Method and arrangement for the thermal regeneration of charged adsorption materials

Claim 2

Method for the thermal regeneration of solid adsorption materials charged with adsorbed impurities which comprises passing a heated gaseous regeneration medium through the charged adsorption material to expel the impurities principally of an organic nature therefrom and discharging regeneration medium containing desorbate from the adsorption material, maintaining a heat pump in which a cooling medium flows in a cooling medium circuit by propelling means which directs said medium in heated condition to a condenser, disposed out of direct contact with said adsorption material, of a first heat exchange of the heat pump wherein the medium is cooled and gives off heat, and the cooled medium then flows to a vaporizer of a second heat exchanger of the heat pump wherein the medium expands and extracts heat, and returning the medium to the propelling means, heating the regeneration medium prior to entrance to the adsorption material by passing it through said first heat exchanger of the heat pump in indirect heat exchange with the cooling medium in said condenser, and cooling said discharged regeneration medium containing desorbate by passing it through said second heat exchanger in indirect heat exchange with the cooling medium in said vaporizer.

Claim 3

Method according to claim 1, wherein said impelling means is a compression pump driven by a combustion engine, wherein at least a part of the exhaust gases of the combustion engine is used as regeneration medium and wherein at least a part of the exhaust gas of the combustion engine is introduced as a protective gas for displacing air in the system of enclosed adsorption material, first heat exchanger, second heat exchanger and connecting pipes.

Claim 4

Method according to claim 1, or claim 2, wherein a plurality of heat pump circuits with different cooling media are provided, in a cascade arrangement whereby the heat of one heat pump circuit is transferred to a heat exchanger which is common to both circuits, and one side of said heat exchanger acts as a condenser of the first heat pump circuit and its second side acts as the evaporator of the second heat pump circuit.

Claim 5

Method according to claim 1, wherein said impelling means is an absorber to absorb cooling medium, a pump to direct the absorbant containing cooling medium to an expeller heated by a combustion device to expel the cooling medium and direct it to the condenser, and wherein exhaust gas from said combustion device is, at least partly, used as regeneration medium.

Claim 6

Method according to claim 4, wherein at least a part of the exhaust gas of said combustion device is introduced as a protective gas for displacing air in the system of enclosed adsorption material, first heat exchanger, second heat exchanger, and connecting pipes.

Claim 7

Method according to claim 4, wherein said pump is a vapor bubble pump and wherein said vapor bubble pump has a bubble-forming vessel which operates as an expeller heated with a combustion device and wherein adsorption liquid from the expeller flows back through a line to the adsorber and wherein said vapor bubble pump has a bubble forming vessel which has wound around it said line carrying hot adsorption liquid to transfer some of its sensible heat to the liquid contents of the bubble forming vessel to form vapor bubbles which rise upward and keep the circulation of the adsorption liquid circulating.

Claim 8

Method according to claim 6, wherein the absorption liquid after separation of cooling medium is cooled by indirect heat exchange with incoming cold absorption liquid containing cooling medium and the cooled absorption liquid directly conducted to the absorber.

Claim 9

Method according to claim 1, wherein said regeneration medium containing desorbate from the adsorption material flows into an initially cold heat-accumulator containing a heat storage material, disposed outside the adsorption material container, to transfer sensible and latent heat to the heat storage material and thereby heat the latter, cooled gaseous regeneration material from the heat-accumulator is heated in said first heat exchanger and returned to said adsorption material, passage of the regeneration medium to the adsorption medium continues until substantial cooling of the regeneration medium by the adsorption medium does not occur and the uncooled, hot regeneration medium flowing to the heat-accumulator heats the storage material by transferring essentially sensible heat, the cooled regeneration medium from the heat-accumulator is conducted without further heating as previously, to the absorption material which it cools, the thus heated regeneration medium is returned to the heat accumulator for further transfer of heat thereto; the heat stored in the heat accumulator effects at least the first heating of the adsorption material for initiating the next desorption by passing the regeneration medium through the heat accumulator containing stored heat prior to contact with the adsorption medium.

Claim 10

Method according to claim 8, wherein the heat capacity of the heat accumulator is at least equal to the heat capacity of the remaining masses in the desorption circuit.

Claim 11

Method according to claim 8, or claim 9, wherein during the desorption phase the gaseous regeneration medium which leaves the adsorption material container together with the expelled desorbate, is cooled in a condenser in the second heat exchanger which is arranged between the adsorption material container, and the heat accumulator and wherein condensate formed in the condenser and the heat accumulator is discharged therefrom.

Claim 12

Method according to claim 1, wherein a heat accumulator is arranged in the desorption circuit before the first heat exchanger.

Claim 13

Method according to claim 11, wherein the heat accumulator is constructed as a container with a poured-on layer which essentially forms the heat storage substance.

Claim 14

Method according to claim 11, or claim 12, wherein a condenser of the second heat exchanger is arranged between the adsorption material container and the heat accumulator.

Claim 15

Method according to claim 11, or claim 12, wherein a by-pass which can be cut-off is provided parallel to the heat accumulator.

Claim 16

Method according to claim 11, or claim 12, wherein a by-pass which can be cut-off is provided parallel to the first heat exchanger.

Claim 17

Method according to claim 11, or claim 12, wherein a condenser of the second heat exchanger is arranged between the absorption material container and the heat accumulator, and wherein a by-pass which can be cut off, is provided parallel to said condenser.