PREPARATION METHOD FOR COMPOSITE POROUS STRUCTURE AND COMPOSITE POROUS STRUCTURE MADE THEREBY

Abstract

The present invention provides a preparation method for a composite porous structure, comprising the following steps: step (a): preparing a porous substrate having multiple pores, a first surface and a second surface; and step (b): continuously feeding a cooling fluid to contact the first surface and to flow continuously to the second surface through the pores of the porous substrate, and heating a coating material to multiple molten particles by a heat source and spraying the molten particles onto the second surface of the porous substrate, so as to form a coating layer having multiple micropores on the second surface of the porous substrate and obtain the composite porous structure formed. Besides, also provided is a composite porous structure prepared by the preparation method.

Claims

1. A preparation method for a composite porous structure, comprising the following steps: step (a): preparing a porous substrate having multiple pores, a first surface and a second surface opposite to the first surface; and step (b): continuously feeding a cooling fluid to contact the first surface and to flow continuously to the second surface through the pores of the porous substrate, and heating a coating material to multiple molten particles by a heat source and spraying the molten particles onto the second surface of the porous substrate, so as to form a coating layer having multiple micropores on the second surface of the porous substrate and obtain the composite porous structure; wherein the coating material is an organic polymer coating material or an inorganic coating material.

2. The preparation method as claimed in claim 1, wherein the temperature of the molten particles is higher than the temperature of the cooling fluid.

3. The preparation method as claimed in claim 2, wherein the heat source temperature of step (b) is between 100 C. and 10000 C.

4. The preparation method as claimed in claim 2, wherein the cooling fluid temperature of step (b) is between 5 C. and 60 C.

5. The preparation method as claimed in claim 1, wherein the step (a) comprises the following steps: step (a1): preparing the porous substrate; and step (a2): filling a liquid into the pores of the porous substrate.

6. The preparation method as claimed in claim 5, wherein the liquid is water, alcohols, ketones, or combinations thereof.

7. The preparation method as claimed in claim 1, wherein the material of the porous substrate is an organic polymer material, a ceramic material, or a metal material.

8. The preparation method as claimed in claim 7, wherein the organic polymer material includes polyethylene, polypropylene or polytetrafluoroethylene.

9. The preparation method as claimed in claim 1, wherein an average pore diameter of the multiple pores in the porous substrate is between 0.1 m and 50 m.

10. The preparation method as claimed in claim 1, wherein the ratio of the inflow volume to outflow volume of the cooling fluid is between 1:0.9 and 1:1.

11. The preparation method as claimed in claim 1, wherein the inorganic coating material is at least one selected from the group consisting of alkali metals, alkaline earth metals, silicates, aluminates, borates, titanates, phosphates, oxides, nitrides, oxynitrides, carbides, oxycarbides and halogen compounds; the organic coating material includes polyethylene, polypropylene or polytetrafluoroethylene.

12. A composite porous structure, which is prepared by the preparation method as claimed in claim 1, the composite porous structure comprising a porous substrate containing multiple pores and a coating layer having multiple micropores, the porous substrate having a first surface and a second surface opposite to the first surface, the coating layer disposed on the second surface of the porous substrate, and the coating layer containing an organic polymer coating material or an inorganic coating material.

13. The composite porous structure as claimed in claim 12, wherein the average pore size of the micropores is between 0.01 m and 5 m.

14. The composite porous structure as claimed in claim 12, wherein the porous coating layer has an average thickness of 5 m to 500 m.

15. The composite porous structure as claimed in claim 12, wherein the material of the porous substrate is an organic polymer material, a ceramic material, or a metal material.

16. The composite porous structure as claimed in claim 15, wherein the organic polymer material includes polyethylene, polypropylene or polytetrafluoroethylene.

17. The composite porous structure as claimed in claim 12, wherein the inorganic coating material is at least one selected from the group consisting of alkali metals, alkaline earth metals, silicates, aluminates, borates, titanates, phosphates, oxides, nitrides, oxynitrides, carbides, oxycarbides and halogen compounds; the organic coating material includes polyethylene, polypropylene or polytetrafluoroethylene.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0034] FIG. 1 is a schematic view of step (b) in the preparation method for a composite porous structure of Example 1.

[0035] FIG. 2 is a pore size distribution diagram of the micropores in the coating layer of the composite porous structure of Example 1.

[0036] FIG. 3 is a pore size distribution diagram of micropores in the coating layer of the composite porous structure of Example 2.

[0037] FIG. 4 is a pore size distribution diagram of micropores in the coating layer of the composite porous structure of a comparative example.

[0038] FIG. 5 to FIG. 7 are schematic perspective views of the porous substrate of the composite porous structure in accordance with the present invention.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

[0039] Hereinafter, the preferred embodiments of the present invention will be described by the following examples, and one skilled in the arts can easily realize the advantages and effects in accordance with the present invention. Various modifications and variations could be made in order to practice or apply the present invention without departing from the spirit and scope of the invention.

[0040] The method of preparing a composite porous structure of the present invention can be described in the following Example 1 and Example 2:

Example 1

[0041] First, referring now to FIG. 1, a hollow tubular porous substrate 10 in the step (a1) is prepared. The porous substrate 10 has a tube wall 101, an axial channel 102 and multiple pores 103. The axial channel 102 is formed in the tube wall 101, and the pores 103 are concavely formed on the tube wall 101. The tube wall 101 has a first surface 1011 (i.e., an inner wall surface) and a second surface 1012 (i.e., an outer wall surface) opposite to the first surface 1011. The tube wall 101 has a thickness of 2.5 mm, a length of 300 mm, an inner diameter of 29.5 mm and an outer diameter of 30 mm. The porous substrate 10 is made of stainless steel and has an average diameter of 3 m. Subsequently, in the step (a2), the porous substrate 10 is immersed in a tank filled with deionized water to allow the multiple pores 103 in the porous substrate 10 to be full with deionized water.

[0042] Next, referring to FIG. 1, the cooling fluid 30 at 25 C. is fed into the axial channel 102 at a flow rate of 3 L/min in the step (b), so that the cooling fluid 30 continuously contacts the first surface 1011 and maintains the overall temperature of the porous substrate 10. A portion of the cooling fluid 30 flows through the pores 103 to the second surface 1012. At the same time, by way of a heat source of 8000 C. generated by a plasma, the alumina coating materials are heated to multiple molten particles 201 at a temperature of about 500 C. in the atmosphere, and the molten particles 201 are sprayed onto the second surface 1012 of the porous substrate 10 with a spraying distance of 10 cm between the heat source and the second surface 1012, so as to obtain a coating layer 20 having multiple micropores. The ratio of the inflow to outflow volume of the cooling fluid 30 is 1:0.99, indicating that the deionized water of the cooling fluid 30 is continuously filled in the multiple pores 103 of the porous substrate 10. In this step, the sprayed molten particles 201 are stacked on the second surface 1012. The deionized water in the multiple pores 103 can be vaporized into steam through the heat (i.e., a temperature greater than 100 C.) of the molten particles 201, so that steam can penetrate through the thin layer to form micropores. Besides, in the step, the molten particles 201 can be continuously cooled and solidified by the cooling fluid 30 continuously flowing in the axial channel 102, and thereby a coating layer is formed on the second surface 1012 to obtain a composite porous structure 1. Herein, the average thickness of the coating layer 20 is 28 m after repeating the above steps three times in synchronization with step (b).

[0043] The pore size distribution of the micropores of the porous coating layer 20 of the composite porous structure 1 is shown in FIG. 2. It can be seen that the pore size distribution of the micropores is very narrow and the pore size has a high uniformity. The porous coating layer 20 of the composite porous structure 1 is measured by a pore size analyzer, PMI CFP-1500A. The average pore diameter of the micropores is about 0.5 m, and the micropores having pore diameters larger than 0.55 m take up 13.4% of the total micropores.

[0044] In addition, the blocking efficiency of the composite porous structure 1 is measured by the method as follows. (1) polystyrene (PS) standard particles (0.45 m or 0.2 m) were formulated into aqueous solutions of different concentrations, and the turbidity was measured by a turbidimeter to make a calibration curve that the concentration and turbidity have a linear relationship; (2) a solution of 100 nephelometric turbidity units (NTU) containing 0.45 m polystyrene standard particles was prepared. The solution was filtered through the composite porous structure 1 before the polystyrene standard particles formed a filter cake on the coating surface 1012. The turbidity of the filtrate obtained after the filtration is 1 NTU, indicating that the composite porous structure 1 has a blocking efficiency of 99% for the 0.45 m polystyrene standard particles

Example 2

[0045] The preparation method of Example 2 is similar to the preparation method of Example 1, the difference lies in that Example 2 repeats step (b) 5 times. The composite porous structure prepared in accordance with the preparation method of Example 2 comprises a porous substrate and a coating layer having multiple micropores formed on the second surface of the porous substrate. The average thickness of the coating layer is 48 m and the average pore diameter of the micropores in the coating layer is about 0.32 m. The pore size distribution thereof is shown in FIG. 3, wherein the micropores having pore diameters larger than 0.35 m take up only 2.7% of the total micropores. In addition, the composite porous structure in accordance with the example has a blocking efficiency of 99% for the 0.2 m polystyrene standard particles

Comparative Example 1

[0046] The preparation method of Comparative Example 1 is similar to the preparation method of Example 1, the difference lies in that, when the molten particles are sprayed onto the second surface of the porous substrate, no cooling fluid containing deionized water is continuously fed to contact the first surface of the porous substrate at the same time. In fact, the first surface of the porous substrate just statically contacts deionized water. The composite porous structure prepared in accordance with the preparation method of Comparative Example 1 contains a porous substrate and a coating layer having multiple micropores formed on the second surface of the porous substrate, wherein the average thickness of the coating layer is 25 m and the average pore diameter of the micropores in the coating layer is about 0.33 m. The pore sizes of these micropores in the composite porous structure are different. The pore size distribution is shown in FIG. 4, wherein the micropores having pore diameters larger than 0.35 m take up 43.6% of the total micropores, and the micropores having pore diameters larger than 0.55 m even take up 23% of the total micropores. Therefore, the composite porous structure in accordance with the comparative example has a blocking efficiency of only 83% for the 0.45 m polystyrene standard particles. Referring to FIG. 5 to FIG. 7, the composite porous structure 1 of Example 1 can use the hollow tube 10 shown in FIG. 5 as the porous substrate 10. In addition, depending on the needs of different applications, the hollow column 10 shown in FIG. 6 or the hollow column 10 shown in FIG. 7 can be used as, but not limited to, a porous substrate without affecting the composite porous structure of the present invention.

[0047] In conclusion, the method for preparing the composite porous structure has a simple process, a short preparation time and a lower cost. Further, the method can adopt more various materials in combination to increase the application potential, and use no toxic organic reagents to meet the requirements of protecting environment. Besides, the composite porous structure obtained by the method of the present invention has a high uniformity of pore size and therefore has a good blocking efficiency.

[0048] Although the aforementioned description has described the numerous features, advantages, compositions and feature details of the present invention, it is just an exemplary description. The details of changes made in accordance with the invention in the range of the general meaning of the patent scope, especially the changes in shape, size, and arrangement, are still within the scope of the invention.