AIR PERMEABLE FILTER MATERIAL COMPRISING A POLYMER AEROGEL
20230201800 · 2023-06-29
Assignee
Inventors
- Marisa SNAPP-LEO (Spence, MA, US)
- Lawino KAGUMBA (Spencer, MA, US)
- Garrett POE (Spencer, MA, US)
- Timothy BURBEY (Spencer, MA, US)
Cpc classification
C08J2205/044
CHEMISTRY; METALLURGY
B01J20/262
PERFORMING OPERATIONS; TRANSPORTING
B01D39/1692
PERFORMING OPERATIONS; TRANSPORTING
B01D39/04
PERFORMING OPERATIONS; TRANSPORTING
C08J2205/026
CHEMISTRY; METALLURGY
B01J20/3064
PERFORMING OPERATIONS; TRANSPORTING
C08J9/286
CHEMISTRY; METALLURGY
A62B23/025
HUMAN NECESSITIES
B01D2239/0681
PERFORMING OPERATIONS; TRANSPORTING
B01J20/28028
PERFORMING OPERATIONS; TRANSPORTING
B01J20/2805
PERFORMING OPERATIONS; TRANSPORTING
B01J20/28083
PERFORMING OPERATIONS; TRANSPORTING
A41D31/14
HUMAN NECESSITIES
C08G73/1071
CHEMISTRY; METALLURGY
A41D13/11
HUMAN NECESSITIES
B01J20/28035
PERFORMING OPERATIONS; TRANSPORTING
A62B18/084
HUMAN NECESSITIES
B01J20/3085
PERFORMING OPERATIONS; TRANSPORTING
B01D2239/10
PERFORMING OPERATIONS; TRANSPORTING
C08J2379/08
CHEMISTRY; METALLURGY
B01J20/28085
PERFORMING OPERATIONS; TRANSPORTING
C08J2205/05
CHEMISTRY; METALLURGY
B01D2239/0442
PERFORMING OPERATIONS; TRANSPORTING
C08G73/1042
CHEMISTRY; METALLURGY
A61L2209/22
HUMAN NECESSITIES
A61L9/014
HUMAN NECESSITIES
International classification
B01J20/26
PERFORMING OPERATIONS; TRANSPORTING
C08G73/10
CHEMISTRY; METALLURGY
C08J9/28
CHEMISTRY; METALLURGY
B01J20/28
PERFORMING OPERATIONS; TRANSPORTING
B01J20/30
PERFORMING OPERATIONS; TRANSPORTING
A61L9/014
HUMAN NECESSITIES
A62B18/08
HUMAN NECESSITIES
B01D39/16
PERFORMING OPERATIONS; TRANSPORTING
B01D39/04
PERFORMING OPERATIONS; TRANSPORTING
A41D13/11
HUMAN NECESSITIES
Abstract
An air-permeable filter material that includes a polymeric aerogel having a polymeric matrix comprising an open-cell structure is disclosed. The air-permeable filter material can be included in a mask, which can be configured to be placed over a user's mouth and/or nose. The mask can include at least one layer of the air-permeable filter material and is positioned such that inhaled and/or exhaled air of the user passes through the filter material.
Claims
1. An air-permeable filter material that comprises a polymeric aerogel having a polymeric matrix comprising an open-cell structure.
2. The air-permeable filter material of claim 1, wherein the air-permeable filter material is comprised in a mask.
3. The air-permeable filter material of claim 2, wherein at least a portion of the mask is configured to be placed over a user's mouth and/or nose.
4. The air-permeable filter material of claim 3, wherein the mask comprises at least one layer of the air-permeable filter material and is positioned such that inhaled and/or exhaled air of the user passes through the filter material.
5. The air-permeable filter material of any one of claims 2 to 4, wherein the mask comprises at least one strap that is attached to at least two different parts of the mask, and wherein at least a portion of the strap is capable of being positioned behind a user's head or ear.
6. The air-permeable filter material of claim 5, wherein the at least one strap comprises a stretchable or elastic portion.
7. The air-permeable filter material of any one of claims 2 to 4, wherein the air-permeable filter material is comprised in a cartridge.
8. The air-permeable filter material of claim 7, wherein the cartridge is a replaceable cartridge for a cartridge-type respirator.
9. The air-permeable filter material of any one of claim 8, wherein the air-permeable filter material is in the form of a film or is in the form of particles, or a combination thereof.
10. The air-permeable filter material of claim 9, wherein the cartridge has a space, and wherein the space is at least partially filled with the film or the particles or both of the film and particles.
11. The air-permeable filter material of claim 1, wherein the material is comprised in a vent filter.
12. The air-permeable filter material of claim 11, wherein the vent filter has a first surface and an opposing second surface, wherein the shape of the first and second surfaces are square or rectangular in shape.
13. The air-permeable filter material of any one of claims 11 to 12, wherein the vent filter comprises an outer border, wherein the outer border comprises a paper material.
14. The air-permeable filter material of claim 13, wherein the paper material is cardboard or cotton.
15. The air-permeable filter material of any one of claims 1 to 4, wherein the polymeric aerogel is in the form of a film or is in particulate form or a combination thereof.
16. The air-permeable filter material of claim 15, wherein the polymeric aerogel is in the form of a film.
17. The air-permeable filter material of claim 16, wherein the film is adhesively bonded to a support, preferably a scrim.
18. The air-permeable filter material of claim 15, wherein the polymeric aerogel is in particulate form.
19. The air-permeable filter material of claim 18, wherein the polymeric aerogel in particulate form is comprised in a support material, preferably a fibrous support material.
20. The air-permeable filter material of any one of claims 1 to 4, wherein the polymeric aerogel is attached to a substrate.
21. The air-permeable filter material of claim 20, wherein the substrate comprises a paper material, a fibrous material, a metal material, a thermoplastic material, or a thermoset material.
22. The air-permeable filter material of claim 21, wherein the substrate is a fiber substrate, preferably, a woven fiber substrate, a knitted fiber substrate, non-woven fiber substrate, or a paper substrate.
23. The air-permeable filter material of claim 22, wherein the substrate is a scrim.
24. The air-permeable filter material of claim 23, wherein the polymeric aerogel is attached to the substrate with an adhesive, preferably a polyester-based adhesive.
25. The air-permeable filter material of claim 20, wherein the substrate is air permeable.
26. The air-permeable filter material of any one of claims 1 to 4, wherein the filter material is a N95, N99, or N100 qualified filter material.
27. The air-permeable filter material of any one of claims 1 to 4, wherein the filter material is a R95, R99, and R100 qualified filter material.
28. The air-permeable filter material of any one of claims 1 to 4, wherein the filter material is a P95, P99, or P100 qualified filter material.
29. The air-permeable filter material of any one of claims 1 to 4, wherein the filter material is a high efficiency (HE) qualified filter material.
30. The air-permeable filter material of any one of claims 1 to 4, wherein the filter material is capable of removing an airborne pathogen from air by passing air comprising the airborne pathogen through at least a portion of the filter material such that the airborne pathogen is retained in the polymeric aerogel and air is allowed to pass through the polymeric aerogel.
31. The air-permeable filter material of claim 30, wherein the airborne pathogen is a virus, a bacteria, a fungi, or a protozoa.
32. The air-permeable filter material of claim 31, wherein the airborne pathogen is a virus, and wherein the virus is preferably an adenovirus, alphavirus, calicivirus, coronavirus, distemper virus, Ebola virus, enterovirus, flavivirus, hepatitis virus, herpesvirus, infectious peritonitis virus, leukemia virus, Marburg virus, Norwalk virus, orthomyxovirus, papilloma virus, parainfluenza virus, the, paramyxovirus, parvovirus, pestivirus, picorna virus, pox virus, rabies virus, reovirus polypeptides, retrovirus, rotavirus, and vaccinia virus.
33. The air-permeable filter material of claim 32, wherein the airborne pathogen is a coronavirus.
34. The air-permeable filter material of claim 33, wherein the coronavirus is MERS-CoV, SARS-CoV, or SARS-CoV-2, preferably SARS-CoV-2.
35. The air-permeable filter material of claim 31, wherein the airborne pathogen is a bacteria, and wherein the bacterial is preferably Actinomyces, Bacillus, Bacteroides, Bordetella, Bartonella, Borrelia, Brucella, Campylobacter, Capnocytophaga, Chlamydia, Corynebacterium, Coxiella, Dermatophilus, Enterococcus, Ehrlichia, Escherichia, Francisella, Fusobacterium, Haemobartonella, Haemophilus, Helicobacter, Klebsiella, L-form bacteria, Leptospira, Listeria, Mycobacteria, Mycoplasma, Neisseria, Neorickettsia, Nocardia, Pasteurella, Peptococcus, Peptostreptococcus, Pneumococcus, Proteus, Pseudomonas, Rickettsia, Rochalimaea polypeptides, Salmonella, Shigella, Staphylococcus, group A streptococcus, group B streptococcus, Treponema, and Yersinia.
36. The air-permeable filter material of claim 31, wherein the airborne pathogen is a fungi, and wherein the fungi is preferably Absidia, Acremonium, Alternaria, Aspergillus, Basidiobolus, Bipolaris, Blastomyces, Candida, Coccidioides, Conidiobolus, Cryptococcus, Curvalaria, Epidermophyton, Exophiala, Geotrichum, Histoplasma, Madurella, Malassezia, Microsporum, Moniliella, Mortierella, Mucor, Paecilomyces, Penicillium, Phialemonium, Phialophora, Prototheca, Pseudallescheria, Pseudomicrodochium, Pythium, Rhinosporidium, Rhizopus, Scolecobasidium, Sporothrix, Stemphylium, Trichophyton, Trichosporon, and Xylohypha.
37. The air-permeable filter material of claim 31, wherein the airborne pathogen is a protozoa, and wherein the protozoa is preferably Babesia, Balantidium, Besnoitia, Cryptosporidium, Eimeria, Encephalitozoon, Entamoeba, Giardia, Hammondia, Hepatozoon, Isospora, Leishmania, Microsporidia, Neospora, Nosema, Pentatrichomonas, or Plasmodium.
38. The air permeable filter material of any one of claims 1 to 4, wherein the polymeric aerogel comprises micropores, mesopores, or macropores, or a combination thereof.
39. The air permeable filter material of claim 38, wherein at least 10%, 50%, 75%, 95%, or 100% of the aerogel's pore volume is made up of micropores.
40. The air permeable filter material of claim 38, wherein at least 10%, 50%, 75%, 95%, or 100% of the aerogel's pore volume is made up of mesopores.
41. The air permeable filter material of claim 38, wherein at least 10%, 50%, 75%, 95%, or 100% of the aerogel's pore volume is made up of macropores, preferably at least 90% of the aerogel's pore volume is made up of macropores.
42. The air permeable filter material of claim 41, wherein less than 90%, 80%, 70%, 60%, 50%, 40%, 30% 20%, 10% or less than 5% of the aerogel's pore volume is made up of micropores and/or mesopores, preferably less than 10% of the aerogel's pore volume is made up of micropores and/or mesopores.
43. The air permeable filter material of claim 38, wherein the polymeric matrix has an average pore size of 2 nanometers (nm) to 50 nm in diameter.
44. The air permeable filter material of claim 38, wherein the polymeric matrix has an average pore size of greater than 50 nanometers (nm) to 5000 nm in diameter, preferably 1,000 nm to 1,400 nm, or more preferably around 1,200 nm.
45. The air permeable filter material of claim 38, wherein the polymeric matrix has an average pore size of 100 nm to 800 nm, preferably 100 nm to 500 nm, more preferably from 150 nm to 400 nm, even more preferably from 200 nm to 300 nm, still more preferably from 225 nm to 275 nm.
46. The air permeable filter material of any one of claims 1 to 4, wherein the polymeric aerogel is an organic polymeric aerogel.
47. The air permeable filter material of any one of claims 1 to 4, wherein the polymeric aerogel is a polyimide aerogel.
48. The air permeable filter material of any one of claims 1 to 4, wherein the polymeric aerogel is a polyamide aerogel, a polyaramid aerogel, a polyurethane aerogel, a polyuria aerogel, or a polyester aerogel.
49. The air permeable filter material of any one of claims 1 to 4, further comprising a support film or layer at least partially penetrating the polymer matrix of the aerogel.
50. The air permeable filter material of claim 49, wherein the support film is a fiber support.
51. The air permeable filter material of claim 50, wherein the fiber support is a woven fiber support, knitted fiber support, non-woven fiber support or a paper.
52. The air permeable filter material of any one of claims 1 to 4, wherein the material is in the form of a film or layer having a thickness of 0.01 millimeters (mm) to 1000 mm thick, or from 0.025 mm to 100 mm thick, or from 0.050 mm to 10 mm thick, or from 0.100 mm to 2 mm thick, or from 0.125 mm to 1.5 mm.
53. The air permeable filter material of any one of claims 1 to 4, wherein the material is re-useable, washable, and/or capable of being disinfected and reused.
54. A method of removing airborne pathogens, the method comprising passing air comprising the airborne pathogen through at least a portion of the air permeable filter material of any one of claims 1 to 53 such that the airborne pathogen is retained in the polymeric aerogel and air is allowed to pass through the polymeric aerogel.
55. The method of claim 54, wherein the airborne pathogen is a virus, a bacteria, a fungi, or a protozoa.
56. The method of claim 55, wherein the airborne pathogen is a virus, and wherein the virus is preferably an adenovirus, alphavirus, calicivirus, coronavirus, distemper virus, Ebola virus, enterovirus, flavivirus, hepatitis virus, herpesvirus, infectious peritonitis virus, leukemia virus, Marburg virus, Norwalk virus, orthomyxovirus, papilloma virus, parainfluenza virus, the, paramyxovirus, parvovirus, pestivirus, picorna virus, pox virus, rabies virus, reovirus polypeptides, retrovirus, rotavirus, and vaccinia virus.
57. The method of claim 56, wherein the airborne pathogen is a coronavirus.
58. The method of claim 57, wherein the coronavirus is MERS-CoV, SARS-CoV, or SARS-CoV-2, preferably SARS-CoV-2.
59. The method of claim 55, wherein the airborne pathogen is a bacteria, and wherein the bacterial is preferably Actinomyces, Bacillus, Bacteroides, Bordetella, Bartonella, Borrelia, Brucella, Campylobacter, Capnocytophaga, Chlamydia, Corynebacterium, Coxiella, Dermatophilus, Enterococcus, Ehrlichia, Escherichia, Francisella, Fusobacterium, Haemobartonella, Haemophilus, Helicobacter, Klebsiella, L-form bacteria, Leptospira, Listeria, Mycobacteria, Mycoplasma, Neisseria, Neorickettsia, Nocardia, Pasteurella, Peptococcus, Peptostreptococcus, Pneumococcus, Proteus, Pseudomonas, Rickettsia, Rochalimaea polypeptides, Salmonella, Shigella, Staphylococcus, group A streptococcus, group B streptococcus, Treponema, and Yersinia.
60. The method of claim 55, wherein the airborne pathogen is a fungi, and wherein the fungi is preferably Absidia, Acremonium, Alternaria, Aspergillus, Basidiobolus, Bipolaris, Blastomyces, Candida, Coccidioides, Conidiobolus, Cryptococcus, Curvalaria, Epidermophyton, Exophiala, Geotrichum, Histoplasma, Madurella, Malassezia, Microsporum, Moniliella, Mortierella, Mucor, Paecilomyces, Penicillium, Phialemonium, Phialophora, Prototheca, Pseudallescheria, Pseudomicrodochium, Pythium, Rhinosporidium, Rhizopus, Scolecobasidium, Sporothrix, Stemphylium, Trichophyton, Trichosporon, and Xylohypha.
61. The method of claim 55, wherein the airborne pathogen is a protozoa, and wherein the protozoa is preferably Babesia, Balantidium, Besnoitia, Cryptosporidium, Eimeria, Encephalitozoon, Entamoeba, Giardia, Hammondia, Hepatozoon, Isospora, Leishmania, Microsporidia, Neospora, Nosema, Pentatrichomonas, Plasmodium.
62. A method of disinfecting the air permeable filter material of any one of claims 1 to 53, the method comprising subjecting the material to a disinfectant solution or spray capable of killing an airborne pathogen.
63. The method of claim 62, wherein the airborne pathogen is a virus, a bacteria, a fungi, or a protozoa.
64. A method of making the air permeable filter material of any one of claims 1 to 53, the method comprising: (a) providing a monomer or a combination of monomers to a solvent to form a solution; (b) polymerizing the monomers in the solution to form a polymer gel matrix; and (c) subjecting the polymer gel matrix to conditions sufficient to remove liquid from the polymer gel matrix to form an aerogel having a polymeric matrix comprising an open-cell structure.
65. The method of claim 64, wherein step (b) further comprises adding a curing agent to the solution to reduce the solubility of polymers formed in the solution and to form macropores in the gel matrix, the formed macropores containing liquid from the solution.
66. The method of any one of claims 64 to 65, the method further comprising: covering or immersing a support film in the solution in step (a) or (b) such that the support film is attached to the resulting polymer gel matrix and ultimately to the produced aerogel matrix.
67. The method of any one of claims 64 to 65, further comprising casting the polymer gel matrix in step (b) onto a support such that a layer of the polymeric gel matrix is comprised on the support, wherein the aerogel in step (c) is in the form of a film.
68. The method of claim 67, further comprising crushing, grinding, or milling the film to produce aerogel particles.
69. A face mask comprising: an air-permeable filter material that comprises a polymeric aerogel having a polymeric matrix comprising an open-cell structure, wherein at least 90% of the polymeric matrix's pore volume comprises macropores; at least one strap that is attached to at least two different parts of the mask, wherein at least a portion of the strap is stretchable or elastic and is capable of being positioned behind a person's head or ear, wherein at least a portion of the air-permeable filter material is configured such that inhaled and/or exhaled air of the person passes through the filter material, and wherein the filter material is capable of removing an airborne pathogen from the air by passing the air comprising the airborne pathogen through at least a portion of the filter material such that the airborne pathogen is retained in the polymeric aerogel and the air is allowed to pass through the polymeric aerogel.
70. The face mask of claim 69, wherein the polymeric aerogel in the air-permeable filter material is in the form of a sheet or film.
71. The face mask of claim 69, wherein the polymeric aerogel in the air-permeable filter material is in particulate form.
72. The face mask of claim 71, wherein the air-permeable filter material further comprises particles of activated carbon or charcoal.
73. The face mask of any one of claims 69 to 72, wherein the airborne pathogen is a virus, preferably a coronavirus, more preferably MERS-CoV, SARS-CoV, or SARS-CoV-2, or even more preferably SARS-CoV-2.
74. The face mask of claim 73, wherein the polymer aerogel is a polyimide aerogel.
75. The face mask of any one of claims 69 to 72, wherein the polymeric matrix has an average pore size of greater than 50 nanometers (nm) to 5000 nm in diameter, preferably 1,000 nm to 1,400 nm in diameter or 100 nm to 800 nm in diameter.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0034] The following drawings form part of the present specification and are included to further demonstrate certain aspects of the present invention. The invention may be better understood by reference to one or more of these drawings in combination with the detailed description of the specification embodiments presented herein.
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[0059] While the invention is susceptible to various modifications and alternative forms, specific embodiments thereof are shown by way of example in the drawings and may herein be described in detail. The drawings may not be to scale.
DETAILED DESCRIPTION
[0060] A discovery has been made that provides a solution to at least some of the problems associated with PPE and/or other equipment that uses filters to filter out undesired particles from air. In one aspect, the solution resides in the use of polymeric aerogels that have a polymeric matrix with an open-cell structure in filtration applications such as PPE equipment (e.g., face or surgical masks). The polymeric aerogels used to make the filter material have a sufficient amount of structural integrity that allows the material to be washed or disinfected or sterilized and reused. This provides an advantage in that it can reduce or prevent PPE shortages such as the shortages seen in today's society, which is dealing with the novel coronavirus (SARS-CoV-2) pandemic. Further, the porous structure of the polymeric aerogels allows for a sufficient amount of air to flow through the aerogel while preventing or limited the flow of viral or bacterial particles, such as, for example particles of SARS-CoV-2.
[0061] These and other non-limiting aspects of the present invention are discussed in further detail in the following sections.
A. Air-Permeable Filter Material and Air-Filtration Devices
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B. Types of Polymeric Aerogels
[0073] The polymeric aerogel comprising the polymeric matrix used in the air-permeable filter material 1 of the present invention can include organic materials, inorganic materials, or a mixture thereof, and have matrices that include macropores, mesopores, or micropores, a combination thereof. The aerogels or wet gels used to prepare the aerogels may be prepared by any known gel-forming techniques, for example adjusting the pH and/or temperature of a dilute metal oxide sol to a point where gelation occurs. Aerogels can be made from polyacrylates, polystyrenes, polyacrylonitriles, polyurethanes, polysiloxanes, polyimides, polyamides, polyaramids, polyfurfural alcohol, phenol furfuryl alcohol, melamine formaldehydes, resorcinol formaldehydes, cresol formaldehyde, phenol formaldehyde, polyvinyl alcohol dialdehyde, polycyanurates, polyacrylamides, various epoxies, agar, agarose, and the like. In particular embodiments the aerogel is a polyimide aerogel.
[0074] Polyimides are a type of polymer with many desirable properties. Polyimide polymers include a nitrogen atom in the polymer backbone, where the nitrogen atom is connected to two carbonyl carbons, such that the nitrogen atom is somewhat stabilized by the adjacent carbonyl groups. A carbonyl group includes a carbon, referred to as a carbonyl carbon, which is double bonded to an oxygen atom. Polyimides are usually considered an AA-BB type polymer because usually two different classes of monomers are used to produce the polyimide polymer. Polyimides can also be prepared from AB type monomers. For example, an aminodicarboxylic acid monomer can be polymerized to form an AB type polyimide. Monoamines and/or mono anhydrides can be used as end capping agents if desired.
[0075] One class of polyimide monomer is usually a diamine, or a diamine monomer. The diamine monomer can also be a diisocyanate, and it is to be understood that an isocyanate could be substituted for an amine in this description, as appropriate. There are other types of monomers that can be used in place of the diamine monomer, as known to those skilled in the art. The other type of monomer is called an acid monomer, and is usually in the form of a dianhydride. In this description, the term “di-acid monomer” is defined to include a dianhydride, a tetraester, a diester acid, a tetracarboxylic acid, or a trimethylsilyl ester, all of which can react with a diamine to produce a polyimide polymer. Dianhydrides are to be understood as tetraesters, diester acids, tetracarboxylic acids, or trimethylsilyl esters that can be substituted, as appropriate. There are also other types of monomers that can be used in place of the di-acid monomer, as known to those skilled in the art.
[0076] Because one di-acid monomer has two anhydride groups, different diamino monomers can react with each anhydride group so the di-acid monomer may become located between two different diamino monomers. The diamine monomer contains two amine functional groups; therefore, after the first amine functional group attaches to one di-acid monomer, the second amine functional group is still available to attach to another di-acid monomer, which then attaches to another diamine monomer, and so on. In this manner, the polymer backbone is formed. The resulting polycondensation reaction forms a polyamic acid.
[0077] The polyimide polymer is usually formed from two different types of monomers, and it is possible to mix different varieties of each type of monomer. Therefore, one, two, or more di-acid monomers can be included in the reaction vessel, as well as one, two or more diamino monomers. The total molar quantity of di-acid monomers is kept about the same as the total molar quantity of diamino monomers if a long polymer chain is desired. Because more than one type of diamine or di-acid can be used, the various monomer constituents of each polymer chain can be varied to produce polyimides with different properties. For example, a single diamine monomer AA can be reacted with two di-acid co monomers, B.sub.1B.sub.1 and B.sub.2B.sub.2, to form a polymer chain of the general form of (AA-B.sub.1B.sub.1).sub.x-(AA-B.sub.2B.sub.2).sub.y in which x and y are determined by the relative incorporations of B.sub.1B.sub.1 and B.sub.2B.sub.2 into the polymer backbone. Alternatively, diamine co-monomers A.sub.1A.sub.1 and A.sub.2A.sub.2 can be reacted with a single di-acid monomer BB to form a polymer chain of the general form of (A.sub.1A.sub.1-BB).sub.x-(A.sub.2A.sub.2-BB).sub.y. Additionally, two diamine co-monomers A.sub.1A.sub.1 and A.sub.2A.sub.2 can be reacted with two di-acid co-monomers B.sub.1B.sub.1 and B.sub.2B.sub.2 to form a polymer chain of the general form (A.sub.1A.sub.1-B.sub.1B.sub.1).sub.w-(A.sub.1A.sub.1-B.sub.2B.sub.2).sub.x-(A.sub.2A.sub.2-B.sub.1B.sub.1).sub.y-(A.sub.2A.sub.2-B.sub.2B.sub.2).sub.z, where w, x, y, and z are determined by the relative incorporation of A.sub.1A.sub.1-B.sub.1B.sub.1, A.sub.1A.sub.1-B.sub.2B.sub.2, A.sub.2A.sub.2-B.sub.1B.sub.1, and A.sub.2A.sub.2-B.sub.2B.sub.2 into the polymer backbone. More than two di-acid co-monomers and/or more than two diamine co-monomers can also be used. Therefore, one or more diamine monomers can be polymerized with one or more di-acids, and the general form of the polymer is determined by varying the amount and types of monomers used.
[0078] There are many examples of monomers that can be used to make the aerogel polymer compositions containing polyamic amide polymer of the present invention. In some embodiments, the diamine monomer is a substituted or unsubstituted aromatic diamine, a substituted or unsubstituted alkyldiamine, or a diamine that can include both aromatic and alkyl functional groups. A non-limiting list of possible diamine monomers comprises 4,4′-oxydianiline (ODA), 3,4′-oxydianiline, 3,3′-oxydianiline, p-phenylenediamine, m-phenylenediamine, o-phenylenediamine, diaminobenzanilide, 3,5-diaminobenzoic acid, 3,3′-diaminodiphenylsulfone, 4,4′-diaminodiphenyl sulfones, 1,3-bis-(4-aminophenoxy)benzene, 1,3-bis-(3-aminophenoxy)benzene, 1,4-bis-(4-aminophenoxy)benzene, 1,4-bis-(3-aminophenoxy)benzene, 2,2-bis[4-(4-aminophenoxy)phenyl]-hexafluoropropane, 2,2-bis(3-aminophenyl)-1,1,1,3,3,3-hexafluoropropane, 4,4′-isopropylidenedianiline, 1-(4-aminophenoxy)-3-(3-aminophenoxy)benzene, 1-(4-aminophenoxy)-4-(3-aminophenoxy)benzene, bis-[4-(4-aminophenoxy)phenyl]sulfones, 2,2-bis[4-(3-aminophenoxy)phenyl]sulfones, bis(4-[4-aminophenoxy]phenyl)ether, 2,2′-bis-(4-aminophenyl)-hexafluoropropane (6F-diamine), 2,2′-bis-(4-phenoxyaniline)isopropylidene, meta-phenylenediamine, para-phenylenediamine, 1,2-diaminobenzene, 4,4′-diaminodiphenylmethane, 2,2-bis(4-aminophenyl)propane, 4,4′diaminodiphenyl propane, 4,4′-diaminodiphenyl sulfide, 4,4′-diaminodiphenylsulfone, 3,4′diaminodiphenyl ether, 4,4′-diaminodiphenyl ether, 2,6-diaminopyridine, bis(3-aminophenyl)diethyl silane, 4,4′-diaminodiphenyl diethyl silane, benzidine, dichlorobenzidine, 3,3′-dimethoxybenzidine, 4,4′-diaminobenzophenone, N,N-bis(4-aminophenyl)-n-butylamine, N,N-bis(4-aminophenyl)methylamine, 1,5-diaminonaphthalene, 3,3′-dimethyl-4,4′-diaminobiphenyl, 4-aminophenyl-3-aminobenzoate, N,N-bis(4-aminophenyl)aniline, bis(p-beta-amino-t-butylphenyl)ether, p-bis-2-(2-methyl-4-aminopentyl)benzene, p-bis(1,1-dimethyl-5-aminopentyl)benzene, 1,3-bis(4-aminophenoxy)benzene, m-xylenediamine, p-xylenediamine, 4,4′-diaminodiphenyl ether phosphine oxide, 4,4′-diaminodiphenyl N-methyl amine, 4,4′-diaminodiphenyl N-phenyl amine, amino-terminal polydimethylsiloxanes, amino-terminal polypropyleneoxides, amino-terminal polybutyleneoxides, 4,4′-Methylenebis(2-methylcyclohexylamine), 1,2-diaminoethane, 1,3-diaminopropane, 1,4-diaminobutane, 1,5-diaminopentane, 1,6-diaminohexane, 1,7-diaminoheptane, 1,8-diaminooctane, 1,9-diaminononane, 1,10-diaminodecane, and 4,4′-methylenebisbenzeneamine, 2,2′-dimethylbenzidine, (also known as 4,4′-diamino-2,2′-dimethylbiphenyl (DMB)), bisaniline-p-xylidene, 4,4′-bis(4-aminophenoxy)biphenyl, 3,3′-bis(4 aminophenoxy)biphenyl, 4,4′-(1,4-phenylenediisopropylidene)bis aniline, and 4,4′-(1,3-phenylenediisopropylidene)bisaniline, or combinations thereof. In a specified embodiment, the diamine monomer is ODA, 2,2′-dimethylbenzidine, or both.
[0079] A non-limiting list of possible dianhydride (“diacid”) monomers includes hydroquinone dianhydride, 3,3′,4,4′-biphenyltetracarboxylic dianhydride (BPDA), pyromellitic dianhydride (PMDA), 3,3′,4,4′-benzophenonetetracarboxylic dianhydride, 4,4′-oxydiphthalic anhydride, 3,3′,4,4′-diphenylsulfonetetracarboxylic dianhydride, 4,4′-(4,4′-isopropylidenediphenoxy)bis(phthalic anhydride), 2,2-bis(3,4-dicarboxyphenyl)propane dianhydride, 4,4′-(hexafluoroisopropylidene)diphthalic anhydride, bis(3,4-dicarboxyphenyl) sulfoxide dianhydride, polysiloxane-containing dianhydride, 2,2′,3,3′-biphenyltetracarboxylic dianhydride, 2,3,2′,3′-benzophenonetetraearboxylic dianhydride, naphthalene-2,3,6,7-tetracarboxylic dianhydride, naphthalene-1,4,5,8-tetracarboxylie dianhydride, 4,4′-oxydiphthalic dianhydride, 3,3′,4,4′-biphenylsulfone tetracarboxylic dianhydride, 3,4,9,10-perylene tetracarboxylic dianhydride, bis(3,4-dicarboxyphenyl)sulfide dianhydride, bis(3,4-dicarboxyphenyl)methane dianhydride, 2,2-bis(3,4-dicarboxyphenyl)propane dianhydride, 2,2-bis(3,4-dicarboxyphenyl)hexafluoropropane, 2,6-dichloronaphthalene-1,4,5,8-tetracarboxylic dianhydride, 2,7-dichloronapthalene-1,4,5,8-tetracarboxylic dianhydride, 2,3,6,7-tetrachloronaphthalene-1,4,5,8-tetracarboxylic dianhydride, phenanthrene, 8,9,10-tetracarboxylic dianhydride, pyrazine-2,3,5,6-tetracarboxylic dianhydride, benzene-1,2,3,4-tetracarboxylic dianhydride, and thiophene-2,3,4,5-tetracarboxylic dianhydride. In a specific embodiment, the dianhydride monomer is BPDA, PMDA, or both.
[0080] In some aspects, the molar ratio of anhydride to total diamine is from 0.4:1 to 1.6:1, 0.5:1 to 1.5:1, 0.6:1 to 1.4:1, 0.7:1 to 1.3:1, or specifically from 0.8:1 to 1.2:1. In further aspects, the molar ratio of dianhydride to multifunctional amine (e.g., triamine) is 2:1 to 140:1, 3:1 to 130:1, 4:1 to 120:1, 5:1 to 110:1, 6:1 to 100:1, 7:1 to 90:1, or specifically from 8:1 to 80:1. Mono-anhydride groups can also be used. Non-limiting examples of mono-anhydride groups include 4-amino-1,8-naphthalic anhydride, endo-bicyclo[2.2.2]oct-5-ene-2,3-dicarboxylic anhydride, citraconic anhydride, trans-1,2-cyclohexanedicarboxylic anhydride, 3,6-dichlorophthalic anhydride, 4,5-dichlorophthalic anhydride, tetrachlorophthalic anhydride 3,6-difluorophthalic anhydride, 4,5-difluorophthalic anhydride, tetrafluorophthalic anhydride, maleic anhydride, 1-cyclopentene-1,2-dicarboxylic anhydride, 2,2-dimethylglutaric anhydride 3,3-dimethylglutaric anhydride, 2,3-dimethylmaleic anhydride, 2,2-dimethylsuccinic anhydride, 2,3-diphenylmaleic anhydride, phthalic anhydride, 3-methylglutaric anhydride, methylsuccinic anhydride, 3-nitrophthalic anhydride, 4-nitrophthalic anhydride, 2,3-pyrazinedicarboxylic anhydride, or 3,4-pyridinedicarboxylic anhydride. Specifically, the mono-anhydride group can be phthalic anhydride.
[0081] In another embodiment, the polymer compositions used to prepare the aerogels of the present invention include multifunctional amine monomers with at least three primary amine functionalities. The multifunctional amine may be a substituted or unsubstituted aliphatic multifunctional amine, a substituted or unsubstituted aromatic multifunctional amine, or a multifunctional amine that includes a combination of an aliphatic and two aromatic groups, or a combination of an aromatic and two aliphatic groups. A non-limiting list of possible multifunctional amines include propane-1,2,3-triamine, 2-aminomethylpropane-1,3-diamine, 3-(2-aminoethyl)pentane-1,5-diamine, bis(hexamethylene)triamine, N′,N′-bis(2-aminoethyl)ethane-1,2-diamine, N′,N′-bis(3-aminopropyl)propane-1,3-diamine, 4-(3-aminopropyl)heptane-1,7-diamine, N′,N′-bis(6-aminohexyl)hexane-1,6-diamine, benzene-1,3,5-triamine, cyclohexane-1,3,5-triamine, melamine, N-2-dimethyl-1,2,3-propanetriamine, diethylenetriamine, 1-methyl or 1-ethyl or 1-propyl or 1-benzyl-substituted diethylenetriamine, 1,2-dibenzyldiethylenetriamine, lauryldiethylenetriamine, N-(2-hydroxypropyl)diethylenetriamine, N,N-bis(1-methylheptyl)-N-2-dimethyl-1,2,3-propanetriamine, 2,4,6-tris(4-(4-aminophenoxy)phenyl)pyridine, N,N-dibutyl-N-2-dimethyl-1,2,3-propanetriamine, 4,4′-(2-(4-aminobenzyl)propane-1,3-diyl)dianiline, 4-((bis(4-aminobenzyl)amino)methyl)aniline, 4-(2-(bis(4-aminophenethyl)amino)ethyl)aniline, 4,4′-(3-(4-aminophenethyl)pentane-1,5-diyl)dianiline, 1,3,5-tris(4-aminophenoxy)benzene (TAPOB), 4,4′,4″-methanetriyltrianiline, N,N,N′,N′-Tetrakis(4-aminophenyl)-1,4-phenylenediamine, a polyoxypropylenetriamine, octa(aminophenyl)polyhedral oligomeric silsesquioxane, or combinations thereof. A specific example of a polyoxypropylenetriamine is JEFFAMINE® T-403 from Huntsman Corporation, The Woodlands, Tex. USA. In a specific embodiment, the aromatic multifunctional amine may be 1,3,5-tris(4-aminophenoxy)benzene or 4,4′,4″-methanetriyltrianiline. In some embodiments, the multifunctional amine includes three primary amine groups and one or more secondary and/or tertiary amine groups, for example, N′,N′-bis(4-aminophenyl)benzene-1,4-diamine.
[0082] Non-limiting examples of capping agents or groups include amines, maleimides, nadimides, acetylene, biphenylenes, norbornenes, cycloalkyls, and N-propargyl and specifically those derived from reagents including 5-norbornene-2,3-dicarboxylic anhydride (nadic anhydride, NA), methyl-nadic anhydride, hexachloro-nadic anhydride, cis-4-cyclohexene-1,2-dicarboxylic anhydride, 4-amino-N-propargylphthalimide, 4-ethynylphthalic anhydride, and maleic anhydride.
[0083] The characteristics or properties of the final polymer are significantly impacted by the choice of monomers which are used to produce the polymer. Factors to be considered when selecting monomers include the properties of the final polymer, such as the flexibility, thermal stability, coefficient of thermal expansion (CTE), coefficient of hydroscopic expansion (CHE) and any other properties specifically desired, as well as cost. Often, certain important properties of a polymer for a particular use can be identified. Other properties of the polymer may be less significant, or may have a wide range of acceptable values; so many different monomer combinations could be used.
[0084] In some instances, the backbone of the polymer can include substituents. The substituents (e.g., oligomers, functional groups, etc.) can be directly bonded to the backbone or linked to the backbone through a linking group (e.g., a tether or a flexible tether). In other embodiments, a compound or particles can be incorporated (e.g., blended and/or encapsulated) into the polyimide structure without being covalently bound to the polyimide structure. In some instances, the incorporation of the compound or particles can be performed during the polyamic reaction process. In some instances, particles can aggregate, thereby producing polyimides having domains with different concentrations of the non-covalently bound compounds or particles.
[0085] Specific properties of a polyimide can be influenced by incorporating certain compounds into the polyimide. The selection of monomers is one way to influence specific properties. Another way to influence properties is to add a compound or property modifying moiety to the polyimide.
C. Preparation of Polymeric Aerogels
[0086] Polymeric aerogel films that can be used in the context of the present invention are commercially available. Non-limiting examples of such films include the Blueshift AeroZero® rolled thin film (available from Blueshift Materials, Inc. (Spencer, Mass.) and Airloy® films (available from Aerogel Technologies, LLC), with the Blueshift AeroZero® rolled thin film being preferred in some aspects. Polymeric aerogel particles that can be used in the context of the present invention are commercially available, Non-limiting examples of such particles include the Blueshift AeroZero® particles (available from Blueshift Materials, Inc. (Spencer, Mass.), Sumteq Thermoplastic Aerogel Particles (can be purchased from Aerogel Technologies, LLC, Boston, Mass.), and Aerogelex Biopolymer Aerogel Particles (can be purchased from Aerogel Technologies, LLC, Boston, Mass.), with the Blueshift AeroZero® particles being preferred in some aspects.
[0087] Further, and in addition to the processes discussed below, polymeric aerogels (films, stock shapes or monoliths, particles, etc.) can be made using the methodology described in International Patent Application Publication Nos. WO 2014/189560 to Rodman et al., 2017/07888 to Sakaguchi et al., 2018/078512 to Yang et al. 2018/140804 to Sakaguchi et al., 2019/006184 to Irvin et al., International Patent Application No. PCT/US2019/029191 to Ejaz et al., U.S. Patent Application Publication No. 2017/0121483 to Poe et al., and/or U.S. Pat. No. 9,963,571 to Sakaguchi et al., all of which are incorporated herein by reference in their entirety.
[0088] The following provides non-limiting processes that can be used to make the polymeric aerogel matrices used in the air-permeable filter material of the present invention. These processes can include: 1) preparation of the polymer gel, 2) optional solvent exchange, 3) drying of the polymeric solution to form the aerogel; 4) attaching a polymeric aerogel film on a substrate; and 5) producing polymeric aerogel particles.
[0089] 1. Formation of a Polymer Gel
[0090] The first stage in the synthesis of an aerogel can be the synthesis of a polymerized gel. For example, if a polyimide aerogel is desired, at least one acid monomer can be reacted with at least one diamino monomer in a reaction solvent to form a polyamic acid. As discussed above, numerous acid monomers and diamino monomers may be used to synthesize the polyamic acid. In one aspect, the polyamic acid is contacted with an imidization catalyst in the presence of a chemical dehydrating agent to form a polymerized polyimide gel via an imidization reaction. “Imidization” is defined as the conversion of a polyimide precursor into an imide. Any imidization catalyst suitable for driving the conversion of polyimide precursor to the polyimide state is suitable. Non-limiting examples of chemical imidization catalysts include pyridine, methylpyridines, quinoline, isoquinoline, 1,8-diazabicyclo[5.4.0]undec-7-ene (DBU), triethylenediamine, lutidine, N-methylmorpholine, triethylamine, tripropylamine, tributylamine, other trialkylamines, 2-methyl imidazole, 2-ethyl-4-methylimidazole, imidazole, other imidazoles, and combinations thereof. Any dehydrating agent suitable for use in formation of an imide ring from an amic acid precursor is suitable for use in the methods of the present invention. Preferred dehydrating agents comprise at least one compound selected from the group consisting of acetic anhydride, propionic anhydride, n-butyric anhydride, benzoic, anhydride, trifluoroacetic anhydride, phosphorus trichloride, and dicyclohexylcarbodiimide.
[0091] In one aspect of the current invention, one or more diamino monomers and one or more multifunctional amine monomers are premixed in one or more solvents and then treated with one or more dianhydrides (e.g., di-acid monomers) that are added in sequentially smaller amounts at pre-defined time increments while monitoring the viscosity. The desired viscosity of the polymerized solution can range from 50 to 20,000 cP or specifically 500 to 5,000 cP. By performing the reaction using incremental addition of dianhydride while monitoring viscosity, a non-crosslinked aerogel can be prepared. For instance, a triamine monomer (23 equiv.) can be added to the solvent to give a 0.0081 molar solution. To the solution a first diamine monomer (280 equiv.) can be added, followed by second diamine monomer (280 equiv.). Next a dianhydride (552 total equiv.) can be added in sequentially smaller amounts at pre-defined time increments while monitoring the viscosity. The dianhydride can be added until the viscosity reaches 1,000 to 1,500 cP. For example, a first portion of dianhydride can be added, the reaction can be stirred (e.g., for 20 minutes), a second portion of dianhydride can be added, and a sample of the reaction mixture was then analyzed for viscosity. After stirring for additional time (e.g., for 20 minutes), a third portion of dianhydride can be added, and a sample can be taken for analysis of viscosity. After further stirring for a desired period of time (e.g., 10 hours to 12 hours), a mono-anhydride (96 equiv.) can be added. After having reached the target viscosity, the reaction mixture can be stirred for a desired period of time (e.g., 10 hours to 12 hours) or the reaction is deemed completed.
[0092] The reaction temperature for the gel formation can be determined by routine experimentation depending on the starting materials. In a preferred embodiment, the temperature range can be greater than, equal to, or between any two of 15° C., 20° C., 30° C., 35° C., 40° C., and 45° C. After a desired amount of time (e.g., about 2 hours), the product can be isolated (e.g., filtered), after which a nitrogen containing hydrocarbon (828 equiv.) and dehydration agent (1214 equiv.) can be added. The addition of the nitrogen containing hydrocarbon and/or dehydration agent can occur at any temperature. In some embodiments, the nitrogen containing hydrocarbon and/or dehydration agent is added to the solution at 20° C. to 28° C. (e.g., room temperature) stirred for a desired amount of time at room temperature. In some instances, after addition of nitrogen containing hydrocarbon and/or dehydration agent, the solution temperature is raised up to 150° C.
[0093] The reaction solvent can include dimethylsulfoxide (DMSO), diethylsulfoxide, N,N-dimethylformamide (DMF), N,N-diethylformamide, N,N-dimethylacetamide (DMAc), N,N-diethylacetamide, N-methyl-2-pyrrolidone (NMP), 1-methyl-2-pyrrolidinone, N-cyclohexyl-2-pyrrolidone, 1,13-dimethyl-2-imidazolidinone, diethyleneglycoldimethoxyether, o-dichlorobenzene, phenols, cresols, xylenol, catechol, butyrolactones, hexamethylphosphoramide, and mixtures thereof. The reaction solvent and other reactants can be selected based on the compatibility with the materials and methods applied i.e. if the polymerized polyamic amide gel is to be cast onto a support film, injected into a moldable part, or poured into a shape for further processing into a workpiece. In a specific embodiment, the reaction solvent is DMSO.
[0094] While keeping the above in mind, the introduction of macropores into the aerogel polymeric matrix, as well as the amount of such macropores present, can be performed in the manner described above in the Summary of the Invention Section as well as throughout this specification. In one non-limiting manner, the formation of macropores versus smaller mesopores and micropores can be primarily controlled by controlling the polymer/solvent dynamics during gel formation. By doing so, the pore structure can be controlled, and the quantity and volume of macroporous, mesoporous, microporous cells can be controlled. For example, a curing additive that reduces the solubility of the polymers being formed during polymerization step (b), such as 1,4-diazabicyclo[2.2.2]octane, can produce a polymer gel containing a higher number of macropores as compared to another curing additive that improves the resultant polymer solubility, such as triethylamine. In another specific non-limiting example when forming a polyimide aerogel having macropores, increasing the ratio of rigid amines incorporated into the polymer backbone such as p-phenylenediamine (p-PDA) as compared to more flexible diamines such as -ODA, the formation of macropores as compared to smaller mesopores and micropores can be controlled.
[0095] The polymer solution may optionally be cast onto a casting sheet covered by a support film for a period of time. Casting can include spin casting, gravure coating, three roll coating, knife over roll coating, slot die extrusion, dip coating, Meyer rod coating, or other techniques. In one embodiment, the casting sheet is a polyethylene terephthalate (PET) casting sheet. After a passage of time, the polymerized reinforced gel is removed from the casting sheet and prepared for the solvent exchange process. In some embodiments, the cast film can be heated in stages to elevated temperatures to remove solvent and convert the amic acid functional groups in the polyamic acid to imides with a cyclodehydration reaction, also called imidization. In some instances, polyamic acids may be converted in solution to polyimides with the addition of the chemical dehydrating agent, catalyst, and/or heat.
[0096] In some embodiments, the polyimide polymers can be produced by preparing a polyamic acid polymer in the reaction vessel. The polyamic acid is then formed into a sheet or a film and subsequently processed with catalysts or heat and catalysts to convert the polyamic acid to a polyimide.
[0097] 2. Optional Solvent Exchange
[0098] After the polymer gel is synthesized, it may be desirable in certain instances to conduct a solvent exchange wherein the reaction solvent is exchanged for a more desirable second solvent. Accordingly, in one embodiment, a solvent exchange can be conducted wherein the polymerized gel is placed inside of a pressure vessel and submerged in a mixture comprising the reaction solvent and the second solvent. Then, a high pressure atmosphere is created inside of the pressure vessel thereby forcing the second solvent into the polymerized gel and displacing a portion of the reaction solvent. Alternatively, the solvent exchange step may be conducted without the use of a high pressure environment. It may be necessary to conduct a plurality of rounds of solvent exchange. In some embodiments, solvent exchange is not necessary.
[0099] The time necessary to conduct the solvent exchange will vary depending upon the type of polymer undergoing the exchange as well as the reaction solvent and second solvent being used. In one embodiment, each solvent exchange can range from 1 to 168 hours or any period time there between including 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21, 22, or 23, 24, 25, 50, 75, 100, 125, 150, 155, 160, 165, 166, 167, or 168 hours. In another embodiment, each solvent exchange can take approximately 1 to 60 minutes, or about 30 minutes. Exemplary second solvents include methanol, ethanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, isobutanol, tert-butanol, 3-methyl-2-butanol, 3,3-dimethyl-2-butanol, 2-pentanol, 3-pentanol, 2,2-dimethylpropan-1-ol, cyclohexanol, diethylene glycol, cyclohexanone, acetone, acetyl acetone, 1,4-dioxane, diethyl ether, dichloromethane, trichloroethylene, chloroform, carbon tetrachloride, water, and mixtures thereof. In certain non-limiting embodiments, the second solvent can have a suitable freezing point for performing supercritical or subcritical drying steps. For example tert-butyl alcohol has a freezing point of 25.5° C. and water has a freezing point of 0° C. under one atmosphere of pressure. Alternatively, and as discussed below, however, the drying can be performed without the use of supercritical or subcritical drying steps, such as by evaporative drying techniques.
[0100] The temperature and pressure used in the solvent exchange process may be varied. The duration of the solvent exchange process can be adjusted by performing the solvent exchange at a varying temperatures or atmospheric pressures, or both, provided that the pressure and temperature inside the pressure vessel does not cause either the first solvent or the second solvent to leave the liquid phase and become gaseous phase, vapor phase, solid phase, or supercritical fluid. Generally, higher pressures and/or temperatures decrease the amount of time required to perform the solvent exchange, and lower temperatures and/or pressures increase the amount of time required to perform the solvent exchange.
[0101] 3. Cooling and Drying
[0102] In one embodiment after solvent exchange, the polymerized gel can be exposed to supercritical drying. In this instance the solvent in the gel can be removed by supercritical CO.sub.2 extraction.
[0103] In another embodiment after solvent exchange, the polymerized reinforced gel can be exposed to subcritical drying. In this instance, the gel can be cooled below the freezing point of the second solvent and subjected to a freeze drying or lyophilization process to produce the aerogel. For example, if the second solvent is water, then the polymerized gel is cooled to below 0° C. After cooling, the polymerized gel can be subjected to a vacuum for a period of time to allow sublimation of the second solvent
[0104] In still another embodiment, after solvent exchange, the polymerized gel can be exposed to subcritical drying with optional heating after the majority of the second solvent has been removed through sublimation. In this instance the partially dried gel material is heated to a temperature near or above the boiling point of the second solvent for a period of time. The period of time can range from a few hours to several days, although a typical period of time is approximately 4 hours. During the sublimation process, a portion of the second solvent present in the polymerized gel has been removed, leaving a gel that can have macropores, mesopores, or micropores, or any combination thereof or all of such pore sizes. After the sublimation process is complete, or nearly complete, the aerogel has been formed.
[0105] In yet another embodiment after solvent exchange, the polymerized gel can be dried under ambient conditions, for example, by removing the solvent under a stream of gas (e.g., air, anhydrous gas, inert gas (e.g., nitrogen (N.sub.2) gas), etc.). Still further, passive drying techniques can be used such as simply exposing the gel to ambient conditions without the use of a gaseous stream.
[0106] Once cooled or dried, the films and stock shapes can be configured for use in the air filter materials 1 of the present invention. For example, the films or stock shapes can be processed into desired shapes (e.g., by cutting or grinding) such as square shapes, rectangular shapes, circular shapes, triangular shapes, irregular shapes, random shapes, etc. Also, and as discussed above, the films or stock shapes can be affixed to a support material such as with an adhesive. In alternative embodiments where an adhesive may not be desired, a support material can be incorporated into the matrix of the polymeric aerogel, which is discussed below. Alternatively, and also discussed below, the polymeric aerogels can be made into particulate form.
[0107] 4. Incorporation of a Support Material into the Matrix of the Polymeric Aerogel
[0108] In addition to the methods discussed above with respect to the use of adhesives for attaching a polymeric aerogel to a support material, an optional embodiment of the present invention can include incorporation of the support material into the polymeric matrix to create a reinforced polymeric aerogel without the use of adhesives. Notably, during manufacture of a non-reinforced polymer aerogel a reinforcing support film can be used as a carrier to support the gelled film during processing. During rewinding, the gelled film can be irreversibly pressed into the carrier film. Pressing the gelled film into the carrier film can provide substantial durability improvement. In another instance, during the above-mentioned solvent casting step, the polymer solution can be cast into a reinforcement or support material.
[0109] The substrate selection and direct casting can allow optimization of (e.g., minimization) of the thickness of the resulting reinforced aerogel material. This process can also be extended to the production of fiber reinforced polymer aerogels—internally reinforced polyimide aerogels are provided as an example. The process can include: (a) forming a polyamic acid solution from a mixture of dianhydride and diamine monomers in a polar solvent such as DMSO, DMAc, NMP, or DMF; (b) contacting the polyamic acid solution with chemical curing agents listed above and a chemical dehydrating agent to initiate chemical imidization; (c) casting the polyamic acid solution onto a fibrous support prior to gelation and allow it to permeate it; (d) allowing the catalyzed polyamic acid solution to gel around, and into, the fibrous support during chemical imidization; (e) optionally performing a solvent exchange, which can facilitate drying; and (f) removal of the transient liquid phase contained within the gel with supercritical, subcritical, or ambient drying to give an internally reinforced aerogel. The polyimide aerogels can be produced from aromatic dianhydride and diamine monomers, such as aromatic diamines or a mixture of at least one aromatic diamine monomer and at least one aliphatic diamine monomer. The resulting polyimide aerogel can be optimized to possess low density, narrow pore size distribution and good mechanical strength. The polyimide aerogel can also be optimized to include mesopores, micropores, or macropores, or any combination thereof or all such pore sizes.
[0110] The preparation of polyimide wet gels can be a two-step procedure: (a) formation of the polyamic acid solution from a mixture of dianhydride and diamine in a polar solvent such as DMAc, NMP, DMF, or DMSO; and (b) catalyzed cyclization with chemical catalyzing agents to form a polyimide. In some embodiments, at least 30 minutes mixing at room temperature can be performed to allow for formation of the polyimide polymer and yielding of stable, robust wet gels. Gelation conditions depend on several factors, including the prepared density of the solution and the temperature of the heating oven. Higher concentration solutions can gel faster than lower density solutions. Once the system has reached the gelled state, the gels are optionally rinsed repeatedly with acetone, ethanol, or the like. Rinsing occurs at least three times prior to drying, and serves to remove residual solvent and unreacted monomers. CO.sub.2 can then be used in techniques known to those in the art for wet solvent extraction to create the aerogel structure. Other techniques for preparing and optimizing polyimide aerogels can be used and are known in the art.
[0111] The reinforced macroporously structured aerogels of the present invention can be any width or length and can be in the form of defined geometry (e.g., a square or circular patch or any other stock shape), or in the form of a sheet or roll. In some instances, the internally reinforced aerogels can have a width up to 6 meters and a length of up to 10 meters, or from 0.01 to 6 meters, 0.5 to 5 meters, 1 to 4 meters, or any range in between, and a length of 1 to 10,000 meters, 5 to 1,000 meters, 10 to 100 meters or any range there between. The width of the composite can be 0.01, 0.05, 0.10, 0.15, 0.20, 0.25, 0.30, 0.35, 0.40, 0.45, 0.50, 0.55, 0.60, 0.65, 0.70, 0.75, 0.80, 0.85, 0.90, 0.95, 1.0, 1.5, 2.0, 2.5, 3.0, 3.5, 4.0, 4.5, 5.0, 5.5, 6.0 meters, including any value there between. The length of the internally reinforced aerogels can be 0.1, 1, 10, 100, 500, 1000, 1500, 2000, 2500, 3000, 3500, 4000, 4500, 5000, 5500, 6000, 6500, 7000, 7500, 8000, 8500, 9000, 9500, 10000 meters and include any value there between. In certain aspect the length of the internally reinforced aerogel can be 1000 meters, and 1.5 meters, respectively, in width. In a further embodiment the internally reinforced aerogel is 100 feet (30.5 meters) in length and 40 inches (1.0 meter) wide.
[0112] In certain embodiments the internally reinforced aerogel includes a non-woven support at least partially or fully embedded or incorporated in a polymeric aerogel.
[0113] The support can be comprised of a plurality of fibers. The fibers can be unidirectionally or omnidirectionally oriented. The support can include, by volume, at least 0.1 to 50% of the internally reinforced aerogel. The support can be in the form of a plurality of fibers, a film or layer of fibers, fiber containing films or layers, or a support film or layer comprising two or more fiber layers pressed together to form the support. The support can include cellulose fibers, glass fibers, carbon fibers, aramid fibers, thermoplastic fibers (e.g., polyethylene fibers, polyester, nylon, etc.), thermoset fibers (e.g., rayon, polyurethane, and the like), ceramic fibers, basalt fibers, rock wool, or steel fibers, or mixtures thereof. The fibers can have an average filament cross sectional area of 7 μm.sup.2 to 800 μm.sup.2, which equates to an average diameter of 3 to 30 microns for circular fibers. Bundles of various kinds of fibers can be used depending on the use intended for the internally reinforced aerogel. For example, the bundles may be of carbon fibers or ceramic fibers, or of fibers that are precursors of carbon or ceramic, glass fibers, aramid fibers, or a mixture of different kinds of fiber. Bundles can include any number of fibers. For example, a bundle can include 400, 750, 800, 1375, 1000, 1500, 3000, 6000, 12000, 24000, 50000, or 60000 filaments. The fibers can have a filament diameter of 5 to 24 microns, 10 to 20 microns, or 12 to 15 microns or any range there between, or 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21, 22, 23, 24 microns or any value there between. The fibers in a bundle of fibers can have an average filament cross sectional area of 7 μm.sup.2 to 800 μm.sup.2, which equates to an average diameter of 3 to 30 microns for circular fibers. Cellulose and paper supports can be obtained from Hirose Paper Mfg Co (Kochi, Japan) or Hirose Paper North America (Macon, Ga., USA).
[0114] Thermoplastic and thermoset fibers can include thermoplastic and/or thermoset polymers. Non-limiting examples of thermoplastic polymers include polyethylene terephthalate (PET), a polycarbonate (PC) family of polymers, polybutylene terephthalate (PBT), poly(1,4-cyclohexylidene cyclohexane-1,4-dicarboxylate) (PCCD), glycol modified polycyclohexyl terephthalate (PCTG), poly(phenylene oxide) (PPO), polypropylene (PP), polyethylene (PE), polyvinyl chloride (PVC), polystyrene (PS), polymethyl methacrylate (PMMA), polyethyleneimine or polyetherimide (PEI) and their derivatives, thermoplastic elastomer (TPE), terephthalic acid (TPA) elastomers, poly(cyclohexanedimethylene terephthalate) (PCT), polyethylene naphthalate (PEN), polyamide (PA), polysulfone sulfonate (PSS), sulfonates of polysulfones, polyether ether ketone (PEEK), polyether ketone (PEKK), acrylonitrile butyldiene styrene (ABS), polyphenylene sulfide (PPS), co-polymers thereof, polyesters or derivatives thereof, polyamides or derivatives thereof (e.g., nylon), or blends thereof.
[0115] Non-limiting examples of thermoset polymers include unsaturated polyester resins, polyurethanes, polyoxybenzylmethylenglycolanhydride (e.g., Bakelite), urea-formaldehyde, diallyl-phthalate, epoxy resin, epoxy vinylesters, polyimides, cyanate esters of polycyanurates, dicyclopentadiene, phenolics, benzoxazines, co-polymers thereof, or blends thereof.
[0116] In other aspects, the internally reinforced aerogel can includes two or more layers of a support. In certain instances, a support can include two unidirectional supports in contact with each other and arranged such that the unidirectional fibers are oriented in different directions to each other. In other instances, the support can comprises two or more layers of a support having omnidirectional fibers.
[0117] The support can be positioned at least partially or fully inside a polymeric aerogel, forming an internal support and an external aerogel. As used herein any support that is at least partially permeated with aerogel material can be partially internalized. The width and length of the aerogel can be substantially similar to the width and length of the internal or partially internalized support.
[0118]
[0119] In certain embodiments, a reinforced aerogel laminate can be constructed having 2, 3, 4, 5 or more reinforced aerogel layers (See
[0120] The cross-sectional thickness of the internally reinforced aerogel measured from top most edge to bottom most edge can be any value. In some embodiments the cross-sectional thickness is between 0.02 to 0.5 mm, including all values and ranges there between. The support can be positioned in the aerogel so that about 0, 0.001, 0.01, 0.025, 0.05, 0.075, 0.1, 0.125, 0.15, 0.175, 0.2, 0.225, 0.25, 0.275, 0.3, 0.325, 0.35, 0.375, 0.4 mm of the aerogel is above the support. In certain instances, the support can be approximately within about 0.5 mils (0.013 mm) of the aerogel midline. In a further aspect about 0.1 to 0.5 mil (0.0025 to 0.013 mm) of support extends beyond one of the aerogel edges with a portion of the support being embedded or incorporated in the aerogel.
[0121] The present invention will be described in greater detail by way of specific examples. The following examples are offered for illustrative purposes only, and are not intended to limit the invention in any manner. Those of skill in the art will readily recognize a variety of noncritical parameters, which can be changed or modified to yield essentially the same results.
[0122] 5. Formation of Polymeric Aerogel Particles
[0123] Once the aerogel films or stock/monolithic shapes are made, the films or shapes can then be milled, chopped, or machined into particles. The aerogel particles can be any size. In some embodiments, the aerogel particle size can be 1 μm to 500 μm, or at least, equal to, or between any two of 1, 2, 3, 4, 5, 10 20, 30, 40, 50, 60, 70, 80, 90, 100, 150, 200, 250, 300, 350, 400, 450 and 500 μm. In some embodiments, the particle size distribution can be single-modal or multi-modal (e.g., bimodal, trimodal, etc.). In certain embodiments, the particle size distribution is bimodal with one mode being between 10 and 100 μm and the other mode being between 150 and 300 μm. Alternatively, the aerogel particles can be purchased (see above non-limiting commercially available options).
EXAMPLES
[0124] The present invention will be described in greater detail by way of specific examples. The following examples are offered for illustrative purposes only, and are not intended to limit the invention in any manner. Those of skill in the art will readily recognize a variety of noncritical parameters, which can be changed or modified to yield essentially the same results.
[0125] Table 2 lists the acronyms for the compounds used in the following Examples.
TABLE-US-00002 TABLE 2 Acronym Name BPDA 3,3′,4,4′-biphenyltetracarboxylic dianhydride DMB 4,4′-Diamino-2,2′-dimethylbiphenyl DMSO Dimethylsulfoxide PA Phthalic anhydride PMDA Pyromellitic dianhydride ODA 4,4′-Oxydianiline TAPOB 1,3,5-Tris(4-aminophenoxy) benzene
Structures of the starting materials are shown below.
##STR00001##
Example 1
Preparation of a Highly Branched BPDA/DMB-ODA Polyimide
[0126] A reaction vessel with a mechanical stirrer and a water jacket was used. The flow of the water through the reaction vessel jacket was adjusted to maintain temperature in the range of 18-35° C. The reaction vessel was charged with DMSO (108.2 lbs. 49.1 kg), and the mechanical stirrer speed was adjusted to 120-135 rpm. TAPOB (65.13 g) was added to the solvent. To the solution was added DMB (1081.6 g), followed by ODA (1020.2 g). A first portion of BPDA (1438.4 g) was then added. After stirring for 20 minutes, a sample of the reaction mixture was analyzed for viscosity using a Brookfield DV1 viscometer (Brookfield, AMETEK, U.S.A.). A second portion of BPDA (1407.8 g) was added, and the reaction mixture was stirred for 20 additional minutes. A third portion of BPDA (138.62 g) was added, and the reaction mixture was stirred for 20 minutes. A sample of the reaction mixture was analyzed for viscosity. After stirring for 8 hours, PA (86.03 g) was added. The resulting reaction mixture was stirred until no more solids were visible. After 2 hours, the product was removed from the reaction vessel, filtered, and weighed.
Example 2
Preparation of a Highly Branched Polyimide Aerogel Monolith by Freeze Drying
[0127] The resin (about 10,000 grams) prepared in Example 1 was mixed with triethylamine (about 219 grams) and acetic anhydride (about 561 grams) for five minutes. After mixing, the resultant solution was poured into a square 15″×15″ mold and left for 48 hours. The gelled shape was removed from the mold, and placed into an acetone bath. After immersion for 24 hours, the acetone bath was exchanged with fresh acetone. The soak and exchange process was repeated five times. After the final exchange, the bath was replaced with tertiary butyl alcohol. After immersion for 24 hours, the tertiary butyl alcohol bath was exchanged for fresh tertiary butyl alcohol. The soak and exchange process was repeated three times The part was subsequently flash frozen and subjected to subcritical drying for 96 hours in at 5° C., followed by drying in vacuum at 50° C. for 48 hours. The final recovered aerogel part had open-cell structure as observed by scanning electron microscopy (SEM) performed on a Phenom Pro Scanning Electron Microscope (Phenom-World, the Netherlands), exhibited a density of 0.22 g/cm.sup.3 and porosity of 88.5% as measured according to ASTM D4404-10 with a Micromeritics® AutoPore V 9605 Automatic Mercury Penetrometer (Micromeritics® Instrument Corporation, U.S.A.), a compression modulus of 2.2 MPa as determined by American Standard Testing Method (ASTM) D395-16, and a compression strength at 25% strain of 3.5 MPa as determined by ASTM D395-16. The distribution of pore sizes was measured according to ASTM D4404-10 using a Micromeritics® AutoPore V 9605 Automatic Mercury Penetrometer (Micromeritics® Instrument Corporation, U.S.A.), and the distribution of pore diameters is provided in
Example 3
Preparation of a Highly Branched Polyimide Aerogel Monolith by Thermal Drying
[0128] The resin (about 10,000 grams) prepared in Example 1 was mixed with triethylamine (about 219 grams) and acetic anhydride (about 561 grams) for five minutes at a temperature of 10-35° C. After mixing, the resultant solution was poured into a square 15″×15″ mold and left for 48 hours. The gelled shape was removed from the mold and placed into an acetone bath. After immersion for 24 hours, the acetone bath was exchanged with fresh acetone. The soak and exchange process was repeated five times. After the final exchange, the part was dried with an ambient (about 20 to 30° C.) drying process to evaporate a majority of the acetone over 48 hours followed by thermal drying at 50° C. for 4 hours, 100° C. for 2 hours, 150° C. for 1 hour, and then 200° C. for 30 minutes. The final recovered aerogel had similar properties as observed in Example 2.
Example 4
Preparation of a Highly Branched Polyimide
[0129] TAPOB (about 2.86 g) was added to the reaction vessel charged with about 2,523.54 g DMSO as described in Example 1 at a temperature of 18-35° C. To the solution was added a first portion of DMB (about 46.75 g), followed by a first portion of ODA (about 44.09 g). After stirring for about 20 minutes, a first portion of BPDA (about 119.46 g) was added. After stirring for about 20 minutes, TAPOB (about 2.86 g), DMB (about 46.75 g), and ODA (about 44.09 g) were added. After stirring for about 20 minutes, BPDA (about 119.46 g) was added. After stirring for about 20 minutes, TAPOB (about 2.86 g), DMB (about 46.75 g), and ODA (about 44.09 g) were added. After stirring for about 20 minutes, BPDA (about 119.46 g) was added. After stirring for about 8 hours, PA (about 50.12 g) was added. The resulting reaction mixture was stirred until no more solids were visible. After about 2 hours, the product was removed from the reaction vessel, filtered, and weighed.
Example 5
Preparation of a Highly Branched Polyimide Aerogel Monolith by Freeze Drying
[0130] The resin (about 400 grams) prepared in Example 4 was mixed with 2-methylimidazole (about 53.34 grams) for five minutes and then benzoic anhydride (about 161.67 grams) for five minutes at a temperature of 18-35° C. After mixing, the resultant solution was poured into a square 3″×3″ mold and placed in an oven at 75° C. for 30 minutes and then left overnight at room temperature. The gelled shape was removed from the mold, and placed into an acetone bath. After immersion for 24 hours, the acetone bath was exchanged with fresh acetone. The soak and exchange process was repeated five times. After the final exchange, the bath was replaced with tertiary butyl alcohol. After immersion for 24 hours, the tertiary butyl alcohol bath was exchanged for fresh tertiary butyl alcohol. The soak and exchange process was repeated three times The part was subsequently frozen on a shelf freezer, and subjected to subcritical drying for 96 hours in at 5° C., followed by drying in vacuum at 50° C. for 48 hours. The final recovered aerogel part had open-cell structure as observed by scanning electron microscopy (SEM) performed on a Phenom Pro Scanning Electron Microscope (Phenom-World, the Netherlands), exhibited a density of 0.15 g/cm.sup.3 and porosity of 92.2% as measured according to ASTM D4404-10 with a Micromeritics® AutoPore V 9605 Automatic Mercury Penetrometer (Micromeritics® Instrument Corporation, U.S.A.). The distribution of pore sizes were measured according to ASTM D4404-10 using a Micromeritics® AutoPore V 9605 Automatic Mercury Penetrometer (Micromeritics® Instrument Corporation, U.S.A.), and the distribution of pore diameters is shown in
Example 6
Preparation of a Highly Branched Polyimide
[0131] TAPOB (about 2.05 g) was added to the reaction vessel charged with about 2,776.57 g DMSO as described in Example 1 at a temperature of 18-35° C. To the solution was added a first portion of DMB (about 33.54 g), followed by a first portion of ODA (about 31.63 g). After stirring for about 20 minutes, a first portion of PMDA (about 67.04 g) was added. After stirring for about 20 minutes, TAPOB (about 2.05 g), DMB (about 33.54 g), and ODA (about 31.63 g) were added. After stirring for about 20 minutes, PMDA (about 67.04 g) was added. After stirring for about 20 minutes, TAPOB (about 2.05 g), DMB (about 33.54 g), and ODA (about 31.63 g) were added. After stirring for about 20 minutes, PMDA (about 67.04 g) was added. After stirring for about 8 hours, PA (about 18.12 g) was added. The resulting reaction mixture was stirred until no more solids were visible. After about 2 hours, the product was removed from the reaction vessel, filtered, and weighed.
Example 7
Preparation of a Highly Branched Polyimide Aerogel Monolith by Freeze Drying
[0132] The resin (about 400 grams) prepared in Example 6 was mixed with 2-methylimidazole (about 40.38 grams) for five minutes and then benzoic anhydride (about 122.38 grams) for five minutes at a temperature of 18-35° C. After mixing, the resultant solution was poured into a square 3″×3″ mold and placed in an oven at 75° C. for 30 minutes and then left overnight at room temperature. The gelled shape was removed from the mold, and placed into an acetone bath. After immersion for 24 hours, the acetone bath was exchanged with fresh acetone. The soak and exchange process was repeated five times. After the final exchange, the bath was replaced with tertiary butyl alcohol. After immersion for 24 hours, the tertiary butyl alcohol bath was exchanged for fresh tertiary butyl alcohol. The soak and exchange process was repeated three times The part was subsequently frozen on a shelf freezer, and subjected to subcritical drying for 96 hours in at 5° C., followed by drying in vacuum at 50° C. for 48 hours. The final recovered aerogel part had open-cell structure as observed by scanning electron microscopy (SEM) performed on a Phenom Pro Scanning Electron Microscope (Phenom-World, the Netherlands), exhibited a density of 0.23 g/cm.sup.3 and porosity of 82.7% as measured according to ASTM D4404-10 with a Micromeritics® AutoPore V 9605 Automatic Mercury Penetrometer (Micromeritics® Instrument Corporation, U.S.A.). The distribution of pore sizes was measured according to ASTM D4404-10 using a Micromeritics® AutoPore V 9605 Automatic Mercury Penetrometer (Micromeritics® Instrument Corporation, U.S.A.), and the distribution of pore diameters is shown in
Example 8
Preparation of a Highly Branched Polyamic Film
[0133] A reaction vessel with a mechanical stirrer and a water jacket was employed. The flow of the water through the reaction vessel jacket was adjusted to maintain temperature in the range of 20-28° C. The reaction vessel was charged with DMSO (108.2 lbs. 49.1 kg), and the mechanical stirrer speed was adjusted to 120-135 rpm. TAPOB (65.03 g) was added to the solvent. To the solution was added DMB (1,080.96 g), followed by ODA (1,018.73 g). A first portion of BPDA (1,524.71 g) was added. After stirring for 20 minutes, a sample of the reaction mixture was analyzed for viscosity. A second portion of BPDA (1,420.97 g) was added, and the reaction mixture was stirred for 20 additional minutes. A sample of the reaction mixture was analyzed for viscosity. A third portion of BPDA (42.81 g) was added, and the reaction mixture was stirred for 20 additional minutes. A sample of the reaction mixture was analyzed for viscosity. After stirring for 8 hours, PA (77.62 g) was added. The resulting reaction mixture was stirred until no more solid was visible. After 2 hours, the resin was removed from the reaction vessel, filtered, and weighed.
[0134] The resin (10,000 grams) was mixed with 2-methylimidazole (250 grams) for five minutes. Benzoic anhydride (945 grams) was added, and the solution mixed an additional five minutes. After mixing, the resultant solution was poured onto a moving polyester substrate that was heated in an oven at 100° C. for 30 seconds. The gelled film was collected and placed into an acetone bath. After immersion for 24 hours, the acetone bath was exchanged for fresh acetone. The soak and exchange process was repeated six times. After the final exchange, the gelled film was removed. The acetone solvent was evaporated under a stream of air at room temperature, and subsequently dried for 2 hrs hours at 200° C. The final recovered aerogel part had open-cell structure as observed by scanning electron microscopy (SEM) performed on a Phenom Pro Scanning Electron Microscope (Phenom-World, the Netherlands), exhibited a density of 0.20 g/cm.sup.3 and porosity of >80% as measured according to ASTM D4404-10 with a Micromeritics® AutoPore V 9605 Automatic Mercury Penetrometer (Micromeritics® Instrument Corporation, U.S.A.). The final recovered film exhibited a tensile strength and elongation of 1200 psi (8.27 MPa) and 14%, respectively, at room temperature as measured according to ASTM D882-02. The film had an average pore size of 400 nm.
Example 9
Preparation of Air Filter Materials and Masks
[0135] AeroZero® rolled thin film (Blueshift Materials, Inc., Spencer, Mass.) having a thickness of 165 microns was used as the air-permeable filter material. A 50 micron thick AeroZero® rolled thin film, a 125 micron thick AeroZero® rolled thin film, a 250 micron thick AeroZero® rolled thin film, and other AeroZero® rolled thin films are also available from Blueshift Materials, Inc., and can also be used in the context of the present invention. The AeroZero® rolled thin films are polyimide aerogels that can be made by the processes described throughout this specification. The thickness of the film can be modified as desired for a given air filter application or product. The rolled thin film was then adhesively attached to a Nomex® fiber scrim (DuPont, Wilmington, Del.). The Nomex® fiber scrim was Meta-Aramid Scrim 69 (obtained from Infiniti TechTex, Mumbai, India). The adhesive was a polyester-based adhesive (Bostik HM4199MV, Bostik Inc., Wauwatusa, Wis.). The following process can be used to make the air-permeable filter: (1) immerse the Nomex® fiber scrim in the polyester-based adhesive; and (2) then press together the loaded scrim with the AeroZero® rolled thin film using a mechanical roll nip set to approximately 10 pounds per square inch pressure and a feed rate of approximately 5 feet per minute.
Example 10
Preparation of Air Filter Materials and Masks
[0136]
[0137]
[0138]
Example 11
Prophetic Example for Testing
Air-Permeable Filter Materials of the Present Invention
[0139] The air-permeable filter materials of the present invention can be subjected to tests to determine the efficiency of any given parameter. Non-limiting tests that can be used in the context of the present invention include any one of, any combination of, or all of: [0140] (1) Bacterial filtration efficiency can be measured according to ASTM F2101 as the percent of bacteria (e.g., Staphylococcus aureus) collected downstream of an air-permeable filter material of the present invention versus the bacteria provided upstream of the air-permeable filter material of the present invention in an aerosol initially comprising 1 million bacterial units at a face velocity of 12.5 cm/s and a flow rate of 30 liters per minute over an area of 40 cm.sup.2. [0141] (2) Viral filtration efficiency can be measured according to ASTM F2101 as the percent of viruses (e.g., Phi X174 bacteriophase) collected downstream of the air-permeable filter material of the present invention versus the viruses provided upstream of the air-permeable filter material of the present invention in an aerosol initially comprising 107 plaque-forming units of the virus at a flow rate of 30 liters per minute and face velocity of 12.5 cm/s over an area of 40 cm.sup.2. [0142] (3) Sub-micron particulate filtration efficiency can be measured according to ASTM F1215 (e.g., using 0.1 micron Latex spheres). [0143] (4) Inhalation and exhalation resistance can be measured according to ASTM F2100-Standard Specification For Performance of Materials Used In Medical face Masks.