IP Library Granted Patent US 12,566,160
Granted Patent B2
US 12,566,160 · App. 18/254,054 · Granted Mar 3, 2026

Pillar structures

Inventors: Jeff Op De Beeck (Mariakerke, BE); Bo Claerebout (Kortrijk, BE); Paul Jacobs (Lokeren, BE)
Assignee: PharmaFluidics NV
G01N30/6095
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Quick Facts
Patent No.
US 12,566,160
App. No.
18/254,054
Granted
Mar 3, 2026
Kind
B2
Abstract

A chemical reactor implemented on a substrate is described. The chemical reactor includes at least one channel for transporting a liquid and/or gas during operation of the chemical reactor. The channel comprises pillar structures perpendicular to the bottom of the channel having a transverse section parallel to the bottom that is substantially rectangular and wherein the pillar structures are provided with a porous layer of substantially homogeneous thickness applied via electrochemical anodising.

Claims (26)

1 . A chemical reactor implemented on a substrate, the chemical reactor comprising:

at least one channel for transporting a fluid during operation of the chemical reactor

wherein the channel includes an ordered set of pillar structures perpendicular to the bottom of the channel,

wherein the pillar structures have;

a transverse section parallel to the bottom that is substantially rectangular,

a width perpendicular to an average flow direction of the fluid in the channel,

a length along the average flow direction of the fluid in the channel, and

a width-to-length ratio greater than 2 to 1, and

wherein the pillar structures are provided with a porous layer of substantially homogeneous thickness applied via electrochemical anodizing, and

wherein the pillar structures are positioned such that a position of a sub-channel between two pillar structures in the average flow direction from a row does not correspond to a position of a sub-channel between two pillar structures in a subsequent row.

2 . A chemical reactor according to claim 1 , wherein a thickness of the porous layer on an outside of the pillar structures varies no more than 10%, along the perimeter of the pillar structures.

3 . A chemical reactor according to claim 1 , wherein the pillar structures are microfabricated pillar structures.

4 . A chemical reactor according to claim 1 , wherein the pillar structures are microfabricated silicon-based pillar structures.

5 . A chemical reactor according to claim 1 , wherein the length is greater than two times the thickness of the porous layer on the non-porous core of the pillar structures.

6 . A chemical reactor according to claim 5 , wherein the length of the pillar structures is at least three times the thickness of the porous layer on the non-porous core of the pillar structures.

7 . A chemical reactor according to claim 1 , wherein the porous layer is formed by removing material on the basis of an electric current applied through the core of the pillars.

8 . A chemical reactor according to claim 1 , wherein the porous layer is formed by growing the porous layer conformably with an outer circumference of the pillars.

9 . A chemical reactor according to claim 8 , wherein the porous layer is grown at a fixed speed, a speed that is equal at all times at all points on the surface of the pillars, or a fixed speed that is equal at all times at all points on the surface of the pillars.

10 . A chemical reactor according to claim 1 , wherein the chemical reactor comprises a chromatographic column.

11 . A chemical reactor according to claim 1 , wherein the chemical reactor is a chromatography system.

12 . A chemical reactor according to claim 11 , wherein the chromatography system is a high-performance liquid chromatography system.

13 . A method for producing a chemical reactor implemented on a substrate, the method comprising:

providing a substrate having at least one channel for transporting a fluid during operation of the chemical reactor, wherein the channel comprises pillar structures which are perpendicular to the bottom of the channel and which have a transverse section parallel to the bottom which is substantially rectangular, the pillar structures having a width perpendicular to an average flow direction of the fluid in the channel, a length along the average flow direction of the fluid in the channel, and a width-to-length ratio greater than 2 to 1, the pillar structures positioned such that a position of a sub-channel between two pillar structures in the average flow direction from a row does not correspond to a position of a sub-channel between two pillar structures in a subsequent row; and

of generating a porous layer of substantially uniform thickness on the pillar structures by electrochemical anodizing.

14 . The method of claim 13 , wherein generating the porous layer by electrochemical anodizing includes removing material based on an electric current applied through a core of the pillar structures.

15 . The method of claim 14 , wherein the electric current is applied orthogonally to an outer sheath of the pillars.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 31, 2023
From: OP DE BEECK, JEFF; CLAEREBOUT, BO; JACOBS, PAUL
To: PHARMAFLUIDICS
Reel/Frame 064764/0384 →
MERGER Recorded Aug 31, 2023
From: PHARMAFLUIDICS NV
To: THERMO FISHER SCIENTIFIC BV
Reel/Frame 064789/0140 →
Priority Claims (1)
BE 2020/6008 · Dec 30, 2020 · national
Continuity (1)
Related Publication 20240003856A1 · Jan 4, 2024
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