Process for the compressive regeneration of flexible, porous materials

Claim 2

A process for the compressive regeneration of flexible, porous particulate material which is loaded with substances removed from liquids treated in a reactor in which the porous material is used as filter particles, oil-separating particles, or carrier, particles, which comprises regenerating the loaded material by: conducting the loaded material together with liquid from the reactor into a press chamber associated with the reactor and having movable press means, with the porous material being drawn into the press chamber from the reactor by moving the press means in a rearward direction to create a suction effect; moving the press means forward after the loaded material has been drawn into the press chamber to press out the liquid and the loading substances from the loaded material while retaining the material in the press chamber; conducting additional liquid into the press chamber for dispersing the porous material in the additional liquid, by subsequently moving the press means rearwardly; and then moving the press means forward to force the regenerated material dispersed in the additional liquid back into the reactor.

Claim 3

A process according to claim 1, further comprising after filling the press chamber, pressing the liquid out of the loaded material by at least one partial forward movement of the press means; taking liquid into the press chamber by at least one partial, subsequently conducted rearward movement of the press means for cleaning the material by flushing; and, by a subsequent forward movement of the press means, pressing the liquid and the substances to be removed out of the material.

Claim 4

A process according to claim 2, wherein wastewater from the reactor is taken in as the liquid to clean the material by flushing.

Claim 5

A process according to claim 2, wherein fresh water is taken in as the liquid for cleaning the material by flushing.

Claim 6

A process according to claim 3 or 4, wherein the water for cleaning the material by flushing is introduced into the press chamber downstream from the press means relative to the stream flow when the press means forces water out of the press chamber.

Claim 7

A process according to claim 1, 2, 3 or 4, wherein the liquid taken in for transporting the regenerated flexible, porous material is wastewater from the reactor.

Claim 8

A process according to claim 1, 2, 3 or 4, wherein the liquid taken in for transporting the regenerated flexible, porous material is fresh water.

Claim 9

A process according to claim 5, wherein the water taken in for transporting the regenerated flexible, porous material is wastewater from the reactor.

Claim 10

A process according to claim 5, wherein the water taken in for transporting the regenerated flexible, porous material is fresh water.

Claim 11

A process according to claim. 2, 3 or 4 comprising forcing the substances out of the loaded flexible, porous material by compressing the material to about 20-5% of its expanded volume.

Claim 12

A process according to claim 5 comprising forcing the substances out of the loaded flexible, porous material by compressing the material to about 20-5% of its expanded volume.

Claim 13

a process according to claim 6 comprising forcing the substances out of the loaded flexible, porous material by compressing the material to about 20-5% of its expanded volume.

Claim 14

A process according to claim 7 comprising fdrcing the substances out of the loaded flexible, porous material by compressing the material to about 20-5% of its expanded volume.

Claim 15

A process according to claim 8 comprising forcing the substances out of the loaded flexible, porous material by compressing the material to about 20-5% of its expanded volume.

Claim 16

A process according to claim 9 comprising forcing the substances out of the loaded flexible, porous material by compressing the material to about 20-5% of its expanded volume.

Claim 17

A process according to claim 1, 2, 3 or 4, wherein the substances to be removed from the loaded flexible, porous material are removed by repeatedly compressing and expanding and simultaneously intaking and removing flushing liquid.

Claim 18

A process according to claim 10, wherein the substances to be removed from the loaded flexible, porous material are removed by repeatedly compressing and expanding and simultaneously intaking and removing flushing liquid.

Claim 19

A process according to claim 1, 2, 3 or 4 further comprising flowing compressed air into the liquid for transporting the regenerated material during the forcing of the regenerated material, dispersed in the liquid for transporting, into the reactor.

Claim 20

A process according to claim 1, 2, 3 or 4 wherein said press means is moved with a stroke velocity of about 0.01-0.5 m/sec.

Claim 21

A process according to claim 10, wherein said press means is moved with a stroke velocity of about 0.01-0.5 m/sec.

Claim 22

A process according to claim 17 wherein said partial forward movements of the press means are effected a sufficient number of times to remove at least 90% of loading substances.

Claim 23

A process according to claim 18 wherein about 5-250 Nm 3 air/m 3 press chamber is flowed into the liquid for transporting the regenerated material into the reactor.

Claim 24

A process for the compressive regeneration of flexible, porous particulate material which is loaded with substances removed from liquids treated in a reactor in which the porous material is used as filter particles, oil-separating particles, or carrier particles, which comprises regenerating the loaded material by: conducting the loaded material together with liquid from the reactor into a press chamber associated wtih the reactor and having movable press means, with the porous material being drawn into the press chamber from the reactor by moving the press means in a rearward direction to create a suction effect; moving the press means forward after the loaded material has been drawn into the press chamber to press out the liquid and the loading substances from the loaded material while retaining the material in the press chamber, said forcing out of the substances out of the loaded flexible, porous materials being effected by compressing the material to about 20-5% of its expanded volume; conducting additional liquid into the press chamber for dispersing the porous material in the additional liquid, by subsequently moving the press means rearwardly; and then moving the press means forward to force the regenerated material dispersed in the additional liquid back into the reactor.

Claim 25

A process for the compressive regeneration of flexible, porous particulate material which is loaded with substances removed from liquids treated in a reactor in which the porous material is used as filter particles, oil-separating particles, or carrier particles, which comprises regenerating the loaded material by: conducting the loaded material together with liquid from the reactor into a press chamber associated wtih the reactor and having movable press means, with the porous material being drawn into the press chamber from the reactor by moving the press means in a rearward direction to create a suction effect; moving the press means forward after the loaded material has been drawn into the press chamber to press out the liquid and the loading substances from the loaded material while retaining the material in the press chamber, said forcing out of the substances out of the loaded flexible, porous materials being effected by compressing the material to about 20-5% of its expanded volume; conducting additional liquid into the press chamber for dispersing the porous material in the additional liquid, by subsequently moving the press means rearwardly; and then moving the press means forward to force the regenerated material dispersed in the additional liquid back into the reactor.

Claim 26

A process according to claim 23 wherein said compression of the flexible materials is effected to about 15-7% of its expanded volume.

Claim 27

A process according to claim 23 wherein the flexible material regenerated is an open cell porous foam of one polyurethane, polyethylene, polypropylene and silicone, and has a density when dry of about 15-100 kg/m 3 , compressibility of about 95-90% by volume and particle size of about 3-50 mm in diameter.

Claim 28

A process according to claim 25 wherein the flexible materials are retained in the press chamber during the compression step by means of a perforated plate having about 1-5 holes per 10 cm 2 of a diameter of about 2-10 mm.

Claim 29

A process according to claim 23 wherein the amount of additional liquid taken into the press chamber for dispersing the porous therein material is about 10-80% of the volume of the press chamber.