Counterflow adsorption filter column for water treatment

Patent metadata

Field	Value
Publication number	US-11198624-B2
Application number	US-201815994569-A
Country	US
Kind code	B2
Filing date	May 31, 2018
Priority date	Mar 15, 2013
Publication date	Dec 14, 2021
Grant date	Dec 14, 2021

Abstract

The present invention relates to a method for treatment and/or purification of water, in particular wastewater or drinking water, preferably for the adsorptive removal of inorganically or organically-based, impurities, such as trace substances and/or micropollutants, wherein, in a counterflow filter device, e.g. a counterflow adsorption filter column, the water that is to be treated and/or that is to be purified firstly, and, secondly, an, in particular particulate, adsorption material are conducted in a counterflow direction. In particular, a procedure is followed in such a manner that the water to be treated and/or purified is passed through a bed of the adsorption material present in the counterflow filter device for the adsorptive removal of impurities and the bed is exchanged and regenerated by preferably continuous removal and supply of the adsorption material in counterflow to the water that is to be treated and/or that is to be purified.

First claim

The invention claimed is:

1. A method for treatment of water for the purpose of adsorptive removal of inorganic-based or organic-based contaminants comprising passing water to be treated through a countercurrent filter apparatus,
wherein the countercurrent filter apparatus is provided for uptake, storage, and release of a particulate adsorption material,
wherein the countercurrent filter apparatus comprises at least one housing, said housing comprising at least one countercurrent zone, a water entry region, and a water exit region,
wherein the at least one countercurrent zone of the countercurrent filter apparatus has a round cross section a, having a cross-sectional area,
wherein the water entry region has a round cross section b, having a cross-sectional area,
wherein the water exit region has a round cross section c, having a cross-sectional area,
wherein the cross-sectional area a of the at least one countercurrent zone is less than the cross-sectional area b of the water entry region and less than the cross-sectional area c of the water exit region, and
wherein the cross-sectional area b of the water entry region and the cross-sectional area c of the water exit region are of equal size,
wherein, in the countercurrent filter apparatus, the water to be treated, on the one hand, and the particulate adsorption material, on the other hand, are conducted in countercurrent to one another in such a way that the water to be treated is passed through a bed of the adsorption material present in the countercurrent filter apparatus for adsorptive removal of the contaminants and the bed is exchanged and regenerated by continuous removal and supply of the adsorption material in countercurrent to the water to be treated,
wherein the adsorption material is introduced continuously into the countercurrent filter apparatus and wherein the adsorption material is removed continuously from the countercurrent filter apparatus,
wherein the adsorption material removed from the countercurrent filter apparatus is sent and subjected to a continuous thermal regeneration operation with desorption of the contaminants, wherein the regenerated adsorption material is introduced continuously back into the countercurrent filter apparatus,
wherein the water to be treated is introduced continuously into the countercurrent filter apparatus in the water entry region and wherein the water treated is removed continuously from the countercurrent filter apparatus in the water exit region,
wherein the water to be treated, on the one hand, and the adsorption material, on the other hand, in the countercurrent filter apparatus have an opposing direction of flow and are contacted with one another in flows countercurrent to one another in the countercurrent filter apparatus,
wherein the adsorption material is formed from spherical activated carbon,
wherein the adsorption material has an abrasion resistance of at least 90%, and
wherein the adsorption material has a bulk density in the range from 250 to 700 g/L.

2. The method as claimed in claim 1 ,
wherein the at least one countercurrent zone, in terms of flow, is disposed between the water entry region and the water exit region, and
wherein the water entry region has at least one adsorption material outlet and wherein the water exit region has at least one adsorption material inlet.

3. The method as claimed in claim 1 ,
wherein the at least one countercurrent zone has a diameter D 1 , and a height H 1 , and the water entry region has a diameter D 2 and the water exit region has a diameter D 3 ,
wherein the at least one countercurrent zone, in terms of flow, is disposed between the water entry region and the water exit region and wherein the at least one countercurrent zone is disposed downstream of the water entry region and upstream of the water exit region, based on the water's direction of flow,
wherein the water entry region comprises at least one water feed and at least one adsorption material outlet and wherein the water exit region comprises at least one water drain and least one adsorption material inlet,
wherein the ratio of the diameter D 1 of the at least one countercurrent zone to the diameter D 2 of the water entry region is at least 1:1.1 and wherein the ratio of the diameter D 1 of the at least one countercurrent zone to the diameter D 3 of the water exit region is at least 1:1.1; and

wherein the countercurrent filter apparatus has a first transition region and a second transition region,
wherein the first transition region, in terms of flow, is disposed between the water entry region and the at least one countercurrent zone and wherein the first transition region is disposed downstream of the water entry region and upstream of the at least one countercurrent zone, based on the water's direction of flow,
wherein the first transition region is conical and, proceeding from the water entry region having the diameter D 2 , narrows in the direction of the at least one countercurrent zone having the diameter D 1 , and
wherein the second transition region, in terms of flow, is disposed between the water exit region and the at least one countercurrent zone and wherein the second transition region is disposed downstream of the at least one countercurrent zone and upstream of the water exit region, based on the water's direction of flow,
wherein the second transition region is conical and, proceeding from the water exit region having the diameter D 3 , narrows in the direction of the at least one countercurrent zone having the diameter D 1 .

4. The method as claimed in claim 3 ,
wherein the ratio of the height H 1 to the diameter D 1 of the at least one countercurrent zone of the countercurrent filter apparatus is at least 1.5:1.

5. The method as claimed in claim 1 ,
wherein water to be treated and purified which is introduced into the countercurrent filter apparatus is conducted through the at least one countercurrent zone of the countercurrent filter apparatus disposed downstream of the water entry region of the countercurrent filter apparatus, based on the water's direction of flow.

6. The method as claimed in claim 1 ,
wherein a filtering rate, calculated as the quotient of volume flow rate [m 3 /h] and cross-sectional area [m 2 ] and based on the water to be treated, of at least 10 m/h is established in the at least one countercurrent zone of the countercurrent filter apparatus.

7. The method as claimed in claim 1 ,
wherein the adsorption material is fed continuously to the countercurrent filter apparatus and wherein the adsorption material is conducted continuously through the countercurrent filter apparatus and wherein the adsorption material is withdrawn continuously from the countercurrent filter apparatus;
wherein the adsorption material introduced into the countercurrent filter apparatus is conducted through the at least one countercurrent zone of the countercurrent filter apparatus disposed downstream of the water exit region of the countercurrent filter apparatus, based on the adsorption material's direction of flow;
wherein the adsorption material is present in the countercurrent filter apparatus in the form of a loose bed; and
wherein the adsorption material, after passing through the at least one countercurrent zone of the countercurrent filter apparatus, is removed from the countercurrent filter apparatus in the water entry region disposed downstream of the water exit region of the countercurrent filter apparatus and downstream of the at least one countercurrent zone of the countercurrent filter apparatus, based on the adsorption material's direction of flow.

8. The method as claimed in claim 1 ,
wherein, in the use state, in the at least one countercurrent zone of the countercurren

Assignees

• Bluecher Gmbh

Inventors

• Schönfeld Raik
• Raiser Jan

Classifications

• C02F2301/04

  Flow arrangements · CPC title

• C02F1/42

  by ion-exchange (ion-exchange in general B01J) · CPC title

• B01D15/02

  with moving adsorbents · CPC title

• C02F1/283

  using coal, charred products, or inorganic mixtures containing them · CPC title

• C02F2303/16

  Regeneration of sorbents, filters · CPC title