JP2018075522A - Method for producing fiber-reinforced polyvinylidene fluoride porous hollow fiber membrane - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a method for producing a porous hollow fiber membrane which, without causing a trouble, such as cracking, in the porous hollow fiber membrane obtained even when a spinning speed is increased, improves load resistance and fatigue resistance, and provides high permeation characteristics, and which can inhibit the breaking of the porous hollow fiber membrane caused by a high flow rate of fluid, such as gas or liquid, or the breaking thereof caused by fatigue.SOLUTION: A method for producing a fiber-reinforced polyvinylidene fluoride porous hollow fiber membrane comprises: allowing a cylindrical braid to pass through the inside of the inner nozzle of a double annular spinning nozzle; applying a membrane-forming stock solution discharged from the outer nozzle of the double annular spinning nozzle to the outer surface of the cylindrical braid which has passed through the inner nozzle of the double annular spinning nozzle to impregnate it therein, and then coagulating it in a coagulation liquid; and carrying out winding onto a winder, thereby producing the fiber-reinforced polyvinylidene fluoride porous hollow fiber membrane. In the method, as the cylindrical braid, there is used a cylindrical braid having a braid density of 70/inch or more, or having a yarn fineness of 280 decitex or more and 36 or more filaments.SELECTED DRAWING: Figure 2

Description

  The present invention relates to a method for producing a fiber-reinforced polyvinylidene fluoride porous hollow fiber membrane. More specifically, the present invention relates to a method for producing a fiber-reinforced polyvinylidene fluoride porous hollow fiber membrane that is effectively used as a treatment membrane for water purification treatment or sewage wastewater treatment, a humidifying membrane for fuel cells or a dehumidifying membrane.

  In recent years, interest in the environment has increased, and water quality regulations have become stricter in the field of water treatment such as drainage and water purification. From the standpoint of high separability and energy saving, separation membranes, especially hollow porous membranes, have been researched and put to practical use. There is a great deal of progress.

Membrane filtration is widely used in the water treatment field because water treatment by sewage treatment and sewage wastewater treatment are easier to maintain and manage, and the quality of the treated water is better than conventional flocculation and precipitation filtration methods. It is used. Here, from the viewpoint of securing water resources in recent years, porous hollow fiber membrane modules having a high strength and a large membrane area per unit volume are often used. For example, in the case of wastewater treatment, a porous hollow fiber membrane module having a membrane area of about 50 to 100 m ² per unit volume is generally used, and the membrane module has an amount of tens to hundreds of liters per minute. Water will be supplied. In that case, the porous hollow fiber membrane may be broken due to the influence of the generated load. Further, when the porous hollow fiber membrane module is used for industrial applications, it is usually used for a long period of several years to 10 years, so that it is also necessary to avoid breakage of the porous hollow fiber membrane due to fatigue.

  As a hollow fiber membrane material excellent in chemical stability, polyvinylidene fluoride (PVDF) is used. The applicant previously used PVDF as the hollow fiber membrane material, triethyl phosphate as the solvent and the solvent to be added to the coagulation bath (and core liquid), and further slowed the substitution rate of the solvent to reduce the skin layer and void. A method for producing a homogeneous PVDF porous membrane without a layer has been proposed (Patent Document 1). However, in such a production method, there have been cases where it is not easy to form a hollow fiber due to a slow solidification rate.

For physical stability, Applicants have also passed the cylindrical braid through the inner nozzle of the double annular spinning nozzle and doubled it on the outer surface of the cylindrical braid that passed through the inner nozzle of the double annular spinning nozzle. In the method for producing a fiber-reinforced porous hollow fiber membrane produced by applying and impregnating a membrane-forming stock solution discharged from an outer nozzle of an annular spinning nozzle, solidifying in a coagulating solution, and drying.
A solution obtained by dissolving polyvinylidene fluoride in triethyl phosphate so as to have a concentration of 16 to 27% by weight as a film forming stock solution is used, and a hollow fiber-like product obtained after spinning is obtained from an aqueous solution of triethyl phosphate having a concentration of 10 to 90% by weight. A method for producing a porous hollow fiber membrane that is coagulated in a coagulating liquid for 40 to 120 seconds is proposed (Patent Document 2).

  The porous hollow fiber membrane module obtained by such a manufacturing method has high permeability characteristics by reducing the coagulation rate and forming a homogeneous membrane by the composition of the membrane stock solution and coagulation solution, and has load resistance and fatigue resistance. On the other hand, there is an excellent effect that the breakage of the porous hollow fiber membrane caused by a fluid such as a high flow rate gas or liquid or the breakage due to fatigue can be suppressed.

  However, if the spinning speed is increased in the manufacturing process of the hollow fiber membrane at a low cost to improve productivity, the starting point of the crack along the axial direction of the porous membrane coated on the cylindrical braid is formed, and the drying shrinkage of the membrane As a result, a phenomenon of breaking in the axial direction occurs.

The following two points can be considered as factors causing the origin of cracks that occur in the axial direction.
(1) Weld line formed at the joint of resin, which is a problem in hollow fiber formation
(2) By slowing down the coagulation rate, the film-forming stock solution penetrates into the braid and the peel strength is improved.On the other hand, the film-forming stock solution permeates too much, resulting in an unstable outer diameter and non-uniform film thickness. And, as a result, the stress due to shrinkage during drying of the film is concentrated in part.

Japanese Patent No. 3,261,761 JP 2012-179603 A JP 2006-010792 A

  The object of the present invention is to improve load resistance and fatigue resistance without causing defects such as cracks in the porous hollow fiber membrane obtained even when the spinning speed is increased, and has high permeability characteristics. Another object of the present invention is to provide a method for producing a porous hollow fiber membrane that can suppress breakage of the porous hollow fiber membrane due to a high flow rate gas or liquid or breakage due to fatigue.

The object of the present invention is to pass the cylindrical braid through the inner nozzle of the double annular spinning nozzle, and on the outer surface of the cylindrical braid that has passed through the inner nozzle of the double annular spinning nozzle, the outer nozzle of the double annular spinning nozzle. A method for producing a fiber-reinforced polyvinylidene fluoride porous hollow fiber membrane produced by applying and impregnating a membrane-forming stock solution discharged from a coagulating solution, coagulating in a coagulating solution, and winding it on a winder In
This is achieved by using a cylindrical braid having a knitting density of 70 / inch or more, a yarn fineness of 280 dtex or more, and 36 filaments or more.

  The method for producing a fiber-reinforced polyvinylidene fluoride porous hollow fiber membrane according to the present invention enables control of the amount of the membrane-forming stock solution penetrating into the cylindrical braid. The diameter shape is stabilized and the film thickness can be made uniform. As a result, the starting point of the crack in the hollow fiber membrane axial direction is not formed, and an excellent effect is obtained that the membrane crack can be eliminated.

It is a side view of the polyester sleeve used in Example 1. 2 is a SEM photograph showing a cross section of the fiber-reinforced porous hollow fiber membrane obtained in Example 1. FIG. It is a SEM photograph which shows the film | membrane surface of the major axis direction of the fiber reinforced porous hollow fiber membrane obtained in Example 1. It is a side view of the polyester sleeve used in Example 2. It is a SEM photograph which shows the cross section of the fiber reinforced porous hollow fiber membrane obtained in Example 2. It is a SEM photograph which shows the membrane surface of the major axis direction of the fiber reinforced porous hollow fiber membrane obtained in Example 2 It is a side view of the polyester sleeve used by the comparative example. FIG. 3 is an SEM photograph showing a cross section of a fiber-reinforced porous hollow fiber membrane obtained in a comparative example. It is a SEM photograph showing the membrane surface in the major axis direction of the fiber reinforced porous hollow fiber membrane obtained in the comparative example

The manufacturing method of the fiber reinforced porous hollow fiber membrane according to the present invention is such that the cylindrical braid is passed through the inner nozzle of the double annular spinning nozzle and the outer surface of the cylindrical braid that has passed through the inner nozzle of the double annular spinning nozzle. A fiber reinforced polyvinylidene fluoride produced by coating and impregnating a film-forming stock solution discharged from the outer nozzle of a double annular spinning nozzle onto a bobbin after coagulating in a coagulating liquid. In the method for producing a porous hollow fiber membrane,
By using a cylindrical braid having a knitting density of 70 / inch or more, or a yarn fineness of 280 dtex or more and 36 filaments or more, the resulting fiber-reinforced porous hollow fiber membrane has a stable outer diameter and a film thickness. Can be made uniform, and as a result, the starting point of the crack in the axial direction of the hollow fiber membrane is not formed, and the membrane crack can be eliminated.

  The cylindrical braid has a knitting density of 70 / inch or more, preferably 70 to 100 / inch, or a yarn fineness of 280 dtex or more and 36 filaments or more, preferably 360 to 500 dtex and 48 to 76 filaments. It can be used without particular limitation regardless of the method of knitting such as circular knitting and oblique knitting. For example, cylindrical nets such as monofilaments, multifilaments, and spun yarns are used, and specific examples include organic fiber base materials such as polyphenylene sulfide, polyester, polypropylene, polyethylene, rayon, vinylon, polyamide, polyimide, and aramid. Polyphenylene sulfide and polyester are used. If the knitting density and yarn fineness are other than these ranges, the outer diameter shape of the hollow fiber membrane is not stable and the film thickness is not uniform, so the starting point of the crack in the axial direction of the hollow fiber membrane is formed, There is a risk of film cracking.

  The membrane-forming stock solution for forming the porous hollow fiber membrane is attached to the outer peripheral surface of the cylindrical braid. The film forming stock solution adheres to the outer circumferential surface of the cylindrical braid by applying the film forming stock solution discharged from the outer nozzle of the double annular spinning nozzle to the outer surface of the cylindrical braid passing through the inner nozzle of the double annular spinning nozzle. Is used. Here, when passing the cylindrical braid through the inner nozzle of the double annular spinning nozzle, generally a tension of about 4 to 50 N is applied to the cylindrical braid.

  As the film-forming stock solution, a solution in which polyvinylidene fluoride is dissolved in a soluble solvent of polyvinylidene fluoride resin so as to have a concentration of about 16 to 27% by weight, preferably about 18 to 25% by weight is used. If the polyvinylidene fluoride concentration is lower than this, the pore size of the membrane becomes too large. On the other hand, if the concentration is higher than this, it becomes difficult to dissolve the polyvinylidene fluoride. As the soluble solvent for the polyvinylidene fluoride resin, various alcohols, aprotic polar solvents such as dimethylformamide, diethylformamide, dimethylacetamide, diethylacetamide, dimethylsulfoxide, N-methyl-2-pyrrolidone, triethyl phosphate and the like are used.

  The cylindrical braid to which the membrane forming raw solution for forming the porous hollow fiber membrane is attached is coagulated with a coagulating liquid by a dry-wet spinning method or a wet spinning method, and after washing and drying, a fiber-reinforced porous hollow fiber A film is formed.

  Patent Document 3 discloses that a cylindrical braid having a yarn fineness of 200 to 600 dtex and a batting number of 16 to 48 is used, but a polyester sleeve used in the example (Example 1). Has a yarn fineness of 280 dtex (dtex) and a number of strokes of 24, and the polyphenylene sulfide sleeve (Example 2) has a yarn fineness of 280 dtex (dtex) and a number of strokes of 24. No effect is shown when the cylindrical braid defined in the present invention is selectively used.

  The coagulation is performed by immersing in the coagulation liquid, for example, for about 20 to 120 seconds, preferably about 20 to 90 seconds. When the coagulation time is shorter than this, the film does not coagulate and becomes irregularly shaped, and even when the coagulation time is longer than this, the manufacturing time is prolonged and no further effect is obtained.

  As the coagulation liquid, an aqueous triethyl phosphate solution of about 10 to 90% by weight, preferably about 60 to 90% by weight, more preferably about 70 to 80% by weight is used. When an aqueous triethyl phosphate solution having a concentration below this is used as the coagulation liquid, a porous film cannot be obtained.

  Next, the present invention will be described with reference to examples.

Example 1
A film forming stock solution was prepared by dissolving 100 g of polyvinylidene fluoride resin (Kureha product KF-1550) in 400 g of dimethyl sulfoxide. Next, a tetron sleeve (knitting density: 70 to 75 / inch, 280 dtex, 24 filaments), which is a polyester braided polyester string, is passed through the inner nozzle of a double annular spinning nozzle having an inner tube diameter of 2.0 mm. The substrate passed through the inner nozzle of the double annular spinning nozzle is impregnated by applying the film forming stock solution pumped and discharged from the outer nozzle of the double annular spinning nozzle to the outer surface using a gear pump. Spinning was performed at 5 m / min, and the mixture was extruded into a coagulating liquid composed of 80% by weight triethyl phosphate aqueous solution and coagulated for 24 seconds.

  The produced hollow fiber membrane penetrates only up to 50% or more of the inside of the Tetron sleeve, and the outer diameter shape thereof is a circular shape that is not particularly distorted or recessed as shown in FIG. there were. Moreover, when the film | membrane surface after washing | cleaning and drying was observed by SEM, the crack of an axial direction was not confirmed as FIG. 3 shows.

Example 2
In Example 1, a Tetoron sleeve (knitting density 35-40 / inch, 360 dtex, number of filaments 48) was used as the cylindrical braid. In the hollow fiber membrane obtained, polyvinylidene fluoride penetrates only up to 50% or more of the inside of the Tetron sleeve, and the outer diameter shape thereof is a circular shape that is not particularly distorted or recessed as shown in FIG. there were. Further, when the film surface after washing and drying was observed with an SEM, no axial crack was observed as shown in FIG.

Comparative Example In Example 1, a tetron sleeve (knitting density 45-50 / inch, 280 dtex, 24 filaments) was used as the cylindrical braid. In the obtained hollow fiber membrane, polyvinylidene fluoride penetrated to 100% of the inside of the Tetron sleeve, and as shown in FIG. 8, the outer diameter shape was not circular, and a dent was confirmed in the cross section. . Moreover, when the film | membrane surface after washing | cleaning and drying was observed with SEM, as shown in FIG. 9, the crack of an axial direction was confirmed.

  The fiber reinforced polyvinylidene fluoride porous hollow fiber membrane produced by the production method according to the present invention has high permeation characteristics and mechanical strength, so that it can be used in water treatment fields such as drainage and purified water, a humidifying membrane for fuel cells, Effectively used as a dehumidifying film.

Claims (4)

A film forming stock solution in which the cylindrical braid is passed through the inner nozzle of the double annular spinning nozzle and discharged from the outer nozzle of the double annular spinning nozzle to the outer surface of the cylindrical braid passing through the inner nozzle of the double annular spinning nozzle. In the method for producing a fiber-reinforced polyvinylidene fluoride porous hollow fiber membrane, which is coated and impregnated, then solidified in a coagulating liquid, and wound into a winder.
A method for producing a fiber-reinforced polyvinylidene fluoride porous hollow fiber membrane, wherein a cylindrical braid having a knitting density of 70 / inch or more, or a yarn fineness of 280 dtex or more and 36 filaments or more is used.   The method for producing a fiber-reinforced polyvinylidene fluoride porous hollow fiber membrane according to claim 1, wherein a polyester sleeve is used as the cylindrical braid.   The method for producing a fiber-reinforced polyvinylidene fluoride porous hollow fiber membrane according to claim 1 or 2, wherein triethyl phosphate is used as the coagulating liquid.   A fiber-reinforced polyvinylidene fluoride porous hollow fiber membrane obtained by the production method according to claim 1, 2 or 3.