KR101051702B1 - PET resin / PF resin copolymerized fluororesin solid lubrication board and its manufacturing method - Google Patents

PET resin / PF resin copolymerized fluororesin solid lubrication board and its manufacturing method Download PDF

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KR101051702B1
KR101051702B1 KR1020090083003A KR20090083003A KR101051702B1 KR 101051702 B1 KR101051702 B1 KR 101051702B1 KR 1020090083003 A KR1020090083003 A KR 1020090083003A KR 20090083003 A KR20090083003 A KR 20090083003A KR 101051702 B1 KR101051702 B1 KR 101051702B1
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resin
pfa
ptfe
steel sheet
pfa resin
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KR20100065235A (en
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김정권
김신아
김규식
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김정권
김규식
김신아
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05DPROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D7/00Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials
    • B05D7/14Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials to metal, e.g. car bodies
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05DPROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D7/00Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials
    • B05D7/24Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials for applying particular liquids or other fluent materials
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B15/00Layered products comprising a layer of metal
    • B32B15/04Layered products comprising a layer of metal comprising metal as the main or only constituent of a layer, which is next to another layer of the same or of a different material
    • B32B15/08Layered products comprising a layer of metal comprising metal as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2/00Processes of polymerisation
    • C08F2/12Polymerisation in non-solvents
    • C08F2/16Aqueous medium
    • C08F2/22Emulsion polymerisation
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D127/00Coating compositions based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Coating compositions based on derivatives of such polymers
    • C09D127/02Coating compositions based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Coating compositions based on derivatives of such polymers not modified by chemical after-treatment
    • C09D127/12Coating compositions based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Coating compositions based on derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D7/00Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
    • C09D7/40Additives

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  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Laminated Bodies (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

본 발명의 목적은 금속강판 표면에 사출용 PTFE수지·PFA수지 공중합체를 소성에 의해 강력하게 부착시킬 수 있고, 윤활성, 내마모성, 내열성 및 내화학성이 뛰어나고, 용이하게 대량 생산이 가능함과 동시에, 제조 비용을 절감할 수 있는 PTFE수지·PFA수지 공중합 불소수지계 고체윤활기판 및 그 제조방법을 제공하는데 있다.An object of the present invention is to be able to strongly adhere the PTFE resin and PFA resin copolymer for injection to the surface of the metal steel sheet by sintering, excellent lubricity, wear resistance, heat resistance and chemical resistance, easy mass production, and at the same time To provide a cost-effective PTFE resin and PFA resin copolymerized fluororesin-based solid lubrication substrate and a method of manufacturing the same.

PTFE수지, PFA수지, 압출용수지, 유화중합 PTFE resin, PFA resin, extrusion resin, emulsion polymerization

Description

PTFE수지·PFA수지 공중합 불소수지계 고체윤활기판 및 그 제조방법{Solid lubricate PTFE·PFA co-polymer resin film and manufacturing method thereof} PTF resin and PFA resin copolymerized fluororesin-based solid lubrication substrate and its manufacturing method {Solid lubricate PTFE · PFA co-polymer resin film and manufacturing method}

본 발명은 PTFE수지·중합 불소수지계 고체윤활기판 및 그 제조방법에 관한 것으로서, 금속강판 표면에 사출용 PTFE수지·PFA수지 공중합체를 소성에 의해 강력하게 부착시킬 수 있고, 윤활성, 내마모성, 내열성 및 내화학성이 뛰어나고, 용이하게 대량 생산이 가능함과 동시에, 제조 비용을 절감할 수 있는 PTFE수지·PFA수지 공중합 불소수지계 고체윤활기판 및 그 제조방법에 관한 것이다.The present invention relates to a PTFE resin, a polymerized fluororesin-based solid lubrication substrate, and a method for manufacturing the same, which can strongly adhere an injection-molded PTFE resin and a PFA resin copolymer to the surface of a metal steel sheet by sintering, and include lubrication, abrasion resistance, heat resistance, and the like. The present invention relates to a PTFE resin and a PFA resin copolymerized fluororesin-based solid lubrication substrate which is excellent in chemical resistance, can be easily mass-produced, and can reduce manufacturing costs.

종래로부터 널리 사용되고 있는 불소수지계인 4불화에틸렌수지(poly tetra fluoro ethylene, 이하 PTFE라고 약칭한다) 수지는 모든 산(酸)이나 알칼리 및 용매에 잘 견디는 우수한 특성을 가지고 있어 내약품성 및 내후성이 다른 수지에 비하여 우수하며, 용융점은 327℃로 매우 높기 때문에 -100℃의 저온에서부터 250℃의 고온까지 안전하게 사용할 수 있으며, 특히 윤활성과 내마모성이 우수하므로 윤 활성, 내마모성, 내열성, 내화학성이 우수하여 사용수명이 긴 고체 윤활베어링의 고체윤활기판으로 널리 이용되고 있다.Polytetrafluorofluoroethylene (hereinafter referred to as PTFE) resin, a fluorine resin system widely used in the past, has excellent properties to withstand all acids, alkalis, and solvents, and thus has different chemical resistance and weather resistance. Compared with the high melting point of 327 ℃, it can be safely used from low temperature of -100 ℃ to high temperature of 250 ℃. Especially, it has excellent lubricity and abrasion resistance, so it has excellent lubricity, abrasion resistance, heat resistance and chemical resistance. It is widely used as a solid lubrication substrate of this long solid lubrication bearing.

그런데, PTFE수지는 내열 및 내약품성이 우수하기 때문에 용융가공이 불가능하며 용매, 접착제가 없으므로 금속표면에 고체 윤활제인 PTFE 수지박막을 부착시켜 만든 고체윤활기판 제조에 특별한 처리가 필요하는 등 성형공정과 사용면에서 많은 제약이 있다.However, since PTFE resin is excellent in heat resistance and chemical resistance, it is impossible to melt processing, and since there is no solvent or adhesive, special processing is required to manufacture a solid lubrication substrate made by attaching a PTFE resin thin film, which is a solid lubricant, on the metal surface. There are many restrictions in terms of use.

종래로부터 불소수지를 이용한 고체윤활기판을 제조하려면 불소수지가 금속표면과의 부착력이 약하기 때문에 금속강판 위에 청동분말을 분말야금법으로 강하게 융착시켜서 다공성이 많은 청동분말 소결층을 형성하고 그 위에 불소수지 분산액을 분산시킨 후 건조 경화시켜 고체윤활기판을 제조하고 있었다.Conventionally, in order to manufacture a solid lubrication substrate using fluorine resin, since the fluorine resin has a weak adhesion to the metal surface, the bronze powder is strongly fused by a metallurgy method on the metal steel sheet to form a porous bronze powder sintered layer, and the fluorine resin is formed thereon. The dispersion was dispersed and then dried and cured to prepare a solid lubricating substrate.

그런데, 이와 같이 제조한 고체윤활기판은 표면에 균열이 발생되거나 두께를 균일하게 제조할 수 없을 뿐만 아니라 제조공정이 복잡하여 제조비용이 매우 비싸진다는 등의 여러 가지 문제점이 있다.However, the solid lubrication substrate prepared in this way has various problems, such as not only cracking the surface or manufacturing the thickness uniformly, but also making the manufacturing process complicated and making the manufacturing cost very expensive.

또한, 청동이나 스텐레스강의 직경이 0.23∼0.50㎜인 금속사를 가로 세로 엮은 금속망 사이의 공간에 고체윤활수지를 많이 함침시킨 다음, 압착시켜서 금속망과 고체윤활제층을 고착시킨 금속망 강화 고체윤활기판이 제조되고 있었으나 금속망을 대각선 방향으로 잡아당길 경우 금속사 끼리의 접촉부위가 엇갈려서 인장강도 및 기계적 강도가 감소되고 또한 윤활기판이 손상되는 문제점이 있으며, 제조공정이 복잡하고 제조비용이 매우 비싸진다는 등의 여러 가지 문제점이 있다.In addition, the metal-reinforced solid lubrication in which a metal lubricant having a diameter of 0.23 to 0.50 mm of bronze or stainless steel is impregnated with a lot of solid lubrication resin in the space between the woven metal mesh and then pressed to fix the metal mesh and the solid lubricant layer. Although the substrate was being manufactured, when the metal mesh is pulled in a diagonal direction, the contact points between the metal yarns are staggered, so that the tensile strength and mechanical strength are reduced, and the lubrication substrate is damaged, and the manufacturing process is complicated and the manufacturing cost is very expensive. There are several problems.

따라서, 본 발명은 상기 여러 가지 문제점을 해결하기 위하여 이루어진 것으로서, 본 발명의 목적은 금속강판 표면에 사출용 PTFE수지·PFA수지 공중합체를 소성에 의해 강력하게 부착시킬 수 있는 고체윤활기판 및 그 제조방법을 제공하는데 있다.Accordingly, the present invention has been made to solve the above various problems, and an object of the present invention is a solid lubrication substrate capable of strongly attaching an injection-molded PTFE resin / PFA resin copolymer to a surface of a metal steel sheet by sintering and its manufacture To provide a method.

본 발명의 다른 목적은 윤활성, 내마모성, 내열성 및 내화학성이 뛰어난 불소수지계 고체윤활기판 및 그 제조방법을 제공하는데 있다.Another object of the present invention is to provide a fluororesin-based solid lubrication substrate having excellent lubricity, abrasion resistance, heat resistance and chemical resistance, and a method of manufacturing the same.

본 발명의 또 다른 목적은 용이하게 대량 생산할 수 있고, 제조비용을 크게 절감시킬 수 있는 불소수지계 고체윤활기판 및 그 제조방법을 제공하는데 있다.Still another object of the present invention is to provide a fluororesin-based solid lubrication substrate and a method of manufacturing the same, which can be easily mass-produced and greatly reduce the manufacturing cost.

본 발명은 상기 목적을 달성하기 위하여 이루어진 것으로서, 본 발명의 PTFE수지·PFA수지 공중합 불소수지계 고체윤활의 제조방법은 입도가 0.15 내지 0.50㎛의 미세한 PTFE수지 44.5 내지 55.50중량%, 입도가 0.15 내지 0.50㎛의 미세한 PFA수지 1.5 내지 2.50중량%, 입도가 0.15 내지 0.50㎛의 미세한 천연흑연분말 2.0 내지 2.8중량%, 증류수 39.7 내지 50.0중량% 및 비이온성 분산제 0.3 내지 0.80중량%를 용기에 넣고 교반하여 PTFE수지·PFA수지 및 천연흑연분말을 균일하게 분산시켜서 혼합하여 PH가 9.0인 알칼리성 혼합액을 제조하는 PTFE수지·PFA수지·천연흑연 분말혼합액 제조단계와; 상기 PTFE수지·PFA수지·천연흑연 분말혼합액 제조 단계에서 제조한 PTFE수지·PFA수지·천연흑연 분말 혼합액을 -5℃의 저온에서 24시간 냉동시키고 다시 해빙시키는 냉동 유화중합법에 의해 저중합도의 유상물을 제조하는 냉동 유화중합단계와; 상기 냉동 유화중합단계에서 중합된 저중합도의 유상물을 80℃ 내지 100℃의 온도로 유지된 수조 내에서 150분 내지 210분 동안 가열하면서 수분을 증발시켜서 중합도가 증가된 고무상 반고체형의 점도가 높은(반죽 형태) 압출용 PTFE수지·PFA수지 공중합체를 제조하는 압출용 PTFE수지·PFA수지 공중합체 제조단계와; 상기 압출용 PTFE수지·PFA수지 공중합체 제조단계에서 제조한 고무상 반고체형 압출용 PTFE수지·PFA수지 공중합체를 0.25 내지 0.35㎜ 두께의 철강판 위에 올려놓고 100℃ 내지 140℃로 가열된 압축롤러에 의해 550 내지 610㎏/㎠의 압력을 인가하여 상기 철강판의 상부 표면에 불소수지계 고체윤활제층을 압축중합시켜서 상기 철강판의 상부 표면에 불소수지계 고체윤활제층을 고착시키는 불소수지계 고체윤활제층 고착단계와; 상기 불소수지계 고체윤활제층 고착단계에서 0.25 내지 0.35㎜ 두께의 철강판 의 상부 표면에 0.15 내지 0.25㎜ 두께의 불소수지계 고체윤활제층을 고착시킨 고체윤활기판을 300℃ 내지 380℃의 온도로 유지된 컨베이어 시스템의 자동 전기로에서 15분 내지 25분 동안 가열소성하여 불소수지를 경화시켜 철강판에 불소수지가 부착된 고체윤활기판을 제조하는 고체윤활기판 제조단계를 포함하는 것을 특징으로 한다.The present invention has been made to achieve the above object, the method of producing a PTFE resin / PFA resin copolymerized fluorine resin-based solid lubrication of the present invention is 44.5 to 55.50% by weight, fine particles of 0.15 to 0.50㎛ particle size, 0.15 to 0.50 1.5 to 2.50 wt% of fine PFA resin, 2.0 to 2.8 wt% of fine natural graphite powder having a particle size of 0.15 to 0.50 μm, 39.7 to 50.0 wt% of distilled water, and 0.3 to 0.80 wt% of nonionic dispersant were added to a container and stirred A step of preparing a PTFE resin, a PFA resin, and a natural graphite powder mixture, wherein the resin, PFA resin and natural graphite powder are uniformly dispersed and mixed to produce an alkaline mixture having a pH of 9.0; The PTFE resin, PFA resin, and natural graphite powder mixture prepared in the step of preparing the PTFE resin, PFA resin, and natural graphite powder mixture are refrigerated at 24 ° C. at -5 ° C. for 24 hours and then thawed again by a freeze emulsion polymerization method. Frozen emulsion polymerization step of producing water; The viscosity of the rubbery semi-solid polymer having increased polymerization degree by evaporating water while heating the low-polymerization oil polymerized in the freezing emulsion polymerization step for 150 minutes to 210 minutes in a water tank maintained at a temperature of 80 ° C to 100 ° C A step of preparing an extruded PTFE resin and a PFA resin copolymer for producing a high (dough form) extruded PTFE resin and a PFA resin copolymer; A compression roller heated to 100 ° C. to 140 ° C. by placing a rubbery semi-solid extrusion PTFE resin and PFA resin copolymer prepared in the step of manufacturing the extruded PTFE resin and PFA resin copolymer on a steel sheet having a thickness of 0.25 to 0.35 mm. By applying a pressure of 550 to 610 kg / cm 2 to compress and polymerize the fluororesin-based solid lubricant layer on the upper surface of the steel sheet to fix the fluororesin-based solid lubricant layer on the upper surface of the steel sheet. Steps; In the fixing step of the fluororesin-based solid lubricant layer, a conveyor on which a solid lubrication substrate on which a fluororesin-based solid lubricant layer of 0.15 to 0.25 mm thickness is fixed to an upper surface of a steel sheet of 0.25 to 0.35 mm thickness is maintained at a temperature of 300 ° C to 380 ° C. It is characterized in that it comprises a solid lubrication substrate manufacturing step of producing a solid lubrication substrate is attached to the steel plate by curing the fluorine resin by heat-fired for 15 to 25 minutes in the automatic electric furnace of the system.

또한, 본 발명의 PTFE수지·PFA수지 공중합 불소수지계 고체윤활기판은 본 발명의 PTFE수지·PFA수지 공중합 불소수지계 고체윤활기판의 제조방법에 의해서 제조한 것을 특징으로 한다.Further, the PTFE resin / PFA resin copolymerized fluororesin-based solid lubrication substrate of the present invention is produced by the method for producing the PTFE resin / PFA resin copolymerized fluororesin-based solid lubrication substrate of the present invention.

본 발명의 PTFE수지·PFA수지 공중합 불소수지계 고체윤활기판 및 그 제조방법에 의하면, 금속강판 표면에 사출용 PTFE수지·PFA수지 공중합체를 소성에 의해 강력하게 부착시킬 수 있고, 윤활성, 내마모성, 내열성 및 내화학성이 뛰어나고, 용이하게 대량 생산이 가능함과 동시에, 제조 비용을 절감할 수 있다는 뛰어난 효과가 있다.According to the PTFE resin and PFA resin copolymerized fluororesin-based solid lubrication substrate of the present invention and a method for producing the same, the PTFE resin and PFA resin copolymer for injection can be strongly adhered to the surface of the metal steel sheet by sintering, and the lubricity, abrasion resistance, and heat resistance And excellent in chemical resistance, easy mass production, and at the same time has an excellent effect of reducing the manufacturing cost.

본 발명의 바람직한 일실시예에 따른 PTFE수지·PFA(불화에틸렌 알코옥사이드(Per Fluoro Alcoxide resine ; 이하 PFA라고 약칭한다)수지 공중합 불소수지계 고체윤활기판의 제조방법에 대하여 실시예를 들어서 상세하게 설명한다.A method for producing a PTFE resin / PFA (Per Fluoro Alcoxide resine; PFA) resin copolymerized fluororesin-based solid lubrication substrate according to a preferred embodiment of the present invention will be described in detail with reference to Examples. .

실시예1Example 1

입도(입자 사이즈)가 0.15 내지 0.50㎛의 미세한 PTFE수지 44.5중량%, 입도가 0.15 내지 0.50㎛의 미세한 PFA수지 2.50중량%, 입도가 0.15 내지 0.50㎛의 미세한 천연흑연분말 2.50중량%, 증류수 50중량% 및 비이온성 분산제(또는 계면활성제라고도 한다) 0.50중량%를 용기(예를 들면, 스테인레스 용기, 플라스틱 용기 또는 유리용기)에 넣고 저속(회전속도 ; 10 내지 50 r.p.m의 속도)으로 교반하여 PTFE수지·PFA수지 및 천연흑연분말을 균일하게 분산시켜서 혼합하여 PH가 9.0인 알칼리성 혼합액을 제조하였다(PTFE수지·PFA수지·천연흑연 분말혼합액 제조단계 ).44.5% by weight of fine PTFE resin having a particle size (particle size) of 0.15 to 0.50 μm, 2.50% by weight of fine PFA resin having a particle size of 0.15 to 0.50 μm, 2.50% by weight of fine natural graphite powder having a particle size of 0.15 to 0.50 μm, and 50% by weight of distilled water. % And 0.50% by weight of a nonionic dispersant (also called a surfactant) are placed in a vessel (e.g., a stainless vessel, a plastic vessel or a glass vessel) and stirred at low speed (rotational speed; 10-50 rpm) for PTFE resin. PFA resin and natural graphite powder were uniformly dispersed and mixed to prepare an alkaline mixed liquid having a pH of 9.0 (PTFE resin, PFA resin, natural graphite powder mixture preparation step).

상기 PTFE수지·PFA수지·천연흑연 분말혼합액 제조단계에서 제조한 PTFE수지·PFA수지·천연흑연 분말 혼합액을 -5℃의 저온에서 24시간 냉동시키고 다시 해빙시키는 냉동 유화중합법에 의해 저중합도의 유상물(油狀物)을 제조하였다(냉동 유화중합단계).The PTFE resin, PFA resin, and natural graphite powder mixture prepared in the step of preparing the PTFE resin, PFA resin, and natural graphite powder mixture are refrigerated at 24 ° C. at -5 ° C. for 24 hours and then thawed again by a freeze emulsion polymerization method. Water was prepared (freezing emulsion polymerization step).

상기 냉동 유화중합단계에서 중합된 저중합도의 유상물을 80℃ 내지 100℃의 온도로 유지된 수조 내에서 150분 내지 210분 동안 가열하면서 수분을 증발시켜서 중합도가 증가된 고무상 반고체형의 점도가 높은(예를 들면, 반죽 형태) 압출용 PTFE수지·PFA수지 공중합체를 제조하였다(압출용 PTFE수지·PFA수지 공중합체 제조단계).The viscosity of the rubbery semi-solid polymer having increased polymerization degree by evaporating water while heating the low-polymerization oil polymerized in the freezing emulsion polymerization step for 150 minutes to 210 minutes in a water tank maintained at a temperature of 80 ° C to 100 ° C A high (e.g., dough-like) extrusion PTFE resin / PFA resin copolymer was prepared (extrusion step for preparing PTFE resin / PFA resin copolymer).

상기 압출용 PTFE수지·PFA수지 공중합체 제조단계에서 제조한 고무상 반고체형 압출용 PTFE수지·PFA수지 공중합체를 0.25 내지 0.35㎜ 두께의 철강판 위에 올려놓고 100℃ 내지 140℃로 가열된 압축롤러에 의해 550 내지 610㎏/㎠의 압력을 인가하여 상기 철강판의 상부 표면에 불소수지계 고체윤활제층을 압축중합시켜서 상기 철강판의 상부 표면에 불소수지계 고체윤활제층을 고착시켰다(불소수지계 고체윤활제층 고착단계).A compression roller heated to 100 ° C. to 140 ° C. by placing a rubbery semi-solid extrusion PTFE resin and PFA resin copolymer prepared in the step of manufacturing the extruded PTFE resin and PFA resin copolymer on a steel sheet having a thickness of 0.25 to 0.35 mm. By applying a pressure of 550 to 610 kg / cm 2 to compress and polymerize the fluororesin-based solid lubricant layer on the upper surface of the steel plate to fix the fluororesin-based solid lubricant layer on the upper surface of the steel plate (fluorine resin-based solid lubricant layer). Fixation phase).

상기 불소수지계 고체윤활제층 고착단계에서 0.25 내지 0.35㎜ 두께의 철강판 의 상부 표면에 0.15 내지 0.25㎜ 두께의 불소수지계 고체윤활제층을 고착시킨 고체윤활기판을 300℃ 내지 380℃의 온도로 유지된 컨베이어 시스템의 자동 전기로에서 15분 내지 25분 동안 가열소성하여 불소수지를 경화시켜 철강판에 불소수지가 부착된 고체윤활기판을 제조하였다(고체윤활기판 제조단계).In the fixing step of the fluororesin-based solid lubricant layer, a conveyor on which a solid lubrication substrate on which a fluororesin-based solid lubricant layer of 0.15 to 0.25 mm thickness is fixed to an upper surface of a steel sheet of 0.25 to 0.35 mm thickness is maintained at a temperature of 300 ° C to 380 ° C. Heat-fired for 15 to 25 minutes in the automatic electric furnace of the system to cure the fluorine resin to prepare a solid lubrication substrate attached to the steel plate (solid lubrication substrate manufacturing step).

실시예2Example 2

입도(입자 사이즈)가 0.15 내지 0.50㎛의 미세한 PTFE수지 55.50중량%, 입도가 0.15 내지 0.50㎛의 미세한 PFA수지 2.00중량%, 입도가 0.15 내지 0.50㎛의 미세한 천연흑연분말 2.00중량%, 증류수 39.70중량% 및 비이온성 분산제 0.80중량%를 용기에 넣고 저속으로 교반하여 PTFE수지·PFA수지 및 천연흑연분말을 균일하게 분산시켜서 혼합하여 PH가 9.0인 알칼리성 혼합액을 제조하였다(PTFE수지·PFA수지·천연흑연 분말혼합액 제조단계).55.50 wt% of fine PTFE resin with particle size (particle size) of 0.15 to 0.50 μm, 2.00 wt% of fine PFA resin with particle size of 0.15 to 0.50 μm, 2.00 wt% of fine natural graphite powder with particle size of 0.15 to 0.50 μm, and distilled water 39.70 weight % And 0.80% by weight of a nonionic dispersant were put in a container and stirred at a low speed to uniformly disperse and mix PTFE resin, PFA resin and natural graphite powder to prepare an alkaline mixed liquid having a pH of 9.0 (PTFE resin, PFA resin, and natural graphite). Powder mixture preparation step).

상기 PTFE수지·PFA수지·천연흑연 분말혼합액 제조단계에서 제조한 PTFE수지·PFA수지·천연흑연 분말 혼합액을 -5℃의 저온에서 24시간 냉동시키고 다시 해빙시키는 냉동 유화중합법에 의해 저중합도의 유상물을 제조하였다(냉동 유화중합단계).The PTFE resin, PFA resin, and natural graphite powder mixture prepared in the step of preparing the PTFE resin, PFA resin, and natural graphite powder mixture are refrigerated at 24 ° C. at -5 ° C. for 24 hours and then thawed again by a freeze emulsion polymerization method. Water was prepared (freezing emulsion polymerization step).

상기 냉동 유화중합단계에서 중합된 저중합도의 유상물을 80℃ 내지 100℃의 온도로 유지된 수조 내에서 150분 내지 210분 동안 가열하면서 수분을 증발시켜서 중합도가 증가된 고무상 반고체형의 점도가 높은 압출용 PTFE수지·PFA수지 공중합체를 제조하였다(압출용 PTFE수지·PFA수지 공중합체 제조단계).The viscosity of the rubbery semi-solid polymer having increased polymerization degree by evaporating water while heating the low-polymerization oil polymerized in the freezing emulsion polymerization step for 150 minutes to 210 minutes in a water tank maintained at a temperature of 80 ° C to 100 ° C A high extrusion PTFE resin / PFA resin copolymer was prepared (preparation step of PTFE resin / PFA resin copolymer for extrusion).

상기 압출용 PTFE수지·PFA수지 공중합체 제조단계에서 제조한 고무상 반고체형 압출용 PTFE수지·PFA수지 공중합체를 0.25 내지 0.35㎜ 두께의 철강판 위에 올려놓고 100℃ 내지 140℃로 가열된 압축롤러에 의해 550 내지 610㎏/㎠의 압력을 인가하여 상기 철강판의 상부 표면에 불소수지계 고체윤활제층을 압축중합시켜서 상기 철강판의 상부 표면에 불소수지계 고체윤활제층을 고착시켰다(불소수지계 고체윤활제층 고착단계).A compression roller heated to 100 ° C. to 140 ° C. by placing a rubbery semi-solid extrusion PTFE resin and PFA resin copolymer prepared in the step of manufacturing the extruded PTFE resin and PFA resin copolymer on a steel sheet having a thickness of 0.25 to 0.35 mm. By applying a pressure of 550 to 610 kg / cm 2 to compress and polymerize the fluororesin-based solid lubricant layer on the upper surface of the steel plate to fix the fluororesin-based solid lubricant layer on the upper surface of the steel plate (fluorine resin-based solid lubricant layer). Fixation phase).

상기 불소수지계 고체윤활제층 고착단계에서 0.25 내지 0.35㎜ 두께의 철강판 의 상부 표면에 0.15 내지 0.25㎜ 두께의 불소수지계 고체윤활제층을 고착시킨 고체윤활기판을 300℃ 내지 380℃의 온도로 유지된 컨베이어 시스템의 자동 전기로에서 15분 내지 25분 동안 가열소성하여 불소수지를 경화시켜 철강판에 불소수지가 부착된 고체윤활기판을 제조하였다(고체윤활기판 제조단계).In the fixing step of the fluororesin-based solid lubricant layer, a conveyor on which a solid lubrication substrate on which a fluororesin-based solid lubricant layer of 0.15 to 0.25 mm thickness is fixed to an upper surface of a steel sheet of 0.25 to 0.35 mm thickness is maintained at a temperature of 300 ° C to 380 ° C. Heat-fired for 15 to 25 minutes in the automatic electric furnace of the system to cure the fluorine resin to prepare a solid lubrication substrate attached to the steel plate (solid lubrication substrate manufacturing step).

실시예3Example 3

입도(입자 사이즈)가 0.15 내지 0.50㎛의 미세한 PTFE수지 51.90중량%, 입도가 0.15 내지 0.40㎛의 미세한 PFA수지 1.50중량%, 입도가 0.15 내지 0.50㎛의 미세한 천연흑연분말 2.80중량%, 증류수 43.50중량% 및 비이온성 분산제 0.30중량%를 용기에 넣고 저속으로 교반하여 PTFE수지·PFA수지 및 천연흑연분말을 균일하게 분산시켜서 혼합하여 PH가 9.0인 알칼리성 혼합액을 제조하였다(PTFE수지·PFA수지·천연흑연 분말혼합액 제조단계).51.90% by weight of fine PTFE resin having a particle size (particle size) of 0.15 to 0.50 μm, 1.50% by weight of fine PFA resin having a particle size of 0.15 to 0.40 μm, 2.80% by weight of fine natural graphite powder having a particle size of 0.15 to 0.50 μm, and 43.50 weight of distilled water % And 0.30% by weight of a nonionic dispersant were added to a container and stirred at low speed to uniformly disperse and mix PTFE resin, PFA resin and natural graphite powder to prepare an alkaline mixed liquid having a pH of 9.0 (PTFE resin, PFA resin, and natural graphite). Powder mixture preparation step).

상기 PTFE수지·PFA수지·천연흑연 분말혼합액 제조단계에서 제조한 PTFE수지·PFA수지·천연흑연 분말 혼합액을 -5℃의 저온에서 24시간 냉동시키고 다시 해빙시키는 냉동 유화중합법에 의해 저중합도의 유상물을 제조하였다(냉동 유화중합단계).The PTFE resin, PFA resin, and natural graphite powder mixture prepared in the step of preparing the PTFE resin, PFA resin, and natural graphite powder mixture are refrigerated at 24 ° C. at -5 ° C. for 24 hours and then thawed again by a freeze emulsion polymerization method. Water was prepared (freezing emulsion polymerization step).

상기 냉동 유화중합단계에서 중합된 저중합도의 유상물을 80℃ 내지 100℃의 온도로 유지된 수조 내에서 150분 내지 210분 동안 가열하면서 수분을 증발시켜서 중합도가 증가된 고무상 반고체형의 점도가 높은 압출용 PTFE수지·PFA수지 공중합체를 제조하였다(압출용 PTFE수지·PFA수지 공중합체 제조단계).The viscosity of the rubbery semi-solid polymer having increased polymerization degree by evaporating water while heating the low-polymerization oil polymerized in the freezing emulsion polymerization step for 150 minutes to 210 minutes in a water tank maintained at a temperature of 80 ° C to 100 ° C A high extrusion PTFE resin / PFA resin copolymer was prepared (preparation step of PTFE resin / PFA resin copolymer for extrusion).

상기 압출용 PTFE수지·PFA수지 공중합체 제조단계에서 제조한 고무상 반고체형 압출용 PTFE수지·PFA수지 공중합체를 0.25 내지 0.35㎜ 두께의 철강판 위에 올려놓고 100℃ 내지 140℃로 가열된 압축롤러에 의해 550 내지 610㎏/㎠의 압력을 인가하여 상기 철강판의 상부 표면에 불소수지계 고체윤활제층을 압축중합시켜서 상기 철강판의 상부 표면에 불소수지계 고체윤활제층을 고착시켰다(불소수지계 고체윤활제층 고착단계).A compression roller heated to 100 ° C. to 140 ° C. by placing a rubbery semi-solid extrusion PTFE resin and PFA resin copolymer prepared in the step of manufacturing the extruded PTFE resin and PFA resin copolymer on a steel sheet having a thickness of 0.25 to 0.35 mm. By applying a pressure of 550 to 610 kg / cm 2 to compress and polymerize the fluororesin-based solid lubricant layer on the upper surface of the steel plate to fix the fluororesin-based solid lubricant layer on the upper surface of the steel plate (fluorine resin-based solid lubricant layer). Fixation phase).

비교예Comparative example

입도(입자 사이즈)가 0.15 내지 0.50㎛의 미세한 PTFE수지 40.0중량%, 입도가 0.15 내지 0.50㎛의 미세한 PFA수지 7.50중량%, 입도가 0.15 내지 0.50㎛의 미세한 천연흑연분말 3.50중량%를 48.70중량%의 증류수 및 0.30중량%의 비이온성 분산제를 용기에 넣고 저속으로 교반하여 PTFE수지·PFA수지 및 천연흑연분말을 균일하게 분산시켜서 혼합하여 PH가 9.0인 알칼리성 혼합액을 제조하였다(PTFE수지·PFA수지·천연흑연 분말혼합액 제조단계).40.0 wt% of fine PTFE resin having a particle size (particle size) of 0.15 to 0.50 μm, 7.50 wt% of fine PFA resin having a particle size of 0.15 to 0.50 μm, and 3.50 wt% of fine natural graphite powder having a particle size of 0.15 to 0.50 μm. Distilled water and 0.30% by weight of a nonionic dispersant were put in a container and stirred at low speed to uniformly disperse and mix PTFE resin, PFA resin and natural graphite powder to prepare an alkaline mixed liquid having a pH of 9.0 (PTFE resin, PFA resin, Natural graphite powder mixture).

상기 PTFE·PFA·천연흑연 분말혼합액 제조단계에서 제조한 PTFE·PFA·천연흑연 분말 혼합액을 -5℃의 저온에서 24시간 냉동시키고 다시 해빙시키는 냉동 유화중합법에 의해 저중합도의 유상물을 제조하였다(냉동 유화중합단계).Low-polymerization oil was prepared by freezing emulsion polymerization in which the PTFE, PFA, and graphite powder mixtures prepared in the above PTFE, PFA, and graphite graphite powder mixture were frozen for 24 hours at -5 ° C and thawed again. (Frozen emulsion polymerization step).

상기 냉동 유화중합단계에서 중합된 저중합도의 유상물을 80℃ 내지 100℃의 온도로 유지된 수조 내에서 150분 내지 210분 동안 가열하면서 수분을 증발시켜서 중합도가 증가된 고무상 반고체형의 점도가 높은 압출용 PTFE수지·PFA수지 공중합체를 제조하였다(압출용 PTFE수지·PFA수지 공중합체 제조단계).The viscosity of the rubbery semi-solid polymer having increased polymerization degree by evaporating water while heating the low-polymerization oil polymerized in the freezing emulsion polymerization step for 150 minutes to 210 minutes in a water tank maintained at a temperature of 80 ° C to 100 ° C A high extrusion PTFE resin / PFA resin copolymer was prepared (preparation step of PTFE resin / PFA resin copolymer for extrusion).

상기 압출용 PTFE수지·PFA수지 공중합체 제조단계에서 제조한 고무상 반고체형 압출용 PTFE수지·PFA수지 공중합체를 0.25 내지 0.35㎜ 두께의 철강판 위에 올려놓고 100℃ 내지 140℃로 가열된 압축롤러에 의해 550 내지 610㎏/㎠의 압력을 인가하여 상기 철강판의 상부 표면에 불소수지계 고체윤활제층을 압축중합시켜서 상기 철강판의 상부 표면에 불소수지계 고체윤활제층을 고착시켰다(불소수지계 고체윤활제층 고착단계).A compression roller heated to 100 ° C. to 140 ° C. by placing a rubbery semi-solid extrusion PTFE resin and PFA resin copolymer prepared in the step of manufacturing the extruded PTFE resin and PFA resin copolymer on a steel sheet having a thickness of 0.25 to 0.35 mm. By applying a pressure of 550 to 610 kg / cm 2 to compress and polymerize the fluororesin-based solid lubricant layer on the upper surface of the steel plate to fix the fluororesin-based solid lubricant layer on the upper surface of the steel plate (fluorine resin-based solid lubricant layer). Fixation phase).

상기 불소수지계 고체윤활제층 고착단계에서 0.25 내지 0.35㎜ 두께의 철강판 의 상부 표면에 0.15 내지 0.25㎜ 두께의 불소수지계 고체윤활제층을 고착시킨 고체윤활기판을 300℃ 내지 380℃의 온도로 유지된 컨베이어 시스템의 자동 전기로에서 15분 내지 25분 동안 가열소성하여 불소수지를 경화시켜 철강판에 불소수지가 부착된 고체윤활기판을 제조하였다(고체윤활기판 제조단계).In the fixing step of the fluororesin-based solid lubricant layer, a conveyor on which a solid lubrication substrate on which a fluororesin-based solid lubricant layer of 0.15 to 0.25 mm thickness is fixed to an upper surface of a steel sheet of 0.25 to 0.35 mm thickness is maintained at a temperature of 300 ° C to 380 ° C. Heat-fired for 15 to 25 minutes in the automatic electric furnace of the system to cure the fluorine resin to prepare a solid lubrication substrate attached to the steel plate (solid lubrication substrate manufacturing step).

상기 비교예에서 제조한 고체 윤활기판의 두께는 0.50㎜로서, 본 발명의 실시예1의 가장 얇은 두께보다 0.01mm 감소하였으며, 고체 윤활제층과 철강판과의 부착력은 매우 양호하였으나, 고체 윤활기판의 상태가 거칠었고, 표면에 미세한 클랙이 발생하여 고체 윤활기판으로 사용할 수 없었다. The thickness of the solid lubrication substrate prepared in the comparative example was 0.50 mm, 0.01 mm less than the thinnest thickness of Example 1 of the present invention, the adhesion between the solid lubricant layer and the steel plate was very good, The condition was rough, and fine cracks were generated on the surface and could not be used as a solid lubrication substrate.

이러한 현상은 실시예1의 PTFE수지와 PFA수지의 조성은 증류수 50중량%에 대하여 PTFE수지 44.5중량%, PFA수지 2.5중량%인데 비하여 비교예2의 PTFE수지와 PFA수지의 조성은 증류수 48.70중량%에 비하여 PTFE수지 40중량%, PFA수지 7.5중량%로 써 비교예에서 첨가한 PFA수지 함량 7.5중량%는 실시예1의 PFA수지 함량 2.5중량%의 3배가 많이 함유되어 300℃ 내지 380℃의 온도로 유지된 컨베이어 시스템의 자동전기로에서 15분 내지 25분간 가열 소성하여 불소수지를 경화시킬 때 용융점이 낮은 PFA수지 성분이 빨리 용융하여 철 강판에 부착과 함께 PTFE 수지에 확산되면서 중합도가 더욱 커지면서 불소수지가 수축되기 때문이라 생각된다.This phenomenon is that the composition of PTFE resin and PFA resin of Example 1 is 44.5% by weight PTFE resin and 2.5% by weight PFA resin with respect to 50% by weight of distilled water, while the composition of PTFE and PFA resin of Comparative Example 2 is 48.70% by weight distilled water. Compared to 40% by weight of PTFE resin and 7.5% by weight of PFA resin, the 7.5% by weight of PFA resin added in Comparative Example contained 3 times as much as 2.5% by weight of PFA resin of Example 1, and the temperature of 300 ° C to 380 ° C. When hardening the fluororesin by heating and baking in an automatic electric furnace of a conveyor system maintained at 15 minutes, the PFA resin component having a low melting point melts quickly and adheres to the iron steel sheet and diffuses into PTFE resin, thereby increasing the degree of polymerization. Is considered to be contracted.

상기 설명에 있어서, 고체윤활기판에 사용되는 철강판은 PTFE수지 및 PFA수지의 기계적 강도를 유지하기 위하여 청동판, 아연 도금강판, 스텐레스 강판, 55% 알루미늄-아연강판 중에서 선택된 어느 하나를 사용할 수 있으나 그 중에서도 55% 알루미늄-아연도금강판을 사용하는 것이 가장 바람직하였다.In the above description, the steel sheet used for the solid lubrication substrate may be any one selected from bronze plate, galvanized steel sheet, stainless steel sheet, 55% aluminum-zinc steel sheet to maintain the mechanical strength of PTFE resin and PFA resin. Among them, it was most preferable to use a 55% aluminum-zinc plated steel sheet.

상기 설명에 있어서, PTFE수지 PFA수지 및 천연흑연의 입도(입자의 크기)가 0.50㎛ 보다 크면, 수분산이 균일하게 이루어지지 않고 일부가 침전되어 바람직하지 못하고, PTFE수지 PFA수지 및 천연흑연의 입도가 0.15㎛ 미만이면, 냉동 유화중합이 잘 이루어 지지 않아 냉동시간이 길어져서 바람직하지 못하다.In the above description, when the particle size (particle size) of PTFE resin PFA resin and natural graphite is larger than 0.50 µm, water dispersion is not uniform and some precipitates, which is undesirable, and the particle size of PTFE resin PFA resin and natural graphite is not preferable. If less than 0.15㎛, freezing emulsion polymerization is not well made, the freezing time is long, which is not preferable.

상기 설명에 있어서, 상기 PTFE수지를 55.50중량% 초과하여 함유하면 상기 고체 윤활중합체가 철강판과의 부착력이 떨어져서 바람직하지 못하고, 상기 PTFE수지를 44.5중량% 미만 함유하면 상기 고체 윤활중합체가 철강판과의 부착력은 강하나 상기 고체 윤활중합층에 균열이 발생하여 바람직하지 못하고, 상기 PFA수지를 2.50중량% 초과하여 함유하면 상기 고체 윤활중합체가 철강판과의 부착력은 강하나 상기 고체 윤활제층에 균열이 발생하여 바람직하지 못하고, 상기 PFA수지를 1.50중량% 미만 함유하면 상기 고체 윤활중합체가 철강판과의 부착력이 떨어져서 바람직 하지 못하다. In the above description, when the content of the PTFE resin is more than 55.50% by weight, the solid lubricating polymer is not preferable due to the poor adhesion to the steel plate, and when the content of the PTFE resin is less than 44.5% by weight, the solid lubricating polymer is Although the adhesive force of is strong, cracking occurs in the solid lubricating polymer layer, which is not preferable. If the PFA resin is contained in an amount exceeding 2.50% by weight, the solid lubricating polymer has a strong adhesive force with the steel sheet but cracking occurs in the solid lubricant layer. If the PFA resin is less than 1.50% by weight, it is not preferable because the solid lubricating polymer has poor adhesion to the steel sheet.

또한, 상기 천연흑연분말을 2.80중량% 초과하여 함유하면 윤활성은 증가하나 다른 성분들의 함량이 부족하여 바람직하지 못하고, 상기 천연흑연분말을 2.00중량% 미만 함유하면 윤활성이 떨어져서 바람직하지 못하고, 상기 증류수를 50중량% 초과하여 함유하면 PTFE수지, PFA수지 및 천연흑연분말을 균일하게 분산시킬 수는 있으나, 상기 냉동 유화중합단계에서 냉동 유화중합법에 의해 저중합도의 유상물을 제조하는 시간이 많이 소요되어 바람직하지 못하고, 상기 증류수를 39.70중량% 미만 함유하면 PTFE수지, PFA수지 및 천연흑연분말을 균일하게 분산시킬 수 없어 바람직하지 못하다.In addition, when the content of the natural graphite powder is greater than 2.80% by weight, the lubricity is increased, but the content of other components is insufficient, which is not preferable. If the content of the natural graphite powder is less than 2.00% by weight, the lubricity is not preferable. If it contains more than 50% by weight, it is possible to uniformly disperse PTFE resin, PFA resin and natural graphite powder, but it takes a long time to prepare an oily substance of low polymerization degree by the freeze emulsion polymerization method in the freezing emulsion polymerization step. It is not preferable, and containing less than 39.70% by weight of distilled water is not preferable because it can not uniformly disperse PTFE resin, PFA resin and natural graphite powder.

상기 비이온성 분산제 0.80중량% 초과하여 함유하면 PTFE수지, PFA수지 및 천연흑연분말을 균일하게 분산시킬 수 있으나 기포가 많이 발생되어 바람직하지 못하며, 상기 비이온성 분산제 0.30중량% 미만 함유하면 기포는 발생하지 않으나 PTFE수지, PFA수지 및 천연흑연분말을 균일하게 분산시킬 수 없어 바람직하지 못하다.If it contains more than 0.80% by weight of the nonionic dispersant, PTFE resin, PFA resin and natural graphite powder may be uniformly dispersed, but many bubbles are not preferable, and if less than 0.30% by weight of the nonionic dispersant, no bubbles are generated. However, PTFE resin, PFA resin and natural graphite powder cannot be uniformly dispersed, which is not preferable.

상기 설명에 있어서, PTFA수지, PFA수지 및 천연흑연분말의 입도가 0.50㎛ 보다 크면 수분산이 완전하게 이루어지지 않기 때문에 PTFA수지, PFA수지 및 천연흑연분말의 일부 입자가 침전이 발생되어 바람직하지 못하고, PTFA수지, PFA수지 및 천연흑연의 입도가 0.15㎛ 미만일 경우에는 상기 냉동 유화중합단계에서 냉동 유화중합이 잘 이루어지지 않아 냉동 시간이 길어져서 바람직하지 못하다.In the above description, when the particle size of the PTFA resin, PFA resin and natural graphite powder is larger than 0.50 µm, since the dispersion of water is not completely performed, some particles of the PTFA resin, PFA resin and natural graphite powder are precipitated, which is not preferable. When the particle size of the PTFA resin, PFA resin and natural graphite is less than 0.15㎛, the freezing emulsion polymerization is not performed well in the freezing emulsion polymerization step, so the freezing time is not long.

또한 상기 압출용 PTFE수지·PFA수지 공중합체 제조단계에서 수분을 증발시 켜서 중합도가 증가된 고무상 반고체형의 점도가 높은 압출용 PTFE수지·PFA수지 공중합체를 철강판의 상부표면에 일정한 두께로 고착시키고, 상기 고체윤활기판 제조단계에서 300℃ 내지 380℃의 온도로 유지된 컨베이어 시스템에서 15 내지 25분 동안 가열 소성하여 경화시킬 때 철강판의 표면과 수지기판의 부착력이 매우 컸다.In addition, the extruded PTFE resin and PFA resin copolymer having a high viscosity of a rubbery semi-solid type having increased polymerization degree by evaporating water in the extrusion PTFE resin and PFA resin copolymer manufacturing step to a predetermined thickness on the upper surface of the steel sheet. The adhesion between the surface of the steel plate and the resin substrate was very large when the sheet was fixed and hardened by heating and baking for 15 to 25 minutes in a conveyor system maintained at a temperature of 300 ° C. to 380 ° C. in the solid lubrication substrate manufacturing step.

이러한 현상은 PTFE수지의 용융점은 327℃이고, PFA수지의 용융점은 300∼310℃이므로 PTFE수지보다 PFA수지가 먼저 용융되어 고체윤활기판을 변화시키지 않고 철강판의 표면과 강력하게 부착되기 때문이다.This phenomenon is because the melting point of the PTFE resin is 327 ° C, and the melting point of the PFA resin is 300-310 ° C, so that the PFA resin is melted before the PTFE resin and strongly adheres to the surface of the steel plate without changing the solid lubrication substrate.

따라서, 본 발명은 금속강판 표면에 사출용 PTFE수지·PFA수지 공중합체를 소성에 의해 강력하게 부착시킬 수 있고, 윤활성, 내마모성, 내열성 및 내화학성이 뛰어남과 동시에, 종래로부터 고체윤활제를 금속판 표면에 부착시키기 위하여 청동분말을 분말야금법에 의해 융착시켜서 금속판 표면에 청동소결층을 부착시킬 필요가 없고, 또한 금속망이나 금속타공판의 빈공간에 PTFE수지 중합체를 함침 밀착시킬 필요가 없고, 금속망이나 타공망을 사용하지 않으므로, 용이하게 대량 제조할 수 있을 뿐만 아니라, 제조 비용을 크게 절감시킬 수 있다.Therefore, according to the present invention, the PTFE resin and PFA resin copolymer for injection can be strongly adhered to the surface of the metal sheet by sintering, and excellent in lubricity, abrasion resistance, heat resistance and chemical resistance, and a solid lubricant is conventionally applied to the surface of the metal sheet. It is not necessary to fuse the bronze powder by powder metallurgy to attach the bronze sintered layer on the surface of the metal plate, and to impregnate the PTFE resin polymer impregnated with the empty space of the metal net or the metal perforated plate. Since no perforated network is used, not only mass production can be easily performed, but also manufacturing cost can be greatly reduced.

상기 설명에 있어서, 특정 실시예를 들어서 도시하고 설명하였으나, 본 발명은 이에 한정되는 것은 아니며, 예를 들면 본 발명의 개념을 이탈하지 않는 범위내에서 이 기술 분야의 통상의 지식을 가진 자에 의해 여러가지로 설계 변경할 수 있음은 물론이다.In the above description, the specific embodiments have been shown and described, but the present invention is not limited thereto, for example, by those skilled in the art without departing from the concept of the present invention. Of course, the design can be changed in many ways.

Claims (3)

입도가 0.15 내지 0.50㎛의 미세한 PTFE수지 44.5 내지 55.50중량%, 입도가 0.15 내지 0.50㎛의 미세한 PFA수지 1.5 내지 2.50중량%, 입도가 0.15 내지 0.50㎛의 미세한 천연흑연분말 2.0 내지 2.8중량%, 증류수 39.7 내지 50.0중량% 및 비이온성 분산제 0.3 내지 0.80중량%를 용기에 넣고 교반하여 PTFE수지·PFA수지 및 천연흑연분말을 균일하게 분산시켜서 혼합하여 PH가 9.0인 알칼리성 혼합액을 제조하는 PTFE수지·PFA수지·천연흑연 분말혼합액 제조단계와;44.5 to 55.50 wt% of fine PTFE resin having a particle size of 0.15 to 0.50 μm, 1.5 to 2.50 wt% of fine PFA resin having a particle size of 0.15 to 0.50 μm, 2.0 to 2.8 wt% of fine natural graphite powder having a particle size of 0.15 to 0.50 μm, and distilled water 39.7 to 50.0% by weight of a nonionic dispersant and 0.3 to 0.80% by weight of a PTFE resin, PFA resin to prepare an alkaline mixed solution having a pH of 9.0 by uniformly dispersing and mixing the PTFE resin, PFA resin and natural graphite powder Natural graphite powder mixture preparation step; 상기 PTFE수지·PFA수지·천연흑연 분말혼합액 제조단계에서 제조한 PTFE수지·PFA수지·천연흑연 분말 혼합액을 -5℃의 저온에서 24시간 냉동시키고 다시 해빙시키는 냉동 유화중합법에 의해 저중합도의 유상물을 제조하는 냉동 유화중합단계와;The PTFE resin, PFA resin, and natural graphite powder mixture prepared in the step of preparing the PTFE resin, PFA resin, and natural graphite powder mixture are refrigerated at 24 ° C. at -5 ° C. for 24 hours and then thawed again by a freeze emulsion polymerization method. Frozen emulsion polymerization step of producing water; 상기 냉동 유화중합단계에서 중합된 저중합도의 유상물을 80℃ 내지 100℃의 온도로 유지된 수조 내에서 150 내지 210분 동안 가열하면서 수분을 증발시켜서 중합도가 증가된 고무상 반고체형의 압출용 PTFE수지·PFA수지 공중합체를 제조하는 압출용 PTFE수지·PFA수지 공중합체 제조단계와;Rubber-based semi-solid extrusion PTFE having an increased polymerization degree by evaporating water while heating the low-polymerization oil polymerized in the freezing emulsion polymerization step for 150 to 210 minutes in a water tank maintained at a temperature of 80 ℃ to 100 ℃ A step for producing an extruded PTFE resin and a PFA resin copolymer for producing a resin and a PFA resin copolymer; 상기 압출용 PTFE수지·PFA수지 공중합체 제조단계에서 제조한 고무상 반고체형 압출용 PTFE수지·PFA수지 공중합체를 0.25 내지 0.35㎜ 두께의 철강판 위에 올려놓고 100℃ 내지 140℃로 가열된 압축롤러에 의해 550 내지 610㎏/㎠의 압력을 인가하여 상기 철강판의 상부 표면에 불소수지계 고체윤활제층을 압축중합시켜서 상기 철강판의 상부 표면에 불소수지계 고체윤활제층을 고착시키는 불소수지계 고체윤활제층 고착단계와;A compression roller heated to 100 ° C. to 140 ° C. by placing a rubbery semi-solid extrusion PTFE resin and PFA resin copolymer prepared in the step of manufacturing the extruded PTFE resin and PFA resin copolymer on a steel sheet having a thickness of 0.25 to 0.35 mm. By applying a pressure of 550 to 610 kg / cm 2 to compress and polymerize the fluororesin-based solid lubricant layer on the upper surface of the steel sheet to fix the fluororesin-based solid lubricant layer on the upper surface of the steel sheet. Steps; 상기 불소수지계 고체윤활제층 고착단계에서 0.25 내지 0.35㎜ 두께의 철강판 의 상부 표면에 0.15 내지 0.25㎜ 두께의 불소수지계 고체윤활제층을 고착시킨 고체윤활기판을 300℃ 내지 380℃의 온도로 유지된 컨베이어 시스템의 자동 전기로에서 15분 내지 25분 동안 가열소성하여 불소수지를 경화시켜 철강판에 불소수지가 부착된 고체윤활기판을 제조하는 고체윤활기판 제조단계를 포함하는 것을 특징으로 하는 PTFE수지·PFA수지 공중합 불소수지계 고체윤활기판의 제조방법.In the fixing step of the fluororesin-based solid lubricant layer, a conveyor on which a solid lubrication substrate on which a fluororesin-based solid lubricant layer of 0.15 to 0.25 mm thickness is fixed to an upper surface of a steel sheet of 0.25 to 0.35 mm thickness is maintained at a temperature of 300 ° C to 380 ° C. PTFE resin and PFA resin, comprising a solid lubrication substrate manufacturing step of curing the fluorine resin by heating and baking in an automatic electric furnace of the system to produce a solid lubrication substrate having fluorine resin attached to the steel sheet. Method for producing a copolymerized fluororesin solid lubrication substrate. 제1항에 있어서, 상기 철강판은 기계적 강도를 유지하기 위하여 청동판, 아연 도금강판, 스텐레스 강판, 55% 알루미늄-아연강판 중에서 선택된 어느 하나를 사용하는 것을 특징으로 하는 PTFE수지·PFA수지 공중합 불소수지계 고체윤활기판의 제조방법.The method of claim 1, wherein the steel sheet is PTFE resin, PFA resin copolymer fluorine characterized in that any one selected from bronze plate, galvanized steel sheet, stainless steel sheet, 55% aluminum-zinc steel sheet to maintain mechanical strength Method for producing a resin-based solid lubrication substrate. 청구항 제1항의 방법에 의해 제조한 것을 특징으로 하는 PTFE수지·PFA수지 공중합 불소수지계 고체윤활기판.A PTFE resin / PFA resin copolymerized fluororesin-based solid lubrication substrate produced by the method of claim 1.
KR1020090083003A 2009-09-03 2009-09-03 PET resin / PF resin copolymerized fluororesin solid lubrication board and its manufacturing method KR101051702B1 (en)

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