FIELD OF THE DISCLOSURE

This disclosure relates to electret webs, including non-woven fibrous webs such as non-woven thermoplastic microfiber webs, containing charge-enhancing additives and uses thereof.

BACKGROUND

An electret is a dielectric material exhibiting a quasi-permanent electrical charge. Electrets are useful in a variety of devices including, e.g. cling films, air filters, filtering facepieces, and respirators, and as electrostatic elements in electro-acoustic devices such as microphones, headphones, and electrostatic recorders.

The performance of microfibrous webs used for aerosol filtration can be improved by imparting an electrical charge to the fibers, forming an electret material. In particular, electrets are effective in enhancing particle capture in aerosol filters. A number of methods are known for forming electret materials in microfibrous webs. Such methods include, for example, bombarding melt-blown fibers as they issue from the die orifices, as the fibers are formed, with electrically charged particles such as electrons or ions. Other methods include, for example, charging the fibers after the web is formed, by means of a DC corona discharge or imparting a charge to the fiber mat by means of carding and/or needle tacking (tribocharging). Recently, a method in which jets of water or a stream of water droplets impinge on a non-woven web at a pressure sufficient to provide filtration enhancing electret charge has been described (hydrocharging).

SUMMARY

Presented in this disclosure are electret webs containing charge-enhancing additives. These charge-enhancing additives provide electret webs that are easy to charge by a variety of different charging mechanisms such as hydrocharging or a combination of DC corona discharge and hydrocharging.

In some embodiments described herein, the electret web comprises a thermoplastic resin and a charge-enhancing additive comprising an N-substituted amino carbocyclic aromatic material. The electret web may be in the form of a non-woven fibrous web or even a non-woven microfiber web.

In other embodiments described herein, an electret filter medium comprises a non-woven microfiber web comprising a blend of a thermoplastic resin and a charge-enhancing additive comprising an N-substituted amino carbocyclic aromatic material. The electret filter media may comprise a respirator filter, a room ventilation system filter, a vehicle ventilation system filter, an air conditioner filter, a furnace filter, a room air purifier filter, a vacuum cleaner filter, or a computer disk drive filter.

Also disclosed are methods for preparing an electret web comprising providing a thermoplastic material; providing a charge-enhancing additive comprising an N-substituted amino carbocyclic aromatic material; hot melt mixing the thermoplastic material and the charge-enhancing additive to form a thermoplastic blend; and melt blowing the thermoplastic blend to form a microfiber web, and charging the web.

DETAILED DESCRIPTION

Electret webs useful in the present disclosure include a blend of a thermoplastic resin and a charge-enhancing additive. Webs prepared from such blends can show enhanced properties over webs prepared with the thermoplastic resins alone. Useful charge-enhancing additives include N-substituted amino carbocyclic aromatic materials.

The electret webs may be in a variety of forms. For example the web may be a continuous or discontinuous film, or a fibrous web. Fibrous webs are particularly useful for the formation of filtration media. In some embodiments the web is a non-woven microfibrous web. Typically microfibers are 1-100 micrometers in average diameter and the microfibers need not have a circular cross-section.

The terms â€œaâ€ , â€œanâ€ , and â€œtheâ€ are used interchangeably with â€œat least oneâ€ to mean one or more of the elements being described.

The term â€œalkylâ€ refers to a monovalent group that is a radical of an alkane, which is a saturated hydrocarbon. The alkyl can be linear, branched, cyclic, or combinations thereof and typically has 1 to 20 carbon atoms. In some embodiments, the alkyl group contains 1 to 18, 1 to 12, 1 to 10, 1 to 8, 1 to 6, or 1 to 4 carbon atoms. Examples of alkyl groups include, but are not limited to, methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, tert-butyl (t-butyl), n-pentyl, n-hexyl, cyclohexyl, n-heptyl, n-octyl, and ethylhexyl.

The term â€œalkenylâ€ refers to a monovalent group that is a radical of an alkene, which is a hydrocarbon with at least one carbon-carbon double bond. The alkenyl can be linear, branched, cyclic, or combinations thereof and typically contains 2 to 20 carbon atoms. In some embodiments, the alkenyl contains 2 to 18, 2 to 12, 2 to 10, 4 to 10, 4 to 8, 2 to 8, 2 to 6, or 2 to 4 carbon atoms. Exemplary alkenyl groups include ethenyl, n-propenyl, and n-butenyl.

The term â€œalkynylâ€ refers to a monovalent group that is a radical of an alkyne, which is a hydrocarbon with at least one carbon-carbon triple bond. The alkynyl can be linear, branched, cyclic, or combinations thereof and typically contains 2 to 20 carbon atoms. In some embodiments, the alkynyl contains 2 to 18, 2 to 12, 2 to 10, 4 to 10, 4 to 8, 2 to 8, 2 to 6, or 2 to 4 carbon atoms. Exemplary alkynyl groups include ethynyl, n-propynyl, and n-butynyl.

The term â€œheteroalkylâ€ refers to an alkyl group which contains heteroatoms. These heteroatoms may be pendant atoms, for example, halogens such as fluorine, chlorine, bromine, or iodine or catenary atoms such as nitrogen, oxygen or sulfur. An example of a heteroalkyl group is a polyoxyalkyl group such as â€”CH₂CH₂(OCH₂CH₂)_nOCH₂CH₃.

The term â€œsubstituted alkylâ€ refers to an alkyl group which contains substituents along the hydrocarbon backbone. These substituents may be alkyl groups, heteroalkyl groups or aryl groups. An example of a substituted alkyl group is a benzyl group.

The term â€œarylâ€ refers to an aromatic carbocyclic group that is a radical containing 1 to 5 rings which may be connected or fused. The aryl group may be substituted with alkyl or heteroalkyl groups. Examples of aryl groups include phenyl groups, naphthalene groups and anthracene groups.

The term â€œN-substituted amino carbocyclic aromaticâ€ refers to a carbocyclic group, i.e. a cyclic group in which the ring structure contains only carbon and hydrogen atoms, that is a radical containing 1 to 5 rings which may be connected or fused, and is substituted with at least one substituted amino group. A substituted amino group is a group of the type â€”NR¹R²where the group R¹is hydrogen, alkyl, alkenyl, alkynyl, aryl, heteroalkyl or substituted alkyl, and the group R²is alkyl, alkenyl, alkynyl, aryl, heteroalkyl or substituted alkyl.

The terms â€œpolymerâ€ and â€œpolymeric materialâ€ refer to both materials prepared from one monomer such as a homopolymer or to materials prepared from two or more monomers such as a copolymer, terpolymer, or the like. Likewise, the term â€œpolymerizeâ€ refers to the process of making a polymeric material that can be a homopolymer, copolymer, terpolymer, or the like. The terms â€œcopolymerâ€ and â€œcopolymeric materialâ€ refer to a polymeric material prepared from at least two monomers.

The terms â€œroom temperatureâ€ and â€œambient temperatureâ€ are used interchangeably to mean temperatures in the range of 20Â° C. to 25Â° C.

The term â€œhot melt processableâ€ as used herein, refers to a composition that can transform, for example, by heat and pressure from a solid to a viscous fluid. The composition should be capable of being hot melt processed without being substantially chemically transformed, degraded or rendered unusable for the intended application.

Unless otherwise indicated, all numbers expressing feature sizes, amounts, and physical properties used in the specification and claims are to be understood as being modified in all instances by the term â€œabout.â€ Accordingly, unless indicated to the contrary, the numbers set forth are approximations that can vary depending upon the desired properties using the teachings disclosed herein.

Thermoplastic resins useful in the present disclosure include any thermoplastic nonconductive polymer capable of retaining a high quantity of trapped electrostatic charge when formed into a web and charged. Typically, such resins have a DC (direct current) resistivity of greater than 10¹⁴ohm-cm at the temperature of intended use. Polymers capable of acquiring a trapped charge include polyolefins such as polypropylene, polyethylene, and poly-4-methyl-1-pentene; polyvinyl chloride; polystyrene; polycarbonates; polyesters, including polylactides; and perfluorinated polymers and copolymers. Particularly useful materials include polypropylene, poly-4-methyl-1-pentene, blends thereof or copolymers formed from at least one of propylene and 4-methyl-1-pentene.

The charge-enhancing additives are N-substituted amino carbocyclic aromatic materials. Typically the charge-enhancing additives are thermally stable making them suitable for use in hot melt processable compositions. The N-substituted amino carbocyclic aromatic materials may be generally described by Formula I:

R¹R²Nâ€”Ar(G)_nâ€ƒâ€ƒFormula I

where Ar is an aryl group, the group R¹is hydrogen, alkyl, alkenyl, alkynyl, aryl, heteroalkyl or substituted alkyl and the group R²is alkyl, alkenyl, alkynyl, aryl, heteroalkyl or substituted alkyl, n is an integer representing the number of substituent positions on the N-substituted amino aryl group, and G represents the substituents on the N-substituted amino aryl group, each G may independently be hydrogen, alkyl, alkenyl, alkynyl, aryl, heteroalkyl, substituted alkyl, or â€”NR³R⁴where R³is hydrogen, alkyl, alkenyl, alkynyl, aryl, heteroalkyl or substituted alkyl and the group R⁴is alkyl, alkenyl, alkynyl, aryl, heteroalkyl or substituted alkyl. In some embodiments, Ar of Formula I is a phenyl group and n is 5. In other embodiments, Ar of Formula I is a naphthalene group and n is 7. In other embodiments, Ar of Formula I is an anthracene group and n is 9.

One useful class of N-substituted amino carbocyclic aromatic materials are those described by Formula II where Z¹and Z²are independently hydrogen, alkyl, alkenyl, alkynyl, aryl, heteroalkyl or â€”NR³R⁴where R³is hydrogen, alkyl, alkenyl, alkynyl, aryl, heteroalkyl or substituted alkyl and the group R⁴is alkyl, alkenyl, alkynyl, aryl, heteroalkyl or substituted alkyl. The group R¹is hydrogen, alkyl, alkenyl, alkynyl, aryl, heteroalkyl or substituted alkyl and the group R²is alkyl, alkenyl, alkynyl, aryl, heteroalkyl or substituted alkyl. The groups Z¹and Z²may be located anywhere on the carbocyclic aromatic ring but typically are located in the 3,5 positions relative to the substituted amino group.

[Image Omitted]

One class of suitable charge-enhancing additive included in the materials described by Formula II, includes, for example, ones in which the groups Z¹and Z²are â€”NR³R⁴groups located at the 3 and 5 positions of the aromatic ring, where R³is hydrogen, alkyl, alkenyl, alkynyl, aryl, heteroalkyl or substituted alkyl and the group R⁴is alkyl, alkenyl, alkynyl, aryl, heteroalkyl or substituted alkyl. In some instances, the substitution on the aromatic ring is symmetrical, meaning that each of the groups â€”NRâ€²R²and Z¹and Z²(if present) are the same. In some embodiments, R¹is a hydrogen and R²is an aryl group. Typically R²is a substituted aryl group, where the substituent is an alkyl group with 1-25 carbon atoms. In some embodiments, R²is a phenyl group substituted with an alkyl group with 1-4 carbon atoms. In other embodiments, R²is a phenyl group substituted with an alkyl group with 5-25 carbon atoms, or 10-25 carbon atoms or even 12-25 carbon atoms. In some of these embodiments, Z¹and Z²are â€”NR³R⁴groups where R³is the same as R¹and R⁴is the same as R². Examples of two such charge-enhancing additives are shown as Formula III and Formula IV below:

[Image Omitted]

Another suitable class of charge-enhancing additive included in the materials described by Formula II, includes, for example, ones in which the group Z¹is a hydrogen and the group Z²is â€”NR³R⁴, where R¹and R³are hydrogens and R²and R⁴are aryl groups. Typically R²and R⁴are substituted aryl groups, where the substituents are alkyl groups with 1-25 carbon atoms. In some embodiments, R²and R⁴are phenyl groups substituted with alkyl groups with 1-4 carbon atoms. In other embodiments, R²and R⁴are phenyl groups substituted with alkyl groups with 5-25 carbon atoms, or 10-25 carbon atoms or even 12-25 carbon atoms. An example of such a charge-enhancing additive is shown as Formula V below:

[Image Omitted]

Another useful class of the N-substituted amino carbocyclic aromatic materials described by Formula I, are those in which Ar is a naphthalene ring, n is 7, each G is hydrogen, R¹is a hydrogen and R²is an aryl group. Typically R²is a substituted aryl group, where the substituent is an alkyl group with 1-25 carbon atoms. In some embodiments, R²is a phenyl group substituted with an alkyl group with 5-25 carbon atoms, or 10-25 carbon atoms or even 12-25 carbon atoms. An example of such a charge-enhancing additive is shown as Formula VI below:

[Image Omitted]

Typically the charge-enhancing additive is present in a thermoplastic resin and charge-enhancing additive blend in amounts in the range of 0.1 to 5% by weight based upon the total weight of the blend. In some embodiments, the charge-enhancing additive is present in an amount ranging from 0.1 to 3% by weight or 0.25 to 2% by weight.

The blend of the thermoplastic resin and the charge-enhancing additive can be prepared by well-known methods. Typically, the blend is processed using melt extrusion techniques, so the blend may be preblended to form pellets in a batch process, or the thermoplastic resin and the charge-enhancing additive may be mixed in the extruder in a continuous process. Where a continuous process is used, the thermoplastic resin and the charge-enhancing additive may be pre-mixed as solids or added separately to the extruder and allowed to mix in the molten state.

Examples of melt mixers that may be used to form preblended pellets include those that provide dispersive mixing, distributive mixing, or a combination of dispersive and distributive mixing. Examples of batch methods include those using a BRABENDER (e.g. a BRABENDER PREP CENTER, commercially available from C.W. Brabender Instruments, Inc.; South Hackensack, N.J.) or BANBURY internal mixing and roll milling equipment (e.g. equipment available from Farrel Co.; Ansonia, Conn.). After batch mixing, the mixture created may be immediately quenched and stored below the melting temperature of the mixture for later processing.

Examples of continuous methods include single screw extruding, twin screw extruding, disk extruding, reciprocating single screw extruding, and pin barrel single screw extruding. The continuous methods can include utilizing both distributive elements, such as cavity transfer mixers (e.g. CTM, commercially available from RAPRA Technology, Ltd.; Shrewsbury, England) and pin mixing elements, static mixing elements or dispersive mixing elements (commercially available from e.g., MADDOCK mixing elements or SAXTON mixing elements).

Examples of extruders that may be used to extrude preblended pellets prepared by a batch process include the same types of equipment described above for continuous processing. Useful extrusion conditions are generally those which are suitable for extruding the resin without the additive.

The extruded blend of thermoplastic resin and charge-enhancing additive may be cast or coated into films or sheets or may be melt-blown into non-woven fibrous webs using known techniques. Melt-blown, non-woven microfibrous webs are particularly useful as filtration media.

Melt-blown, non-woven microfibrous electret filters are especially useful as an air filter element of a respirator, such as a filtering facepiece, or for such purposes as home and industrial air-conditioners, air cleaners, vacuum cleaners, medical air line filters, and air conditioning systems for vehicles and common equipment, such as computers, computer disk drives and electronic equipment. In respirator uses, the electret filters may be in the form of molded or folded half-face respirators, replaceable cartridges or canisters, or prefilters.

Melt-blown microfibers useful in the present disclosure can be prepared as described in Van A. Wente, â€œSuperfine Thermoplastic Fibers,â€ Industrial Engineering Chemistry, vol. 48, pp. 1342-1346 and in Report No. 4364 of the Naval Research Laboratories, published May 25, 1954, entitled â€œManufacture of Super Fine Organic Fibersâ€ by Van A. Wente et al.

Useful melt-blown microfibers for fibrous electret filters typically have an effective fiber diameter of from about 3 to 30 micrometers, in some embodiments from about 7 to 15 micrometers, as calculated according to the method set forth in Davies, C. N., â€œThe Separation of Airborne Dust and Particles,â€ Institution of Mechanical Engineers, London, Proceedings 1B, 1952.

Staple fibers may also be present in the web. The presence of staple fibers generally provides a more lofty, less dense web than a web of only blown microfibers. Preferably, no more than about 90 weight percent staple fibers are present, more preferably no more than about 70 weight percent. Examples of webs containing staple fiber are disclosed in U.S. Pat. No. 4,118,531 (Hauser).

Sorbent particulate material such as activated carbon or alumina may also be included in the web. Such particles may be present in amounts up to about 80 volume percent of the contents of the web. Examples of particle-loaded webs are described, for example, in U.S. Pat. No. 3,971,373 (Braun), U.S. Pat. No. 4,100,324 (Anderson) and U.S. Pat. No. 4,429,001 (Kolpin et al.).

Various optional additives can be blended with the thermoplastic composition including, for example, pigments, UV stabilizers, antioxidants and combinations thereof. Additionally, other types of charge-enhancing additives may added if desired, as long as they do not interfere with the function of the N-substituted amino carbocyclic aromatic material.

The electret filter media prepared according to the present disclosure generally have a basis weight in the range of about 10 to 500 g/m², and in some embodiments, about 10 to 100 g/m². In making melt-blown microfiber webs, the basis weight can be controlled, for example, by changing either the collector speed or the die throughput. The thickness of the filter medium is typically about 0.25 to 20 millimeters, and in some embodiments, about 0.5 to 2 millimeters. Multiple layers of fibrous electret webs are commonly used in filter elements. The solidity of the fibrous electret web typically is about 1% to 25%, more typically about 3% to 10%. Solidity is a unitless parameter that defines the solids fraction of the web. Generally the methods of this disclosure provide electret webs with generally uniform charge distribution throughout the web without regard to basis weight, thickness, or solidity of the medium. The electret filter medium and the resin from which it is produced should not be subjected to any unnecessary treatment which might increase its electrical conductivity, e.g., exposure to ionizing radiation, gamma rays, ultraviolet irradiation, pyrolysis, oxidation, etc.

The electret web may be charged as it is formed or the web may be charged after the web is formed. In electret filter media, the medium is generally charged after the web is formed. In general, any standard charging method known in the art may be used. For example, charging may be carried out in a variety of ways, including hydrocharging. A combination of DC corona discharge and hydrocharging may also be used.

Examples of suitable DC corona discharge processes are described in U.S. Pat. Re. No. 30,782 (van Turnhout), U.S. Pat. Re. No. 31,285 (van Turnhout), U.S. Pat. Re. No. 32,171 (van Turnhout), U.S. Pat. No. 4,215,682 (Davis et al.), U.S. Pat. No. 4,375,718 (Wadsworth et al.), U.S. Pat. No. 5,401,446 (Wadsworth et al.), U.S. Pat. No. 4,588,537 (Klaase et al.), and U.S. Pat. No. 4,592,815 (Nakao).

Hydrocharging of the web is carried out by impinging jets of water or a stream of water droplets onto the web at a pressure sufficient to provide the web with filtration enhancing electret charge. The pressure necessary to achieve optimum results varies depending on the type of sprayer used, the type of polymer from which the web is formed, the type and concentration of additives to the polymer, the thickness and density of the web and whether pre-treatment, such as DC corona surface treatment, was carried out prior to hydrocharging. Generally, pressures in the range of about 10 to 500 psi (69 to 3450 kPa) are suitable.

The jets of water or stream of water droplets can be provided by any suitable spray means. An apparatus useful for hydraulically entangling fibers is generally useful in the method of the present disclosure, although operation is carried out at lower pressures in hydrocharging than generally used in hydroentangling. Hydrocharging is understood to include the method described in U.S. Pat. No. 5,496,507 (Angadjivand) and other various derivative methods for imparting an electret charge using the fluid wetting and dewetting process as described in, for example, Japanese Patent Application Number JP 2002161467 (Horiguchi), Japanese Patent Application Number JP 2002173866 (Takeda), Japanese Patent Application Number JP 2002115177 (Takeda), Japanese Patent Application Number JP 2002339232 (Takeda), Japanese Patent Application Number JP 2002161471 (Takeda), Japanese Pat. No. 3,780,916 (Takeda), Japanese Patent Application Number JP 2002115178 (Takeda), Japanese Patent Application Number JP 2003013359 (Horiguchi), U.S. Pat. No. 6,969,484 (Horiguchi), U.S. Pat. No. 6,454,986 (Eitzman), Japanese Patent Application Number JP 2004060110 (Masumori), Japanese Patent Application Number JP 2005131485 (Kodama), and Japanese Patent Application Number JP 2005131484 (Kodama).

To model filtration performance, a variety of filtration testing protocols have been developed. These tests include measurement of the aerosol penetration of the filter web using a standard challenge aerosol such as dioctylphthalate (DOP), which is usually presented as percent of aerosol penetration through the filter web (% Pen) and measurement of the pressure drop across the filter web (Î”P). From these two measurements, a quantity known as the quality factor (QF) may be calculated by the following equation:

QF=âˆ’ln(% Pen/100)/Î”P,

where ln stands for the natural logarithm. A higher QF value indicates better filtration performance, and decreased QF values effectively correlate with decreased filtration performance. Details for measuring these values are presented in the Examples section. Typically, the filtration media of this disclosure have measured QF values of 0.3 or greater at a face velocity of 6.9 centimeters per second.

EXAMPLES

These examples are merely for illustrative purposes only and are not meant to be limiting on the scope of the appended claims. All parts, percentages, ratios, etc. in the examples and the rest of the specification are by weight, unless noted otherwise. Solvents and other reagents used were obtained from Sigma-Aldrich Chemical Company; Milwaukee, Wis. unless otherwise noted.

Table of AbbreviationsAbbreviation orTradeDesignationDescriptionCharge-1,3,5-tris(4-n-dodecylanilino)benzene, the synthesisEnhancingis shown in the Syntheses Examples section as SE-1.Additive-1Charge-1,3,5-tris(4-n-butylanilino)benzene, the synthesisEnhancingis shown in the Syntheses Examples section as SE-2.Additive-2Charge-1,3-bis(4-n-dodecylanilino)benzene, the synthesisEnhancingis shown in the Syntheses Examples section as SE-3.Additive-3Charge-Î²-(4-n-dodecylanilino)naphthalene, the synthesisEnhancingis shown in the Syntheses Examples section as SE-4.Additive-4PP-1Polypropylene resin grade 1, ESCORENE PP 3746G,commercially available from Exxon-Mobil Corporation,Irving, TX.PP-2Polypropylene resin grade 2, TOTAL PP3960,commercially available from Total Petrochemicals USAInc., Houston, TX.

Test MethodsFiltration Testing

The samples were tested for % DOP aerosol penetration (% Pen) and pressure drop (Î”P), and the quality factor (QF) was calculated. The filtration performance (% Pen and QF) of the nonwoven microfiber webs were evaluated using an Automated Filter Tester AFT Model 8127 (available from TSI, Inc., St. Paul, Minn.) using dioctylphthalate (DOP) as the challenge aerosol and a MKS pressure transducer that measured pressure drop (Î”P (mm of H₂O)) across the filter. The DOP aerosol is nominally a monodisperse 0.3 micrometer mass median diameter having an upstream concentration of 100 mg/m³. The aerosol was forced through a sample of filter medium at a calibrated flow rate of 42.5 liters/minute (face velocity of 6.9 cm/s) with the aerosol ionizer turned off. The total testing time was 23 seconds (rise time of 15 seconds, sample time of 4 seconds, and purge time of 4 seconds). The concentration of DOP aerosol was measured by light scattering both upstream and downstream of the filter medium using calibrated photometers. The DOP % Pen is defined as: % Pen=100Ã—(DOP concentration downstream/DOP concentration upstream). For each material, 6 separate measurements were made at different locations on the BMF web and the results were averaged.

The % Pen and Î”P were used to calculate a QF by the following formula:

QF=âˆ’ln(% Pen/100)/Î”P,

where ln stands for the natural logarithm. A higher QF value indicates better filtration performance and decreased QF values effectively correlate with decreased filtration performance.

Elemental Analysis:

Elemental analysis samples were analyzed for weight percent Carbon, Hydrogen and Nitrogen by combustion using a LECO 932 CHNS elemental analyzer (LECO Corp, St. Joseph, Mich.). The samples were run in triplicate. A sulfamethazine standard was also run to check calibration. The results of each individual run are shown along with the calculated averages and standard deviations.

Thermal Stability Analysis:

The thermal stability of charge-enhancing additive samples was measured with a Thermogravimetric Analyzer (TGA) Model 2950 available from TA Instruments, New Castle, Del. Approximately 5-10 milligrams of material was placed in the TGA and heated from room temperature to 500Â° C. at a rate of 10Â° C./min under an air environment while the weight loss was measured. Results are presented as the temperature at which 2% weight loss occurred.

Synthesis ExamplesSynthesis Example SE-1Preparation of Charge-Enhancing Additive-1

[Image Omitted]

In a three-necked round-bottomed flask fitted with magnetic stirring bar was placed phloroglucinol dehydrate (6.63 grams, 97%), 4-dodecylaniline (36.40 grams, 97%) and iodine (0.13 gram, 99%) and toluene (30 milliliters). After the flask was equipped with Dean-Stark trap and condenser, it was then heated at 130Â° C. for 12 hours under constant stirring. After the temperature of the reaction mixture was allowed to cool to about 60Â° C. (the mixture was a viscous liquid), it was slowly poured into 200 milliliters of ethanol to cause precipitation. The precipitate was obtained as a pink solid through filtration. Recrystallization twice from ethanol (150 milliliters for each) afforded Charge-Enhancing Additive-1 (31.0 grams, 87.8% yield) as a light pink powder after being dried at 50Â° C. under vacuum (27 mmHg) overnight. Elemental Analysis and a ¹H NMR spectrum were obtained with the following results: Elemental Analysis: (Calculated: C, 84.15; H, 10.95; N, 4.91; Found: C, 84.28; H, 10.86; N, 4.85); ¹H NMR (400 MHz CDCl₃) Î´ 7.07(d, J=8.32 Hz, 6H), 7.02 (d, J=8.32 Hz, 6H), 6.21 (s, 3H), 5.51 (s, 3H), 2.53 (t, J=7.6 Hz, 6H), 1.65-1.50 (m, 6H), 1.28-1.15 (m, 54H), 0.88 (t, J=7.6 Hz, 9H). Thermal stability was measured using the Thermal Stability Test Method described above. The results are shown in Table 1 below.

Synthesis Example SE-2Preparation of Charge-Enhancing Additive-2

[Image Omitted]

In a three-necked round-bottomed flask fitted with magnetic stirring bar was placed phloroglucinol dehydrate (20.00 grams, 97%), 4-butylaniline (73.63 grams, 97%) and iodine (0.40 gram, 99%). After the flask was equipped with Dean-Stark trap and condenser, it was then heated at 150Â° C. for 20 hours under constant stirring. After the temperature of the reaction mixture was allowed to cool to about 60Â° C. (the mixture was a viscous liquid), it was slowly poured into 200 milliliters of ethanol to cause precipitation. The precipitate was obtained as a pink solid through filtration. Recrystallization from ethanol afforded Charge-Enhancing Additive-2 (42.0 grams, 67.5% yield) as a light pink powder after being dried at 50Â° C. under vacuum (27 mmHg) overnight. Elemental Analysis and a ¹H NMR spectrum were obtained with the following results: Elemental Analysis: (Calculated: C, 83.19; H, 8.73; N, 8.08; Found: C, 83.08; H, 8.79; N, 8.00); ¹H NMR (400 MHz CDCl₃) Î´ 7.08(d, J=8.24 Hz, 6H), 7.02 (d, J=8.24 Hz, 6H), 6.21 (s, 3H), 5.51 (s, 3H), 2.55 (t, J=7.6 Hz, 6H), 1.65-1.53 (m, 6H), 1.40-1.30 (m, 6H), 0.93 (t, J=7.60 Hz, 9H). Thermal stability was measured using the Thermal Stability Test Method described above. The results are shown in Table 1 below.

Synthesis Example SE-3Preparation of Charge-Enhancing Additive-3

[Image Omitted]

In a three-necked round-bottomed flask fitted with magnetic stirring bar was placed resorcinol (5.83 grams, 98%), 4-dodecylaniline (30.00 grams, 97%) and iodine (0.15 gram, 99%). After the flask was equipped with a condenser and air was removed by flushing with N₂, the flask was placed in an oil bath. The oil was heated and the magnetic stirrer was turned on when the mixture became liquid. The mixture was heated at 190Â° C. for 24 hours under constant stirring. The reaction mixture solidified during cooling to room temperature, and ethanol (60 milliliters) was added to the flask. The flask was re-heated to boil the mixture for 5 minutes. The resulted solution was placed in refrigerator overnight to give a dark red solid which was collected by filtration. Removal of discoloration was carried out by dissolving in acetone (100 milliliters) and adding activated carbon (2.0 grams). The thus treated solid was further purified by chromatography by passing it through silica gel (70-150 mesh, commercially available from Alfa Aesar) using methylene chloride as the eluting solvent. The pure product was obtained as light pale powder (6.50 grams, 20.6% yield) after removing the solvent using a rotary evaporator and drying the solid at 50Â° C. under vacuum (27 mmHg) overnight. Elemental Analysis and a ¹H NMR spectrum were obtained with the following results: Elemental Analysis: (Calculated: C, 84.50; H, 10.81; N, 4.69; Found: C, 84.64; H, 10.52, N, 4.69); ¹H NMR (400 MHz CDCl₃) Î´ 7.10-7.05 (m, 5H), 7.02 (d, J=8.36 Hz, 4H), 6.67 (s, 1H), 6.55 (d, J=8.0 Hz, 2H), 5.58 (bs, 2H), 2.54 (t, J=7.84 Hz, 4H), 1.65-1.50 (m, 4H), 1.40-1.20 (m, 36H), 0.93 (t, J=7.84 Hz, 6H). Thermal stability was measured using the Thermal Stability Test Method described above. The results are shown in Table 1 below.

Synthesis Example SE-4Preparation of Charge-Enhancing Additive-4

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In a three-necked round-bottomed flask fitted with magnetic stirring bar was placed Î²-Naphthol (20.60 grams), 4-dodecylaniline (35.00 grams, 97%) and iodine (0.50 gram, 99%). After the flask was equipped with a condenser and air was removed by flushing with N₂, the flask was placed in an oil bath. The oil was heated and the magnetic stirrer was turned on when the mixture became liquid. The mixture was heated at 190Â° C. for 48 hours under constant stirring. The reaction mixture solidified during cooling to room temperature, and ethanol (100 milliliters) was added to the flask. The flask was heated to boil the mixture for 5 minutes. The resulted solution was placed in refrigerator overnight to give a dark grey solid which was collected by filtration. Recrystallization from ethanol (80 milliliters) yielded Charge-Enhancing Additive-4 as a grey-greenish powder (19.6 grams, 39% yield) after being dried at 50Â° C. under vacuum (27 mmHg) overnight. Elemental Analysis and a ¹H NMR spectrum were obtained with the following results: Elemental Analysis: (Calculated: C, 86.76; H, 9.62; N, 3.61; Found: C, 86.32; H, 9.45; N, 3.59); ¹H NMR (400 MHz CDCl₃) Î´ 7.72(d, J=8.88 Hz, 2H), 7.62 (d, J=8.24 Hz, 1H), 7.40-7.35 (m, 2H), 7.30-7.24 (m, 1H), 7.20-7.08 (m, 5H), 5.77 (s, 1H), 2.58 (t, J=7.04 Hz, 2H), 1.70-1.50 (m, 2H), 1.35-1.20 (m, 18H), 0.93 (t, J=7.04 Hz, 3H). Thermal stability was measured using the Thermal Stability Test Method described above. The results are shown in Table 1 below.

TABLE 1Charge-EnhancingTemperature at 2% weight lossAdditive(Â° C.)1371232432224268

Examples 1-11 and Comparative Examples C1-C6

For each of the Examples and Comparative Examples, the procedures described below were followed. The data for these Examples are presented in Tables 2 and Table 3.

Step Aâ€”Preparation of Microfiber Webs:

For each Example, one of the charge-enhancing additives described above (either Charge-Enhancing Additive 1, 2, 3 or 4) was selected and dry blended with one of the 2 grades of polypropylene at the concentration shown in Table 2, and the blend was extruded as described in Van A. Wente, â€œSuperfine Thermoplastic Fibers,â€ Industrial Engineering Chemistry, vol. 48, pp. 1342-1346 and Naval Research Laboratory Report 111437 (Apr. 15, 1954). The extrusion temperature ranged from about 250Â° C.-300Â° C. and the extruder was a BRABENDER conical twin-screw extruder (commercially available from Brabender Instruments, Inc.) operating at a rate of about 2.5 to 3 kg/hr (5-7 lb/hr). The die was 25.4 cm (10 in) wide with 10 holes per centimeter (25 holes per inch). Melt-blown microfiber (BMF) webs were formed having basis weights of 49-97 g/m², effective fiber diameters of 7.3-14.1 micrometers and a thicknesses of about 0.71-1.55 millimeters.

Similarly, for each Comparative Example, a BMF web was prepared from the same grade of polypropylene as the corresponding Example web, but no charge-enhancing additive was added. Table 2 summarizes the specific web characteristics for each of the examples.

Step Bâ€”Electret Preparation:

Each of the BMF webs prepared in Step A above was charged by one of two electret charging methods: hydrocharging, or a combination of corona pre-treatment and hydrocharging. Table 2 summarizes the specific charging method applied to each of the samples.

Charging Method 1â€”Hydrocharging:

A fine spray of high purity water having a conductivity of less than 5 microS/cm was continuously generated from a nozzle operating at a pressure of 896 kiloPascals (130 psig) and a flow rate of approximately 1.4 liters/minute. The selected BMF webs prepared in Step A were conveyed by a porous belt through the water spray at a speed of approximately 10 centimeters/second while a vacuum simultaneously drew the water through the web from below. Each BMF web was run through the hydrocharger twice (sequentially once on each side) and then allowed to dry completely overnight prior to filter testing.

Charging Method 2â€”Corona Pre-Treatment and Hydrocharging:

The selected BMF webs prepared in Step A above were pretreated by DC corona discharge. The corona pre-treatment was accomplished by passing the web on a grounded surface under a corona brush source with a corona current of about 0.01 milliamp per centimeter of discharge source length at a rate of about 3 centimeters per second. The corona source was about 3.5 centimeters above the grounded surface on which the web was carried. The corona source was driven by a positive DC voltage. The BMF web was then charged by hydrocharging as described in Charging Method 1.

Filtration Performance:

Each of the charged samples prepared in Step B above was cut into a 1 meter section. Each section was tested for its % DOP aerosol penetration (% Pen) and pressure drop (Î”P), and the quality factor (QF) was calculated as described in the Test Methods given above. These results are reported in Table 3 below as % Pen, Î”P and QF.

TABLE 2Charge-EnhancingAdditiveEff. FiberBasisAdditiveChargingResinConcn.Diam.SolidityWeightThicknessExampleExampleMethodGrade(wt %)(Î¼m)(%)(g/m²)(mm)121PP1114.16.9971.55221PP1113.97.7500.71311PP1112.07.4490.74411PP1110.36.0520.97C1â€‚none1PP107.65.3551.16511PP20.757.45.0591.30C2â€‚none1PP207.65.7591.13612PP20.757.45.0591.30C3â€‚none2PP207.65.3591.30711PP10.759.45.7561.08C4â€‚none1PP107.85.9530.99811PP20.7510.26.9600.97C5â€‚none1PP207.76.0601.11941PP118.96.0520.9710â€‚41PP10.57.76.0520.9711â€‚31PP10.57.56.2500.89C6â€‚none1PP107.35.9571.08

TABLE 3ChargingÎ”PExampleMethod% Pen(mm of H₂O)QF119.391.21.992131.680.562.073113.100.782.61416.171.062.64C1136.902.20.45510.752.332.12C2152.822.070.31621.522.321.83C3221.052.370.67718.941.251.94C4121.851.830.83813.671.502.22C5117.101.880.949136.231.330.7610â€‚133.881.650.6611â€‚111.142.031.08C6143.481.820.46