METHOD AND APPARATUS FOR MANUFACTURING POROUS POLYTETRAFLUOROETHYLENE MATERIAL

Abstract: A method for manufacturing a porous polytetra­ fluoroethylene material comprising extruding or rolling or a process consisting of the both an unsintered polytetra­ fluoroethylene mixture containing a liquid lubricant, and carrying out simultaneously next four steps of a) evaporating a liquid lubricant, b) stretching the molded articles in an unsintered condition, c) sintering the same in a stretched condition, and d) stretching the same in a sintered condition at an atmospheric temperature of more than 390°C to obtain mechanical strengths such as a Young's modulus of more than 10000 kg/cm², and a matrix tensile strength of more than 1100 kg/cm².

Description: METHOD AND APPARATUS FOR lLNUFACTURING POROUS POLYTETRAFLUOROETHYLENE MATERIAL BACKGROUND OF THE INVENTION This invention relates to a method for manufacturing a porous polyetetrafluoroethylene material with high mechanical strength and more particularly to improvement in the economization of energy required for steps for removing a liquid lubricant, stretching and sintering the article. The invention also releates to an apparatus for use in such method. A porous polytetrafluoroethylene (hereinafter referred to '1PTFE") materialtakesadvantageof excellent heat resistance, chemical resistance, electric insulation and repellency of PTFE and is used in various filters, diaphragms and other waterproof gas-permeable materials, insulating materials for cables and sealing materials or the like. Various methods for manufacturing a porous PTFE material have been well known. Among others, what is commercially appealing to the market is a stretching process for making porous PTFE whose basic idea is disclosed in Japanese Patent Publication No. 13560/67. In the first step of the process, powdered PTFE and a liquid lubricant are mixed and the mixture is shaped by a paste extrusion and a calender rolling or a combination thereof to obtain an unsintered molded article in the form of a film, tube or a rod and the like. The second and subsequent steps comprises: (1) eliminating the liquid lubricant contained in the molded article by evaporation or extraction, (2) rendering the molded article porous by strentching, and (3) sintering the porous article at a temperature higher than the melting point of PTFE to fix the porous structure. The reason why the second and subsequent steps are thus subdivided is as follows. Stretching of molded PTFE containing a liquid lubricant at a temperature heretofore employed (from room temperature to a temperature lower than the crystalline melting point of PTFE) fails to lead to uniform stretching due to the action of interfacial tension of the liquid lubricant and give rise to a porous structure heterogeneous in pore size distribution. The sintering step must be carried out at a temperature higher than the crystalline melting point of PTFE. However, this step has been taken separately from the stretching step since the stretching has heretofore been carried out mostly at a temperature lower than the crystalline melting point of PTFE. It has been customary to divide the process into unit steps to be carried out at different temperatures and different speeds, thus requiring much time and energy for cr#-,eessing and wasting much labor. SUMMARY OF THE INVENTION It is, therefore, an object of the present invention to provide a method for manufacturing PTFE, which enables one to carry out eliminating of lubricants, stretching and sintering in one step in a temperature not lower than 430 C, thereby eliminating the second and subsequent steps which have heretofore been employed. Another object of the invention is to provide an apparatus for manufacturing PTFE, thereby greatly reducing processing time and saving energy required for the production of the porous PTFE material. As a result of extensive researches into temperature, speed and other operative conditions in the stretching and sintering steps, it has been found that when an unsintered PTFE molded material containing a liquid lubricant is stretched at a temperature of not lower than 3900C under the conditions under which a temperature distribution is precisely controlled, removal of the lubricant by evaporation can proceed simultaneously with stretching and sintering can also be carried out simultaneously with stretching after sintering. Through further researches on the conditions under which the steps are readily carried out, it has now been found that the method of the present invention can proceed advantageous ly by employing an oven circulating hot air as a control system for temperature distribution and providing in the furnace a catalyst which facilitates the combustion of the vaporized lubricant. The present invention is based on the above findings and provides a method for manufacturing a porous polytetrafluoroethylene materials, comprising molding a mixture of an unsintered polytetrafluoroethylene and a liquid lubricant into an article by extruding and rolling, and then by simultaneously carrying out four steps of a) removing the liquid lubricant by evaporation, b) stretching the article in an unsintered condition, c) sintering the article in a stretched condition, and d) stretching the article in a sintered condition at a temperature of more than 3900C to obtain a sintered porous polytetrafluoroethylene material having a Young modulus of more 2 than 10,000 kg/cm , and a matrix tensile strenoth of more 2 than 1,100 kg/cm BRIEF DESOTIPTION OF THE DRAWINGS Fig. 1 is a graph schematically representing the manner in which the temperature is raised in the furnace; Fig. 2 shows a graph of differential thermal spectrum in the proximity of the crystalline melting point; Fig. 3 is a schematical diagram showing the manner in which stretched tension is measured in the furnace#; Fig. 4 is a graph showing the result of measurement of the tension; Fig. 5 is a graph showing a relation between temperature and stretching ratio of PTFE under a certain tension; and Fig. 6 is a schematical cross-setional view of an apparatus used to carry out the method of the invention. DETAILED DESCRIPTION OF THE INVENTION When the unsintered PTFE molded article enters into a temperature not lower than the crystalline melting point of PTFE, the temperature of molded PTFE increases with simultaneous initiation of the evaporation of the liquid lubricant, resulting in that PTFE is maintained at a temperature less than the boiling point of the liquid lubricant due to absorption of heat of vaporization. Under such condition, tension is applied to molded PTFE so that its stretching proceeds within a limited range in an unsintered condition and proceeds to increase the surface area where the liquid lubricant has been remove. Increasing the surface area facilitates the evaporation of the liquid lubricant still left in the molded article. That is, porosification and evaporation of the liquid lubricant are simultaneously achieved. After the liquid lubricant has beew evaporated thoroughly, the temperature of PTFE gradually increases and sinterina starts when it reaches crystalline melting point of PTFE. PTFE maintains higher viscosity at a temperature not lower than the crystalline melting point and develops a fibruous structure when stretched by tension applied from the both ends thereof. The process is scehmatically shown in Figs. 1 to 5. Fig. 1 shows a temperature profile in the stage wherethe temperature is increased. When the molded article at room temperature reaches an inlet A of the furnace, it is gradually heated and its temperature is elevated to the initial boiling point B of the liquid lubricant, where the rate of the increase in the temperature becomes to reduce due to heat of vaporization. Further, when the temperature of the molded article reaches a dry distrillation point C' of lubricant, where the rate of increase in the temperature is elevated and the temperature reaches the crystalline melting point of PTFE. Since the temperature of the furnace as set is further higher, the article absorbs a certain amount of heat in tis crystalline melting temperature, and finally its temperature becomes closer to the temperature of the furnace. Referring to Fig. 2 showing data of differential thermal analysis of the unsintered PTFE molded article in the proximity of crystalline melting point, the endothermic curve shows a peak at a temperature of 3480C and a shoulder at a temperature of 3380C and further a small pe in the proximity of 3800C. These peaks are depended on the crystalline structure formed when PTFE was polymerized. On the other hand, after sintering, the above-described peaks in the endothermic curve reduce but instead a sharp peak appears at a temperature of 327 C. This means that the crystalline structure is varied before and after sintering step, and it is obvserved that the endothermic peak is shifted to the side of high temperature when the rate of increase and decrease in the temperature is higher. Fig. 3 is schematical diagram showing how much tension is applied to the molded article in a steady state in the furnace where the liquid lubricant is removed by evaporation, the article is stretched in an unsintered condition, it is sintered, and it is stretched after sintering. In this instance, a tension meter using a strain gauze is coupled to a pulley to continuously record the stress loaded on the opposite ends of PTFE in the furnace. Fig. 4 is a graph representing a dynamic tension curve when a stretch ratio is varied at a constant furnace temperature while the article is supplied to the furnace at a speed of 3m/min. Measurements are performed at furnace temperatures ranging from 2000C to 45000. Fig. 5 is a graph showing a relation betwen the furnace temperature and stretch ratio under a certain constant dynamic tension, obtained from the graph in Fig. 4. It is understood from Fig. 5 that if the PTFE molded article containing the liquid lubricant enters into the furnace as shown in Fig. 1 under conditions under which, for example, dynamic tension is exerted to load the article a stress of 100 g, little stretching occurs between the points A and B in Fig. 1 but stretching of not exceeding about 100% occurs at the point C at about 250 C. However, the article is subjected to a higher temperature as high as up to about 3500C between the points C and D and then stretched up to 800%. Between the points D and E, if the upper limit of the furnace temperature set is, for example, 4000C, stretching of not lower than 1400% is achieved simultaneously with the sintering. It is, of course, a normal procedure to predetermine the stretch ratio at the top and the bottom of the furnace so that the dynamic tension is varied according to that ratio and the stretch ratios shown at various temperatures are changed accordingly. However, it has been discovered during repeated tests that when the furnace temperature was set, for example, 4000C in excess of the endothermic peak shown in Fig. 2 (3800C), the porous PTFE material had greater mechanical properties, particularly, Young's modulus and matrix tensile strentth. More specifically, the furnace temperature#which was set at 3800C or less may not satisfy either Young's modulus of not lower than 2 10000 kg/cm or matrix tensile strength of not lower than 2 1100 dg/cm . However, the furnace temperature set at 3900C or more may satisfy both the requirements, and the self-supported porous PTFE material may be obtained convenient to handle. It is also confirmed that the PTFE molded article not containing a liquid lubricant is not qualified to satisfy Young's modulus of not lower than 10000 kg/cm2 and matrix tensile strength of not lower than 1100 kg/cm2 when supplied to the furnace. Although the physical background of the method according to the invention is still unclear, it is believe^, though not sticked to, that the phenomenon relates to a rate of temperature increase till a temperature above the endothermic peak is reached and the rate of temperature decrease once such a high temperature is reached. The method of the present invention may be suitably applicable to the various articles in the form of a film, tube or rod. Liquid lubricants which can be mixed with PTFE include those which are capable of wetting the surface of PTFE and capable of being evaporated at a temperature not higher than the melting temperature of PTFE. Preferred lubricants include those having a boiling point not higher than 2600C may be suitably used as it is readily evaporated from the molded article. Generally, petroleum hydrocarbons are used as they are easy to handle and reasonable in price. The furnace temperature at which the invention is carried out must be not lower than 3900C. Although the crystalline melting point of PTFE is 3470C, it is required to use a temperature exceeding the crystalline melting point of 3800C if it is desired to satisfy higher Young's modulus and matrix tensile strength. On the other hand, the furnace temperature affects the rate of increase in the temperature of PTFE molding. More specifically, as the furnace temperature is incrased to more than 450 C or 500CC, simultaneous operation of re oal of the liciuld lubricant, stretching and sintering of PTFE can be carried out at a higher speed. According to the present invention, It has now been confirmed that the method may be carried out so long as the temperature distribution within the furnace is controlled within the range of not more than 30 C. The higher the furnace temperature, the r.ore accurate the temperature distribution. The higher accuracy of temperature allows PTFE o be predetermined high speed, homogeneous heating d cooling. With low accuracy, fluctuations are observed in melting of crystals and recrystallization, which tend to cause micro-breakage during the treatment and result in fluctuations in the physical properties of the porous material. According to the present invention, it has been found that the oven which is adopted to circulate a hot air at a high speed to homogenize the furnace temperature distribution is well suitable for heat means which controls the temperature with high accuracy in the high temperature atmosphere. Further, it has been also discovered that incorporation into the furnace, of a catalyst which facilitates oxidization of evaporated lubricant lessens a solvent concentration in the furnace atmosphere to maintain it below explosion limit, and that thermal energy by combustion is used to the best advantage so that energy cost is greatly deducted. Since the higher a circulatine wind velocity is, the better a temperature distribution accuracy is improved in the furnace, more than 5 m/sec. wind velocity is preferable in a working temperature and 10 - 40 m/sec. wind velocity is more preferable. The velocity may be changed according to the shape of the molded article. Next, an apparatus will be described hereinafter into which the invention is well embodied. The basic structure of the apparatus is shown as in Fig. 6 and includes heat means, and supply and ta#- up means for the molded article. Heat means is a circulating hot air system. To this end, a double-cylinder piped furnace is employed wherein the molded article passes through an inner cylinder portion 4 and a heater is incorporated into an outer cylindrical portion 5. These two cylindrical portions are in connection with one another, and a hot air in the furnace is circulated at a constant flow rate by a fan 7. The furnace temperature is detected by a thermocouple 8 or the like disposed with the inner cylindrical portion as the center and is fed back by the heater for temperature control. The furnace temperature is influenced by an inflow of the air from the furnace inlet and outlet as well as a supplied speed of molded articles and combustion caloric energy of the lubricant. A pressure box 2 at the furnace inlet and a nozzle 1 at the outlet are arranged to provide an adjustable mechanism which controls inflow of the air. A portion of tne air in the furnace is forcibly discharged by an exhaust pipe 10 to maintain oxygen concentration required for combusiton in the furnace. Catalysts are mounted on one or more places where the hot air is curculated. A platinum group catalyst is one of the catalysts having excellent oxidizing capacity and is suitably used for the purpose of the invention. Means for supplying and taking-up the molded article will be d#scr####hereinafter. Basically, a takeup portion is required t3 be driven at a speed higher than a speed at which a supplying portion does since a stretching operation ts interposed When the molded article is, for example, a film, means is preferably in the form of a roll as is well suit therefor. When the molded article is a tube or a rod, means is preferably in the form of a pair of capstans with a groove to conform to the outer diameter. In addition a guide roll, a supply stand, take-up machine or various detectors are arranged as the case may be. EXAMPLE 1 A liquid lubricant naphtha No. 5 (manufactured b Shell Petroleum Co.; boiling range 152-1970C) with 25 parts by weight was mixed with a PTFE fine powder F104 (manufactured by Daikin Kogye Co., Ltd.) with 100 parts by weight and then extruded to a tube of the outer diameter of 3 mm, the inner diameter of 2 mm by a ram extruder. Next, the tube was subjected to simultaneous treatments such as removal of the lubricant and stretching, sintering the tube as shown in Table 1 at the temperature ranging from 350 - 5200C by the use of the apparatus shown in Fig. 6. As a result, a homogeneous porous tube was obtained in either case. The lubricant was fully evaporated and removed. An extracted residue (the tube was extracted in acetone to measure weight decrease before and after extraction) was shown less than 0.1 weight % in either case. Table 2 shows properties of porous tubes obtained, wherein strength characteristics of the tube obtained at the furnace temperature of more than 3900C are matrix strength of 1100 kg/cm2 and Young's modulus of more than 10000 kg/cm2. On the other hand, the tube obtained at the atmospheric temperature of 3600C results in that one of the value of either matrix tensile strength or Young's modulus in less than the afore-mentioned limit. Table 1 Test Condition Furnace Supply Take-u Stretching Test No. Temperature Speed Speed Ratio ( C) (/mien.) (m/min.) (%) 1 360 1.5 6.0 300 2 400 3.0 6.0 100 3 400 3.0 12.0 300 4 420 3.5 38.5 1000 5 520 7.0 28.0 300 6 360 2.0 22.0 1000 Table 1 Characteristics of Porous Tube Dimensions Property of Matter Test Outer Inner Poro- Bubbling Matrix Ten- Young's No. Dia. Dia. sity Point sile Strength Modulus (mm) (mm) (%) (kg/cm2) (kg/cm2) 1 2.2 1.5 65 0.32 825 8000 2 2.3 1.7 42 1.20 1150 10500 3 2.2 1.6 68 0.43 1340 11000 4 2.3 1.7 82 0.18 1240 14000 5 2.4 1.9 76 0.22 1200 20000 6 2.1 1.6 86 0.15 1150 7000 * Calculation is made according to the follow ing formula 2.2 FM = FR x dR wherein FM: matrix tensile strengh kg/mm2, FR: actual tensile strength of porous sample kg/mm2, dR: apparent specific density of porous sample. EXAMPLE 2 A liquid lubricant naphtha No. 5 with 26 parts by weight was mixed with a PTFE fine powder F104 with 100 parts by weight and then extruded to give a rod of the outer diameter of 25 mm by a ram extruder. The rod was further rolled out to a film measured in the width of 650 mm and the thickness of 0.25 mm.. The film was subjected to simultaneous treatments such as removal of the lubricant and stretching, sintering the film under a condition as shown in Table 3 by the use of the apparatus having a supply stand, a guide roll, and a take-up machine suitable for the film. Characteristics of the porous film as obtained are shown in Table 4 from which it is understood that the film is obtained with a higher strength and sufficient permeability. Table 3 Test Condition Furnace Supply Take-up Stretching Test No. Temperature Speed Speed Ratio (uc) (m/min.) (m/min.) (%) 7 350 2.0 12.0 500 8 400 4.0 12.0 200 9 t00 4.0 24.0 500 10 400 4.0 44.0 1000 11 540 10.0 30.0 200 12 540 10.0 60.0 500 13 350 3.0 33.0 1000 Table 4 Characteristics of Porous Film Matrix Tensile Dimension Strength in Test Film Perme- Longitudinal Young's No. Thickness Porosity ability Direction . Modulus (mm) (%) (Gurley (kg/cm2) (kg/cm2) sec.) 7 0.19 71.7 4.1 1200 7500 8 0.21 46.5 48.2 1120 11000 9 0.20 72.1 6.5 1150 10900 10 0.19 84.7 2.0 1360 13000 11 0.19 68.5 9.4 1270 15000 12 0.18 80.0 4.5 1460 17000 13 0.17 89.0 1.5 1200 6500 For production of the PTFE porous materials the three individual steps or processes have been heretofore requied, such as removal of the liquid lubricant, and stretching and sintering of the molded article to botain the porous materials from the paste extruded materials. According to the present invention, these three steps are performed simultaneously at one step and greatly reduce a process instrument, time and engergy and labor. While the invention has been described in detail and with reference to specific embodiments thereof, it will be apparent to one skilled in the art that various changes and modifications can be made therein without departing from the spirit and scope thereof.

Claims: WHAT IS CLAIMED IS: 1. A method for manufacturing a porous polytetrafluoroethylene material comprising extruding or rolling or a process consisting of the both an unsintered polytetrafluoroethylene mixture containing a liquid lubricant, and carrying out simultaneously next four steps of a) evaporating a liquid lubricant, b) stretching the molded articles in an unsintered condition, c) sintering the same in a stretched condition, and d) stretching the same in a sintered condition at an atmospheric temperature of more than 3900C to obtain mechanical strengths such as a Young's modulus of more than 10000 kg/cm2, and a matrix 2 tensile strength of more than 1100 kg/cm 2. A method of manufacturing a polytetrafluoroethylene porous material as described in Claim 1,characterized in that control of an atmospheric temperature at which four steps of evaporating the lubricant, stretching the molded articles in an unsintered conditiion, sintering the same in a stretched condition, and stretching the same in a sintered condition are simultaneously carried out, is made by G circulating hot air oven at wind velocity of more than 5 m/sec., and that the evaporated lubricant is burnt by an oxidizing catalyst. 3. A method of manufacturing a polyetetrafluoroethylene porous material as described in Claim 1, characterized in that a molded articles is in either form O - a film, tube or a rod. 4. A method of manufacturing a polytetrafluoroethylene porous material as described in Claim 1, characterized in that a boiling range of the lubricant is less than 26O0C. 5. A method of manufacturing a porous polytetrafluoroethylene material as described in Claim 1, characterized in that the atmospheric temperature at which four steps of evaporating the lubricant, stretching the molded articles in an unsintered condition, sinterina the same in a stretched condition, and stretching the same in a sintered condition are simultaneously carried out, is more than 4500C, and that a furnace temperature distribution is less than 300C. 6. A method of manufacturing a porous polytetrafluoroethylene material as described in Claim 1, characterized in that the atmospheric temperature at which four steps of evaporating the lubricant, sintering the molded articles in an unsintered conditions, sintering the same in a stretched condition, and stretching the same in a sintered condition are simultaneously carried out, is more than 5000C, and that a furnace temperature distribution is less than 300C. 7. An apparatus of manufacturing a porous polytetrafluoroethylene porous material from an unsintered polytetrafluroroethvlene containinq a liauid lubricant which is subiected to four stets, simultaneouslv carried out, of evaporatinq the lubricant, stretchinq the molded material in an unsintered condition, sinterinq the same in a stretched condition, and stretching the same in a sintered condition, said apparatus comprising a hot furnace including a double cylinder piped furnace of an inner cylinder part through which a molded material passes and an outer cylinder portion in which a heater is incorporated, said two cylinder parts being coupled to one another by the both ends thereof, means for circulating a hor air-thwugh said two cylinder parts, means for detecting a furnace temperature, means for adjusting an inflow of the air at an inlet and an outlet of the furnace, means for forcibly exhausting a portion of the furnace hot air, a catalyst for facilitating oxidization of the vaporized lubricant, and means for supplying the molded article to the furnace, and take-up means actuated at a speed more than such supply speed.

Inventors: ASAKO, SHIGERU C/O OSAKA WORKS, OKITA, KOICHI C/O OSAKA WORKS, TOYOOKA, SHINICHI C/O OSAKA WORKS, YAMADA, KATSUYA C/O OSAKA WORKS
Applicants: SUMITOMO ELECTRIC INDUSTRIES LIMITED
Application year: 1984
Main classification: B29C67
IPC codes: B29C55, B29D23, B29D7, B29C67