Meltblown wetlaid method for producing non-woven fabrics from natural cellulose

Abstract

The present invention provides a meltblown wetlaid method for producing non-woven fabrics from natural cellulose using pulp as raw material and N-methylmorpholine N-oxide (NMMO) as solvent for dissolving into dope. The dope is then extruded out of a spinneret to form filament bundle by meltblown method. Subsequently, by means of ejecting mist aerosol of water, the filament bundle is coagulated with regeneration. Via post treatments of water rinsing, hydro-entangled needle punching, drying, winding-up and the like have been orderly applied, then final product of nonwoven fabrics with continuous filament are produced from natural cellulose.

Description

FIELD OF THE PRESENT INVENTION

The present invention relates to a “meltblown wetlaid method for producing non-woven fabrics from natural cellulose”, particularly for one with environment protective process that not only has advantages in low manufacturing cost without environmental pollution but also features good degree of air permeability and degree of water absorption so that it meet medical and industrial application requirements such as apparels, sanitary and medical materials, filtrating materials, wiping materials for biomedical and optoelectronic wafers and the like.

BACKGROUND OF THE INVENTION

Currently, most nonwoven fabrics of chemical synthetic fiber are produced from melted macromolecule polymers and made by spunlaid process through extrusion and stretch to form continuous filaments as well as stacking laying for web formation so that the nonwoven fabrics of such filaments feature in good physical properties of air permeability and water absorption. Thus, such nonwoven fabrics of chemical synthetic fiber are prevalently used in application fields of medical, sanitary, wiper, filters and so on. According to the survey and statistics of Association of the Nonwoven Fabrics Industry USA (INDA), the marketing share for the nonwoven fabrics of chemical synthetic produced spunlaid process already from 33.5% in 1994 (second) leaps up to 43.7% in 2009 (first) with total annual yield of 2.7 million tons. Wherein, main raw materials are from polypropylene (PP), polyester (PET), polyethylene (PE) and Nylon in quantity order with overall consumed quantity 96%. However, the wasted nonwoven fabric of chemical synthetic fiber after having been used incurs a malignant impact to the environment because they are indissoluble by natural environment. Moreover, for all aforesaid chemical raw materials from petrochemical material, acquiring cost will gradually increased in follow with gradual decrease in mining quantity of petrochemical material, which is not inexhaustible. Nowadays, the manufacturers of the nonwoven fabric gradually divert to use natural materials in substitute for raw materials of chemical synthetic fiber. Nevertheless, only wet-laid method and hydro-entangled needle punching method of long process can be adopted by using such natural materials to produce nonwoven fabric with final product of staple fiber instead of filament in high manufacturing cost so that the degrees of air permeability and water absorption of such nonwoven fabric are decreased. Therefore, how to using suitable natural fiber material with low manufacturing cost to produce nonwoven fabrics with filament instead of staple fiber becomes an urgent and critical issue.

SUMMARY OF THE INVENTION

The primary object of the present invention is to provide a “meltblown wetlaid method for producing non-woven fabrics from natural cellulose” with pulp as raw material and N-methylmorpholine N-oxide (NMMO) as solvent for dissolving into dope. Then, the dope is extruded out of a spinneret to form filament bundle by meltblown method; and by means of ejecting mist aerosol of water, the filament bundle is coagulated with regeneration. After post treatments of water rinsing, hydro-entangled needle punching, drying, winding-up and the like have been orderly applied, then final product of nonwoven fabrics with continuous filament are produced from natural cellulose. Accordingly, the present invention becomes an environment protective process with advantages in low manufacturing cost due to short process and solvent adequately recycle without environmental pollution due to nontoxic N-methylmorpholine N-oxide (NMMO).

The other object of the present invention is to provide a “meltblown wetlaid method for producing non-woven fabrics from natural cellulose” to produce nonwoven fabrics with continuous filament from natural cellulose features better degree of air permeability for nonwoven and degree of water absorption for nonwoven than conventional nonwoven produced either from chemical synthetic fiber or conventional natural fiber so that its waste is biodegradable without any harmful effect in environment.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a flow chart of block diagram showing the fabricating process of the present invention.

FIG. 2 is a chemical structure of the (N-methylmorpholine N-oxide, called NMMO for short) used in the present invention.

FIG. 3 is an operational schematic view showing a forming process for cellulose melt-blown filaments of the present invention.

FIG. 4 is a fabrication processing view showing an overall meltblown wetlaid method of the present invention.

FIG. 5 is an enlarged schematic view with 1000 times of magnification showing a non-woven fabric produced from natural cellulose of the present invention.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

For further disclose the fabricating process and efficacy, detailed description for some preferred exemplary embodiments with associated drawings is presented below. Please refer to FIGS. 1 through 5, show processing steps of fabricating method for embodiments of a “meltblown wetlaid method for producing non-woven fabrics from natural cellulose”, as follows:

a. Material Selection and Preparation: Select wood pulp as raw material, preferably pulp cellulose of staple or filament with content cellulose being over 65% and degree of polymerization (DP) being between 500˜1200;

b. Dope Blending and Dissolution: By putting N-methylmorpholine N-oxide (NMMO) (whose chemical structure as shown in FIG. 2) as dissolving solvent and 1,3-phenylene-bis 2-oxazoline (BOX) as stabilizer into prepared pulp for high speed blending and dissolving under low temperature between 60 degree of Celsius and 80 degree of Celsius (60° C.˜80° C.) by horizontal dope blending machine by means of cellulose features of high expanding, moistening and dissolving ability as well as high rate of dissolving speed to expedite mutually blending and dissolving effect; Then, dehydrate it via heating up to temperature between 80 degree of Celsius and 120 degree of Celsius (80° C.˜120° C.) by vacuum thin film evaporator for 5 minutes to decrease water content thereof down to 5˜13% so that a homogenized mucilaginous dope D can be formed;

c. Meltblown and Filament Formation: by meltblown method, the dope D is extruded out of a spinneret 3 to form filament bundle as shown in FIG. 2, the dope D is fed into a die assembly 2 and forcedly extruded out the spinneret 3 via a gear pump 1 to form filament bundle, wherein certain hot air H is continuously filled in for circulation therein then discharged out via surrounding of the spinneret 3; and

d. Post Treatments and Fabric Formation: By means of ejecting mist aerosol of water, the filament bundle is coagulated with regeneration; After post treatments of water rinsing, hydro-entangled needle punching, drying, winding-up and the like have been orderly applied (as shown in FIG. 4), then final product of nonwoven fabrics with continuous filament are produced from natural cellulose (as shown in FIG. 5).

Wherein, stabilizer solvent, 3-phenylene-bis 2-oxazoline (BOX) in above step b functions to subdue the declining recession for the color and degree of polymerization (DP) of cellulose. Whereas, the dissolving solvent N-methylmorpholine N-oxide (NMMO) in above steps b through d is nontoxic with concentration of 45%˜75% so that it can be recycled with low consumption rate via filtration, decolor, and condensation under low pressure distillation after having been drained out in water rinse process with rate of recovery up to over 99.5%. Thereby, it completely complies with the criteria of the environmental protection because it not only can reduce the manufacturing cost but also will not incur any harmful pollution to the environment.

Moreover, for the dope D in above step b, the content percentage of cellulose thereof is 6 wt %˜15 wt %, the viscosity thereof is 300˜3000 poise, the light transmittance index thereof is 1.470˜1.495, and the melting Index thereof is 200˜1000.

Furthermore, the wood pulp in above step a can be replaced by paper pulp of staple or filament with content cellulose being over 65%.

For further proving the features and efficacy of the present invention, some exemplary experimental cases having been performed with measured data are described as following.

Firstly, prepare wood pulp cellulose samples 1 through 10 in range for degree of polymerization (DP) being 650˜1050 with respective composition of dope as shown in TABLE 1;

Secondly, by putting N-methylmorpholine N-oxide (NMMO) and 1,3-phenylene-bis 2-oxazoline (BOX) into prepared pulp for high speed blending and dissolving under low temperature between 60 degree of Celsius and 80 degree of Celsius (60° C.˜80° C.). Then, dehydrate extra water content therein via heating up to temperature between 80 degree of Celsius and 120 degree of Celsius (80° C.˜120° C.) by vacuum thin film evaporator for 5 minutes to decrease water content thereof down to 5˜13% so that respective homogenized mucilaginous dope D for each sample is formed;

Thirdly, by meltblown method, each sample dope D is extruded out of a spinneret 3 to form filament bundle respectively; and

Finally, by means of ejecting mist aerosol of water, the filament bundle is coagulated with regeneration. After post treatments of water rinsing, hydro-entangled needle punching, drying, winding-up and the like have been orderly applied, then final product of nonwoven fabric for samples 1 through 10 are produced as shown in TABLE 1.

TABLE 1
Composition of Dope for Samples 1 through 10
		MP	RR	CP	CP	CP	VC	LTI	MI
		of	for	of	of	of	of	of	of
	DP	ARA	DP	CL	SV	WT	DP	DP	DP
	U
S	nil	wt %	%	%	%	%	poise	nil	nil
1	650	0.05%	26.2	7.6	81.3	11.1	840	1.489	870
2	650	0.10%	20.5	8.5	81.9	9.6	980	1.482	820
3	650	0.15%	14.7	9.1	81.2	9.7	1240	1.486	810
4	650	0.20%	11.6	8.5	82.0	9.5	1060	1.481	820
5	650	0.25%	11.3	8.2	81.8	10.0	960	1.485	830
6	1050	0.05%	26.5	7.8	81.8	10.4	1240	1.481	750
7	1050	0.10%	21.7	7.5	81.1	11.4	1560	1.480	720
8	1050	0.15%	15.9	9.1	82.1	8.8	1420	1.482	700
9	1050	0.20%	13.8	8.2	82.0	9.8	1280	1.476	740
10	1050	0.25%	12.1	7.9	81.0	11.1	1320	1.479	710
Remark
S = sample
U = unit
DP = degree of polymerization
MP of ARA = mixing percentage of anti-recession additive
RR for DP = rate of recession for degree of polymerization
CP of CL = content percentage of cellulose
CP of SV = content percentage of solvent
CP of WT = content percentage of water
VC of DP = viscosity of dope
LTI of DP = light transmittance index of dope
CP of DP = melting Index of dope

Subsequently, perform nonwoven strength test for samples 11 through 20, which are prepared into different basis weights of nonwoven in accordance with respective degree of polymerization (DP) and mixing percentage of anti-recession additive shown in TABLE 1, by criteria of CNS5610 with following procedure.

1. Specimen Preparation:

Respectively obtain 10 pieces of specimens for each cross direction (CD) and mechanical direction or machine direction (MD) with specimen length being over 180 mm and specimen width being 2.54 mm.

2. Strength Test:

By using universal strength testing machine with specimen holding jaws of testing fixture being set 76 mm under crosshead speed for extension test being set 300 mm/min, respectively perform test for each of 10 specimens.

3. Testing Results:

Respective nonwoven strength for samples 11 through 20 is listed in following TABLE 2.

TABLE 2
Physical Properties for Samples 11 through 20
		MP	BW	SMD	SCD	FN
		of	of	of	of	of
	DP	ARA	NW	NW	NW	FB
	U
S	nil	wt %	g/m2	kgf	kgf	μm
11	650	0.05%	75	15.1	8.3	4.2
12	650	0.10%	76	16.0	8.9	3.8
13	650	0.15%	75	16.1	8.2	4.5
14	650	0.20%	74	16.0	8.0	3.5
15	650	0.25%	75	15.5	8.8	4.7
16	1050	0.05%	75	15.8	8.8	5.5
17	1050	0.10%	74	15.2	9.1	5.8
18	1050	0.15%	76	16.7	9.4	6.2
19	1050	0.20%	75	16.2	9.5	5.9
20	1050	0.25%	75	16.1	9.5	7.2
Remark
S = sample
U = unit
DP = degree of polymerization
MP of ARA = mixing percentage of anti-recession additive
BW of NW = basis weight of nonwoven
SMD of NW = strength in machine direction of nonwoven
SCD of NW = strength in cross direction of nonwoven
FN of FB = fineness (or fiber number) of fiber

Finally, perform air permeability test and water absorption test for samples 21 through 32, which are prepared in accordance with respective degree of polymerization (DP) and basis weights of nonwoven, by criteria of CNS5612 with following procedure.

1. Air Permeability Test:

Respectively obtain 4 pieces of specimens with specimen dimension being 26×26 cm² for each sample. By using Textest FX 3300 Air Permeability Tester, respectively perform test for each of 12 specimens 21 through 32.

2. Water Absorption Test:

Respectively obtain 5 longitudinal pieces of specimens with specimen width being 76 mm, specimen weight being 5.0±0.1 g and specimen length being determined in accordance with the specimen weight. For testing procedure of water absorption test: firstly, put each specimen in a holding basket, and then dunk the holding basket with specimens in water in totally immersion manner for 10 seconds; secondly, lift the holding basket with specimens out of the water to drip water for 10 seconds; and finally, put the holding basket with specimens into a measuring glass of known weight to measure overall gross weight with 0.1 g precision.

The rate of water absorption for specimen is calculated by following formula:Rate of Water Absorption (%): RA_W(%)={[W_A(g)−W_D(g)]/W_D(g)}×100

Where,

• • RA_W denotes to rate of water absorption for each specimen;
  • W_D denotes to specimen dry weight before dunking in water; and
  • W_A denotes to specimen wet weight after dunking in water.

3. Testing Results:

Respective nonwoven strength for samples 21 through 32 is listed in following TABLE 3.

TABLE 3
Physical Properties for Samples 21 through 32
	DP	BW of NW	FN of FB	DAP for NW	DAP for DWA
	U
S	nil	g/m2	μm	cm3/cm2/min	%
21	650	25	4.1	2650	450
22	650	75	3.6	605	520
23	650	125	4.6	219	610
24	650	175	3.4	195	750
25	650	225	4.6	182	920
26	650	300	4.2	145	1420
27	1050	25	5.2	2870	420
28	1050	75	5.6	627	550
29	1050	125	6.0	230	650
30	1050	175	5.9	211	730
31	1050	225	6.2	195	880
32	1050	300	5.8	158	1350
Remark
S = sample
U = unit
DP = degree of polymerization
BW of NW = basis weight of nonwoven
FN of FB = fineness (or fiber number) of fiber
DAP for FB = degree of air permeability for nonwoven
DWA for FB = degree of water absorption for nonwoven

As demonstrated by the samples 11 through 20 in TABLE 2 and samples 21 through 32 in TABLE 3, the nonwoven fabric of continuous filament produced from natural cellulose by the present invention features very ideal strength either in mechanical direction (MD) or cross direction (CD) as well as better degree of air permeability for nonwoven and degree of water absorption for nonwoven than conventional nonwoven produced either from chemical synthetic fiber or conventional natural fiber so that it meet medical and industrial application requirements such as apparels, sanitary and medical materials, filtrating materials, wiping materials for biomedical and optoelectronic wafers and the like.

In conclusion of disclosure heretofore, the present invention has advantages in low manufacturing cost due to short process and solvent adequately recycle without environmental pollution due to nontoxic N-methylmorpholine N-oxide (NMMO). Accordingly, the present invention becomes an environment protective process with novelty and practical usage.

Claims

1. A meltblown wetlaid method for producing non-woven fabrics with continuous filament from natural cellulose, comprising the steps of: (a) selecting wood pulp as raw material;(b) mixing the wood pulp of step (a) with N-methylmorpholine N-oxide (NMMO) as a dissolving solvent and 1,3-phenylene-bis 2-oxazoline (BOX) as a stabilizer, blending the mixture, and dissolving the mixture at a temperature of 60 to 80° C.;(c) heating the mixture of step (b) to a temperature of 80 to 120° C. for 5 to 10 minutes to decrease the water content thereof down to 5 to 13% to form a homogenized mucilaginous dope;(d) extruding the homogenized mucilaginous dope of step (c) out of a spinneret by the meltblown method to form a filament bundle;(e) Coagulating the filament bundle with regeneration by ejecting mist aerosol of water; and(f) rinsing the coaglulated filament bundle of step (e) with water; and(g) hydro-entangled needle punching, drying, and winding-up the rinsed coaglulated filament bundle of step (f) to produce the nonwoven fabrics with continuous filament.

2. The method of claim 1, wherein the wood pulp as raw material is wood pulp or paper pulp cellulose of staple or filament and has a cellulose content of over 65% and a degree of polymerization (DP) of from 500 to 1200.

3. The method of claim 1, wherein the concentration of the dissolving solvent N-methylmorpholine N-oxide (NMMO) in the mixture of step (b) is from 45 to 75%.

4. The method of claim 1, wherein the dope of step (c) has a cellulose content of from 6 to 15wt%.

5. The method of claim 1, wherein the dope of step (c) has a viscosity of from 300 to 3000 poise.

6. The method of claim 1, wherein the dope of step (c) has a light transmittance index of from 1.470 to 1.495.

7. The method of claim 1, wherein the dope of step (c) has a melting index of from 200 to 1000.

8. The method of claim 1, wherein the nonwoven fabric of step (g) has a speed of winding-up of from 2 to 200 meters per minute.

9. The method of claim 1, wherein the nonwoven fabric of step (g) has a basis weight of from 10 to 300 g/m2.

10. The method of claim 1, wherein the nonwoven fabric of step (g) has a tensile strength in mechanical direction (MD) of over 15 kgf and a tensile strength in cross direction (CD) of over 8 kgf.

11. The method of claim 1, wherein the nonwoven fabric of step (g) has a fiber fineness of from 1 to 15 μm.

12. The method of claim 1, wherein the nonwoven fabric of step (g) has a degree of air permeability of from 100 to 3500 cm3/cm2/min.

13. The method of claim 1, wherein the nonwoven fabric of step (g) has a degree of water absorption of from 300 to 2000%.