold Z of said second distribution device; and,wherein said first distribution device and said second distribution device are operated synchronously;distributing, a plurality of separate gas flows, comprising an adsorption flow; at least one primary desorption flow, a secondary desorption flow and a cooling flow among the plurality N of process chambers for simultaneously carrying out an adsorption step, at least one primary desorption step in a closed circuit inert or stabilized gas, a secondary desorption step in an open circuit of inert or stabilized gas and a cooling step;said distribution being performed in parallel, utilizing said apparatus;wherein the number of beds where adsorption takes place is greater than the number of beds where primary desorption takes place;wherein the number of beds where secondary desorption takes place is smaller than the number of beds where primary desorption takes place,wherein the number of beds where cooling takes place is equal to or greater than the number of beds where secondary desorption takes place;wherein the distribution of said adsorption, desorption, secondary desorption and cooling flows is cyclically changed through N possible configurations; and,wherein the desorption flows are countercurrent to said adsorption and cooling flows. 8. A method as claimed in claim 7, wherein said adsorbent material consists of macroporous styrene-divinylbenzene resins or activated carbons in the form of small-diameter spherules derived from pitch residues of oil distillation, with a very low ash content. 9. A method as claimed in claim 7, further comprising the steps of: generating an outflow from said primary desorption flow;injecting a flow of liquid nitrogen in a cryogenic exchanger;cryogenically purifying said outflow from said primary desorption flow by separating the compounds contained therein in liquid form;using the nitrogen that evaporates during cryogenic purification to feed the secondary desorption flow; and,using a portion of said purified outflow to feed said secondary desorption flow.