Fluid distribution device for a gas-liquid contactor, gas-liquid contactor and method for adding a gas to a liquid

Patent metadata

Field	Value
Publication number	US-10486113-B2
Application number	US-201515533389-A
Country	US
Kind code	B2
Filing date	Dec 7, 2015
Priority date	Dec 8, 2014
Publication date	Nov 26, 2019
Grant date	Nov 26, 2019

Abstract

A fluid distribution device for a gas-liquid contactor the device having a first side, a second side and a plurality of through-holes extending from the first side to the second side, through which holes a first fluid can flow. The fluid distribution device further having an interior, which is delimited by the first side and the second side and which is sealed in a fluid-tight manner in relation to the through-holes, a plurality of openings, which connect the interior to the second side, and a fluid connection, through which a second fluid can be introduced into or evacuated from the interior. A gas-liquid contactor having a fluid distribution device of this type and to a method for adding a gas to a liquid is also disclosed.

First claim

The invention claimed is:

1. A method for adding a gas to a liquid, using a gas-liquid contactor having a housing in which a multiplicity of hollow fibers are disposed and a space that surrounds the hollow fibers is configured, the method comprising the following steps:
introducing a liquid to which gas is to be added into the space which surrounds the hollow fibers of the gas-liquid contactor,
introducing a gas into the hollow fibers of the gas-liquid contactor,
allowing the liquid to which gas is to be added and the gas to flow in the gas-liquid contactor, and
obtaining a liquid to which gas has been added,
wherein the liquid to which gas is to be added and the gas flow through the gas-liquid contactor in counter flow and
wherein the gas-liquid contactor comprises a fluid distribution device, wherein the fluid distribution device comprises a first side and a second side; a multiplicity of through bores which extend from the first side to the second side and through which the liquid to which gas is to be added flows; an interior space which is delimited by the first side and by the second side and which is designed to be fluid-tight in relation to the through bores; a multiplicity of openings which connect the interior space to the second side; and a fluid connector through which the gas is introduced into the interior space or discharged from the interior space.

2. The method as claimed in claim 1 , wherein a liquid pressure of the liquid to which gas is to be added is higher than a gas pressure of the gas, if and when the hollow fibers have a membrane having a porous hydrophobic material.

3. The method as claimed claim 1 , wherein a liquid pressure of the liquid to which gas is to be added is lower than a gas pressure of the gas, if and when the hollow fibers have a membrane having a pore-free and gas-permeable hydrophobic material.

4. The method as claimed in claim 1 , wherein the liquid to which gas is to be added is a liquid to be exposed to ozone, and in that the gas is an ozone-containing gas.

5. The method as claimed in claim 4 , wherein the ozone-containing gas which exits from the fluid connector from the gas-liquid contactor still comprises large quantities of non-utilized oxygen is so that it is an oxygen-containing gas, wherein the oxygen-containing gas is subject to an exhaust gas treatment comprising the following steps:
destroying residual quantities of ozone in the oxygen-containing gas;
if and when the oxygen-containing gas has a hydrocarbon concentration of more than 20 ppm: reducing the concentration of hydrocarbons in the oxygen-containing gas to less than 20 ppm;
de-humidifying the oxygen-containing gas;
increasing the oxygen concentration in the de-humidified oxygen-containing gas to at least 85 percent by volume;
transferring the gas that has been de-humidified and enriched with oxygen to an ozone generator where the gas is employed for generating ozone, such that an ozone-containing gas results again.

6. The method as claimed in claim 1 , wherein the first side and the second side of the fluid distribution device each have a circular-type base area.

7. The method as claimed in claim 1 , wherein the through bores of the fluid distribution device have a diameter which is larger than a diameter of the openings.

8. The method as claimed in claim 1 , wherein the fluid connector of the fluid distribution device is disposed on a lateral circumference of the fluid distribution device.

9. The method as claimed in claim 1 , wherein the gas-liquid contactor extends along a direction of longitudinal extent, from a first end to a second end, and the fluid distribution device is disposed on the first end or on the second end of the gas-liquid contactor.

10. The method as claimed in claim 1 , wherein the gas-liquid contactor has two fluid distribution devices, wherein the one fluid distribution device is disposed on the first end and the other fluid distribution device is disposed on the second end.

11. The method as claimed in claim 1 , wherein two flanges which are in each case disposed on a side of the fluid distribution device that in the direction of longitudinal extent of the gas-liquid contactor is outboard and which serve for connecting the gas-fluid contactor to a line system.

12. The method as claimed in claim 1 , wherein the fluid distribution device is disposed in such a manner that the through bores of the fluid distribution device are in fluid communication with the space that surrounds the hollow fibers, and in that the openings of the fluid distribution device are in fluid communication with an interior region of the hollow fibers.

13. The method as claimed in claim 1 , wherein the hollow fibers have a membrane having a porous hydrophobic material.

14. The method as claimed in claim 1 , wherein the hollow fibers ( 3 ) have a membrane having a pore-free and gas-permeable hydrophobic material.

Assignees

• Univ Berlin Tech

Inventors

• Sabelfeld Marina
• Geissen Sven-Uwe

Classifications

• C02F1/44

  by dialysis, osmosis or reverse osmosis {(general membrane separation processes B01D61/00, membrane modules B01D63/00, electrodialysis C02F1/4693, combination of membrane modules and bioreactors C02F3/1268)} · CPC title

• B01D2325/027

  Nonporous membranes · CPC title

• C02F1/78

  with ozone {(C02F1/4672 takes precedence)} · CPC title

• C02F2303/16

  Regeneration of sorbents, filters · CPC title

• B01F5/0456

  Operations & Transport · mapped topic