COMPOSITE MEMBRANE COMPRISING HIGHLY PERMEABLE GUTTER LAYER AND METHOD FOR PREPARING SAME
20230271144 · 2023-08-31
Assignee
Inventors
- Su Young MOON (Daejeon, KR)
- Jong Myeong LEE (Daejeon, KR)
- Bong Jun Chang (Daejeon, KR)
- Chang In Kong (Daejeon, KR)
- Jae-Hyeok LEE (Daejeon, KR)
Cpc classification
B01D71/44
PERFORMING OPERATIONS; TRANSPORTING
B01D69/02
PERFORMING OPERATIONS; TRANSPORTING
B01D53/228
PERFORMING OPERATIONS; TRANSPORTING
B01D65/08
PERFORMING OPERATIONS; TRANSPORTING
B01D71/64
PERFORMING OPERATIONS; TRANSPORTING
B01D71/70
PERFORMING OPERATIONS; TRANSPORTING
B01D69/12
PERFORMING OPERATIONS; TRANSPORTING
B01D69/10
PERFORMING OPERATIONS; TRANSPORTING
B01D67/0002
PERFORMING OPERATIONS; TRANSPORTING
International classification
B01D69/12
PERFORMING OPERATIONS; TRANSPORTING
B01D69/10
PERFORMING OPERATIONS; TRANSPORTING
B01D65/08
PERFORMING OPERATIONS; TRANSPORTING
B01D71/44
PERFORMING OPERATIONS; TRANSPORTING
B01D71/70
PERFORMING OPERATIONS; TRANSPORTING
Abstract
The present disclosure relates to a composite membrane in which a rubbery polymer is introduced into a gutter layer to suppress the physical aging of the highly permeable composite membrane, and more particularly, to a composite membrane comprising a porous support layer; a gutter layer on the porous support layer; and an active layer on the gutter layer, wherein the gutter layer comprises a blend of poly(l-trimethlsilyl-l-propyne) (PTMSP) and a rubbery polymer and a method for preparing the same. The composite membrane according to the present disclosure has high permeation performance and a remarkable decline in physical aging leading to a decrease in permeability over time and thus has very high industrial applicability.
Claims
1. A composite membrane, comprising: a porous support layer; a gutter layer on the porous support layer; and an active layer on the gutter layer, wherein the gutter layer comprises a blend of poly(l-trimethlsilyl-l-propyne) (PTMSP) and a rubbery polymer.
2. The composite membrane according to claim 1, wherein the porous support layer is at least one polymer selected from polysulfone, polyethersulfone, polyetherethersulfone, polyphenylsulfone, polyacrylonitrile, polyetherimide, polyimide, polyamide, polyimide-amide, polyethylene, polyethyleneterephthalate, polyetherketone, polyetheretherketone, polyurethane, nylon and polyvinylidenefluoride.
3. The composite membrane according to claim 1, wherein the active layer is at least one polymer selected from acetylated methyl cellulose, polymers of intrinsic microporosity, thermally rearranged polymers and perfluoropolymers.
4. The composite membrane according to claim 1, wherein the rubbery polymer is at least one polymer selected from polydimethlysiloxane (PDMS), silicone-based rubber, polybutadiene, nitrile rubber, acrylic rubber, butyl rubber, polyisoprene and poly(styrene-co-butadiene).
5. The composite membrane according to claim 1, wherein a mix ratio of the poly(l-trimethlsilyl-l-propyne) (PTMSP) and the rubbery polymer in the polymer blend ranges from 9:1 to 5:5 by weight.
6. A method for preparing a composite membrane, comprising: forming a porous support layer; forming a gutter layer of a blend of poly(l-trimethlsilyl-l-propyne) (PTMSP) and rubbery polymer on the porous support layer; and forming an active layer on the gutter layer.
7. The method for preparing a composite membrane according to claim 6, wherein a mix ratio of the poly(l-trimethlsilyl-l-propyne) (PTMSP) and the rubbery polymer in the polymer blend ranges from 9:1 to 5:5 by weight.
8. The method for preparing a composite membrane according to claim 6, wherein the step of forming the gutter layer comprises preparing a mixed solution of the poly(l-trimethlsilyl-l-propyne) (PTMSP) and the rubbery polymer using an organic solvent and forming a film on water by water casting.
9. The method for preparing a composite membrane according to claim 8, wherein the organic solvent in the step of forming the gutter layer is at least one selected from chloroform, dipropylamine, isobutanol, cyclohexene, butanol, isovaleric acid, ethylether, isoamyl alcohol, ethylacetate, pentanol, 2-pentanone, hexanol, heptanol, acetic anhydride, pentyl acetate, octanol, cyclohexane, 2-hexanone, n-butyronitrile, diethylcarbonate, cyclohexanol, heptaldehyde, t-butyl chloride, benzyl alcohol, nitromethane, diisobutyl ketone, aniline and acetophenone.
10. The method for preparing a composite membrane according to claim 8, wherein the mixed solution in the step of forming the gutter layer comprises the poly(l-trimethlsilyl-l-propyne) (PTMSP) and the rubbery polymer in an amount ranging from 0.01 to 10 weight %.
Description
DESCRIPTION OF DRAWINGS
[0016]
[0017]
[0018]
BEST MODE
[0019] Hereinafter, the present disclosure will be described in detail. It should be understood that the terms or words used in the specification and the appended claims should not be construed as being limited to general and dictionary meanings, but rather interpreted based on the meanings and concepts corresponding to the technical aspects of the present disclosure on the basis of the principle that the inventor is allowed to define the terms appropriately for the best explanation.
[0020] To solve the above-described problem, the present disclosure provides a composite membrane comprising a porous support layer; a gutter layer on the porous support layer; and an active layer on the gutter layer, wherein the gutter layer comprises a blend of poly(l-trimethlsilyl-l-propyne) (PTMSP) and a rubbery polymer.
[0021] According to an embodiment of the present disclosure, the porous support layer may be at least one polymer selected from polysulfone, polyethersulfone, polyetherethersulfone, polyphenylsulfone, polyacrylonitrile, polyetherimide, polyimide, polyamide, polyimide-amide, polyethylene, polyethyleneterephthalate, polyetherketone, polyetheretherketone, polyurethane, nylon and polyvinylidenefluoride.
[0022] According to an embodiment of the present disclosure, the active layer may be at least one polymer selected from acetylated methyl cellulose, polymers of intrinsic microporosity, thermally rearranged polymers and perfluoropolymers, including the above-described polymers. Additionally, polymers used as the commonly used materials of gas separation membranes may be used without limitation.
[0023] In this instance, the polymers of intrinsic microporosity may include any material widely used in sensors and gas separation membranes, for example, polymers having microporosity in molecules in chemical structures.
[0024] Additionally, a typical example of the thermally rearranged polymers may include those induced from polyimides comprising at least one functional group of a hydroxyl group or an amine group or copolymers comprising the polyimides through a thermal treatment process, and specifically, may be at least one selected from the group consisting of polybenzoxazole induced from polyimide having a hydroxyl group, polypyrrolone induced from polyimide having an amine group, polybenzoxazole-pyrrolone copolymers induced from the polyimides having hydroxyl and amine groups, polypyrrolone-imide copolymers induced from the copolymers comprising the polyimides and/or polybenzoxazole-imide copolymers.
[0025] The thermally rearranged polymers according to the present disclosure may be induced from the above-described polyimides or the copolymers comprising the polyimides through the thermal treatment process. Specifically, the predetermined thermal treatment process may convert the polyimide having a hydroxyl group to polybenzoxazole, the polyimide having an amine group to polypyrrolone and the polyimides having a hydroxyl group and an amine group to polybenzoxazole-pyrrolone copolymers. Additionally, the copolymers comprising the polyimides may be converted to polypyrrolone-imide copolymers and/or polybenzoxazole-imide copolymers by the predetermined thermal treatment process.
[0026] In this instance, the thermally rearranged polymers induced through the thermal treatment process are subjected to a morphology change such as a significant increase in fractional free volume (FFV) and an increase in d-spacing with the decreasing density and the increasing size of micropores by thermal conversion reaction, thereby greatly increasing the gas permeability and improving the chemical resistance and heat resistance of the polymer.
[0027] According to an embodiment of the present disclosure, the thickness of the gutter layer may range from 10 to 10,000 nm, and more preferably 50 to 1,000 nm. When the thickness of the gutter layer exceeds the corresponding thickness range, permeability reduces, and when the thickness of the gutter layer is less than the corresponding thickness range, low mechanical properties make it impossible to use as the gutter layer.
[0028] According to an embodiment of the present disclosure, the rubbery polymer may be at least one polymer selected from polydimethlysiloxane (PDMS), silicone-based rubber, polybutadiene, nitrile rubber, acrylic rubber, butyl rubber, polyisoprene and poly(styrene-co-butadiene).
[0029] According to an embodiment of the present disclosure, a mix ratio of the poly(l-trimethlsilyl-l-propyne) (PTMSP) and the rubbery polymer in the polymer blend may range from 9:1 to 5:5 by weight.
[0030] Additionally, to solve the above-described problem, the present disclosure provides a method for preparing the composite membrane including forming the porous support layer; forming the gutter layer comprising the blend of the poly(l-trimethlsilyl-l-propyne) (PTMSP) and the rubbery polymer on the porous support layer; and forming the active layer on the gutter layer.
[0031] According to an embodiment of the present disclosure, the mix ratio of the poly(l-trimethlsilyl-l-propyne) (PTMSP) and the rubbery polymer in the polymer blend may range from 9:1 to 5:5 by weight.
[0032] According to an embodiment of the present disclosure, the step of forming the gutter layer preferably includes preparing a mixed solution of the poly(l-trimethlsilyl-l-propyne) (PTMSP) and the rubbery polymer using an organic solvent and forming a film on water by water casting.
[0033] According to an embodiment of the present disclosure, the organic solvent in the step of forming the gutter layer preferably includes at least one selected from chloroform, dipropylamine, isobutanol, cyclohexene, butanol, isovaleric acid, ethylether, isoamyl alcohol, ethylacetate, pentanol, 2-pentanone, hexanol, heptanol, acetic anhydride, pentyl acetate, octanol, cyclohexane, 2-hexanone, n-butyronitrile, diethylcarbonate, cyclohexanol, heptaldehyde, t-butyl chloride, benzyl alcohol, nitromethane, diisobutyl ketone, aniline and acetophenone.
[0034] According to an embodiment of the present disclosure, the mixed solution in the step of forming the gutter layer may comprise the poly(l-trimethlsilyl-l-propyne) (PTMSP) and the rubbery polymer in an amount ranging from 0.01 to 10 weight %, and more preferably 0.1 to 2 weight %. At high concentrations above the above-described range, the gutter layer is thick and reduces in permeability, and at low concentrations less than the above-described range, the prepared gutter layer is too thin and has low mechanical properties, and thus cannot be used as the gutter layer.
[0035] According to an embodiment of the present disclosure, the thickness of the gutter layer may range from 10 to 10,000 nm, and more preferably 20 to 1,000 nm. When the thickness of the gutter layer exceeds the corresponding thickness range, permeability reduces, and when the thickness of the gutter layer is less than the corresponding thickness range, low mechanical properties makes it impossible to use as the gutter layer.
[0036] Hereinafter, an embodiment and an example of the present disclosure will be described in sufficient detail with reference to an exemplary embodiment of the present disclosure together with the accompanying drawings to enable those skilled in the art to easily practice the invention. In particular, the technical aspect of the present disclosure and the essential elements and operations are not limited thereto. Additionally, the present disclosure may be embodied by many other types of equipment, and is not limited to the embodiments and examples described herein.
<Preparation Example> Preparation of a Gutter Layer Polymer Blend Solution
[0037] The polymer blend that forms the gutter layer according to an embodiment of the present disclosure is prepared by the following method.
[0038] Poly(l-trimethlsilyl-l-propyne) (PTMSP) (GELEST, INC) and polydimethlysiloxane (PDMS) (product name: Sylgard 184 Elastomer Base, available from Dow Corning Corporation) are dissolved in a chloroform solvent at a weight ratio of the PDMS to the PTMSP of 0 to 100, and the polymer concentration is adjusted to 0.1 to 2 weight % by adding the chloroform solvent to the prepared solution.
<Example A> Preparation of a Composite Membrane Comprising a Gutter Layer
[0039] The gutter layer polymer blend solution prepared according to the preparation example according to an embodiment of the present disclosure is dripping on water in an amount of 0.5 microliters using a micropipette in a water tank filled with water at the temperature of the water tank adjusted to 25° C. to prepare a film, and the prepared film on the water is placed on a porous polysulfone (PSF) support (pore diameter: 10 to 20 nm, Toray Chemical Korea Inc.) by lifting up the support from the water to prepare a composite membrane. Subsequently, the prepared composite membrane is left to dry naturally to remove water. In this instance, the composition used when preparing the gutter layer of the prepared composite membrane and the thickness of the gutter layer are summarized in the following table 1.
TABLE-US-00001 TABLE 1 Composition of gutter Polymer Gutter layer layer (Weight ratio) concentration (%) thickness (nm) Comparative PTMSP 0.75 20 example Example 1 9:1 0.75 24 Example 2 8;2 0.75 25 Example 3 7:3 0.75 27 Example 4 6:4 0.75 28 Example 5-1 5:5 0.75 22 Example 5-2 5:5 0.1 11 Example 5-3 5:5 0.25 13 Example 5-4 5:5 0.5 17 Example 5-5 5:5 1 55 Example 5-6 5:5 2 200
[0040] To compare aging in the composite membrane, the present disclosure forms the single thin film on water using water casting and places it on the porous polysulfone (PSF) support to prepare the composite membrane. To this end, the PTMSP and the PDMS are dissolved in the chloroform solvent at the weight ratio of the PDMS to the PTMSP of 0 to 1 to prepare the solution. In this instance, the gutter layer is prepared by adjusting the total polymer content in the solution to the concentration of 0.1 to 2 weight % relative to the chloroform solvent.
[0041] In this instance, when the mix ratio of the PDMS to the PTMSP is larger than 5:5, due to the high flowability of the PDMS, it is impossible to form the film having the optimal mechanical strength on water, and it is difficult to stably attach the film to the porous support. Additionally, when the mix ratio of the PDMS to the PTMSP is less than 9:1, the formed film is very thin, so it is impossible to obtain the film having the optimal mechanical strength.
[0042] The following table 2 summaries a comparison of initial CO.sub.2 permeation performance, permeation performance after aging and CO.sub.2/N.sub.2 selectivity (polymer concentration=0.75 weight %) of the composite membrane as a function of the mix ratio of the PDMS. In all conditions, CO.sub.2 permeability after 24 hours-aging is lower than CO.sub.2 permeability before aging, but compared to a composite membrane made of PTMSP alone, at least twice improvement in permeability after aging is found. Additionally, a slight increase in selectivity is observed as the effect of the aging.
TABLE-US-00002 TABLE 2 Permeability and Permeability and selectivity selectivity after before aging 24 hours-aging PTMSP:PDMS CO.sub.2 CO.sub.2/N.sub.2 CO.sub.2 CO.sub.2/N.sub.2 (Weight ratio) GPU — GPU — Comparative PTMSP 42,100 3.9 8,750 4.2 example Example 1 9:1 37,300 3.8 19,240 4.3 Example 2 8:2 36,290 3.9 20,050 4.4 Example 3 7:3 38,230 3.8 21,000 4.2 Example 4 6:4 41,000 3.7 22,300 4.2 Example 5 5:5 38,800 3.9 25,600 4.5
<Analysis Example> Gas Permeability and Anti-Aging Effect Analysis of a Composite Membrane
[0043] The gas permeability test of the composite membrane prepared according to an embodiment of the present disclosure is performed by attaching the prepared composite membrane to a thick circular PET film having a hole having an inner diameter of 2 cm, and an outer diameter of 7 cm and a thickness of 100 μm to prepare a composite membrane disc for permeability measurement.
[0044] To get ready to measure permeability, a lower plate and a circular upper plate made of stainless steel are placed with a dead-end gas permeable cell having a rubber gasket interposed between them and tightly fixed to prevent gas leaks.
[0045] The gas permeation is measured using pure CO.sub.2 and N.sub.2 gas. Each gas is fed into the permeable cell under the pressure of 2 bars, and the gas flow rate of the gas flowing through the prepared composite membrane disc is measured using a bubble flow meter.
[0046] The permeability and GPU are calculated using the measured permeation flow rate through the following equations.
Permeability=Q (cm{circumflex over ( )}3/sec)/(A (cm{circumflex over ( )}2)*P (cmHg)) (Equation 1)
1 [GPU]=1*[10{circumflex over ( )}(−6)*Q (cm{circumflex over ( )}3/sec)/(A (cm{circumflex over ( )}2)*P (cmHg))] (Equation 2)
In this instance, Q is the permeation flow rate, A is the permeation area of the composite membrane, and P is the pressure of compressed feed gas.
[0047]
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[0049]