詳細內(nèi)容：PA6 ST811HSじPA6 ST811HS PP韓國SK R140H POM 韓國可隆 TC3010 PC日本帝人 GN-3620H PC基礎創(chuàng)新塑料 DFL-4032 PA46日本DSM TS250F6D BK PMMA 日本三菱麗陽 IRH-70 PC臺化 AC3830-AA TPV 美國�？松�美孚 121-87 PPO 基礎創(chuàng)新塑料(歐盟) SE1GFN1 PA66美國泰科納GF50-01 TPEE韓國可隆KP3372 PA12 德國贏創(chuàng)德固賽 L1724 PVDF 美國蘇威 720(2) PA/ABS上海羅地亞KC226 PA12 法國阿科瑪 50R53 PBT新光5886 PA6荷蘭DSM S223G6-NC PA66荷蘭DSM GS-60 PPS美國泰科納1141L4 PMMA 德國贏創(chuàng)德固賽 7H TPV 荷蘭DSM X5755 PP韓國LG R1510 PPS日本東麗A610MG1 PBT漳州長春3010-104 PVC德國P70HT PA12 法國阿科瑪 G170 ABS/PMMA 韓國三星 SF-0505EA POM 德國泰科納 C9021GV1/20 TPEE盧森堡杜邦70D PPS日本東麗A305M D1 PEI 基礎創(chuàng)新塑料 CRS5201 PBT深圳東麗2164GS30 POM 日本杜邦 DE8504 TPEE美國泰科納MT9677 POM 韓國工程塑料 TX-11H PA6 ST811HSじPA6 ST811HS PA6 ST811HSじPA6 ST811HS (1) injection: the general injection molding machine can be used, and the melting index of glass fiber reinforced PPS is 50. The technological conditions of injection are: barrel temperature, pure PPS at 280~330 C, 40%GFPPS at 300-350 C, nozzle temperature, pure PPS at 305 C, 40%GFPPS at 330 C, mold temperature at 120-180 C, injection pressure, 50-130MPA. PA6 ST811HSじPA6 ST811HS PBT韓國杜邦SK605 BK851 PVC德國VK710 PA6日本東麗1011G-45 IXEF 比利時蘇威 1022/0006PC基礎創(chuàng)新塑料(南沙) 920 PPO 基礎創(chuàng)新塑料(日本) PX9406P PA610 基礎創(chuàng)新塑料 QL4540 PA612德國贏創(chuàng)德固賽SX8002 PPE 日本三菱工程 PX100L（粉） PVC韓國韓華CP-430 PBT美國杜邦SK665FR BK507 PA66基礎創(chuàng)新塑料NYKON R BK EVA美國�？松�美孚UL 00728CC PP韓國韓華道達爾BI972 PA66加拿大英威達T3000HS1L TPV 土耳其英菲力 VU424-40A PC臺化出光 A1600 PBT基礎創(chuàng)新塑料(日本)420SE0-1001 TPU美國路博潤S-195A PA6中石化巴陵BL3350 POE新加坡三井化學A4050S PMMA 日本住友化學 HT25X LLDPE中石化武漢EGF-35B-1 PC德國科思創(chuàng)（拜耳） 2097 PP日本住友化學AW564 HIPS基礎創(chuàng)新塑料CL4310 PA46荷蘭DSM HF4550 BK ABS韓國LGAF-345 HDPE伊朗國家石化HF5110PC/ABS 德國科思創(chuàng)（拜耳） FR2010 MDPE卡塔爾石化K307 POM 德國巴斯夫 Z2320-003 PC/ABS 韓國LG 100F ABS日本電氣化學GR-2000 PP韓國韓華道達爾BJ850 PA6 ST811HSじPA6 ST811HS PA6 ST811HSじPA6 ST811HS (2) extrusion: exhaust exhaust extruder. The process is as follows: the temperature of the feeding section is less than 200 degrees, the temperature of the barrel is 300-340 degrees, the connection temperature is 320-340 degrees, and the die temperature is 300-320 degrees. (3) molding: suitable for large products, using two compression, first cooling, and then hot press. The preheating temperature of hot press is pure PPS at about 360 C 15min, GFPPS is about 380 centigrade 20min, and the pressure of mould pressure is 10~30Mpa, which is cooled to 150 DEG C. (4) spray forming: suspension spraying and suspension spraying and dry powder thermal spraying were used to spray the PPS onto the metal surface, and then the coating was obtained by plasticizing and quenching. The coating temperature of PPS was above 300 C and kept 30min. Drying process PA6 ST811HSじPA6 ST811HS PA46荷蘭DSM TW200F8 MS韓國LGXT560 PC泰國三菱工程 HL-7005 PC/ABS 基礎創(chuàng)新塑料 CX1440 PA66日本東麗CM3511G-60 EVA美國杜邦420 PA66基礎創(chuàng)新塑料RFL-36XXY BK LLDPE韓國樂天化學UR644 PMMA 法國阿科瑪 V 825-HID EVA美國杜邦150PC基礎創(chuàng)新塑料(南沙) 945 PP韓國曉星J700X PA6基礎創(chuàng)新塑料PB1006 LM BN 70745 PP日本三菱工程FX4G POM 基礎創(chuàng)新塑料 KCL36 SEBS李長榮7551 TPU德國科思創(chuàng)（拜耳）5377（粉） PBT日本寶理3316 ED3002 PBT基礎創(chuàng)新塑料(南沙)357TF BK1066L PA12 基礎創(chuàng)新塑料 PDX-I-99038 NAT PA6日本東麗CM1011G-30 BK PA66美國杜邦FGFE5171 TPV 美國埃克森美孚 121-68W228 PVC德國E10-65C PBT新光DF4806 PA6T 日本三井化學 C430NK BK PP韓國SK BH3820 PC/ABS 韓國三星 HP-1000P PA66美國杜邦158L PC/PET 基礎創(chuàng)新塑料 X8303 PA66日本旭化成1502S MVLDPE(茂金屬)美國陶氏）2045G PA6意大利波利.布蘭德B AV NA FD LCP美國達特FSR315 PA6T 日本三井化學 EW630N PA6 ST811HSじPA6 ST811HS PA6 ST811HSじPA6 ST811HS Temperature: 100~105 C Time: 3hr 2. Injection molding process 1) mold temperature: 60-80 C 2) barrel temperature: the front section: 220~260 C middle section: 290~310 C after section: 300~320 C Nozzles: 290~300 C 3) injection pressure: 60~70Mpa4) injection speed: medium speed 5) injection time: according to the size of the parts, the mold is filled with the parts, and the basic surface cooling and setting is the best. PA6 ST811HSじPA6 ST811HS PVDF 法國阿科瑪 460 TPU德國科思創(chuàng)（拜耳）192 POE新加坡三井化學DF740 PBT江蘇長春1200 PP臺化K8009 PC德國科思創(chuàng)（拜耳） 2405 702395 LLDPE中石化福煉DFDA-7042 PBT惠州南亞1210G6 ABK1 LLDPE中石化鎮(zhèn)海DFDA-7042 MVLDPE(茂金屬)美國�？松�美孚27-03CH PP韓國大林EP332K PA66惠州南亞6512 PA66意大利LATI66 H2 G/30 PP美國�？松�美孚7033E3 PC基礎創(chuàng)新塑料(南沙) EXRL0847 TPE美國吉力士90A EVA比利時�？松�美孚UL 05540EH2 TPU德國亨斯邁65AB HIPS歐盟TOTAL4440 PBT南亞1403G3 GBK4 PP日本P2854 POM 日本旭化成 SG452 PC日本三菱工程 S-1000R ABS廣州LGAF-312C PA6中石化巴陵BL3240 TPU美國路博潤2363-65D PPS美國泰科納4332L6 PA6德國AKROB3GF50 PA46荷蘭DSM TE373 PC日本住友化學 301-4 TPU美國路博潤5703 POM 韓國工程塑料 F30-03 PC日本三菱工程 ECF2008 KR TPU拜耳優(yōu)得3095AU PC/ABS 寧波臺化 AC2300 PA6 ST811HSじPA6 ST811HS PA6 ST811HSじPA6 ST811HS ABS The wall thickness of 1. products: the wall thickness of the products is related to the flow length of the melt, the production efficiency and the requirements of the use. The ratio of the maximum flow length and wall thickness of ABS melt is 190:1, this value will vary with the grade, so that the wall thickness of ABS products should not be too thin, the products need for electroplating, wall thickness is slightly thicker, to increase the adhesion of surface coatings and products. The wall thickness of this product is selected between 1.5 and 4.5mm. Considering the wall thickness of products, should also pay attention to the uniformity of the wall thickness, are not too big, the products need for electroplating on the surface should be smooth without bump, because these parts due to electrostatic interaction is difficult to remove dust adhesion, resulting in poor fastness of coating. In addition, it is necessary to avoid the existence of the sharp angle, so as to prevent the stress concentration, so it is appropriate to use the arc for the corner of the corner and the parts of the thick and thin connection. _ 2. draft: draft articles and shrinkage is directly related to the grade of different products, different shapes and different molding conditions and molding shrinkage have some differences, generally 0.3 ~ 0.6%, sometimes up to 0.4 ~ 0.8%, the product size precision molding. The demoulding slope of ABS products is considered as: the mold core part is 31 degrees along the die direction, and the cavity part is 4 (/ 1 20') along the die direction. For products with more complex shapes or letters and patterns, the deviated slope should be properly increased. The top 3. requirements: products due to apparent smoothness of the electroplating performance have a greater impact, any tiny scar on the table view there will appear obviously in electroplating, so in addition to the requirements of any scars are not allowed on the cavity, but also the effective area to the top, the the root rod at the top out of sync is better in the process of ejecting force should be uniform. PA6 ST811HSじPA6 ST811HS PC荷蘭DSM G4F 23R TPV 美國�？松�美孚 103-50 PC日本出光 GTN-2510 PA6漳州長春10G6-104 HIPS鎮(zhèn)江奇美PH-66 PVC日本信越TK-700(粉) TPU德國科思創(chuàng)（拜耳）345 GPPS新加坡電氣化學MD-100-301 GPPS（張家港雪佛龍）MC3500 TPV 荷蘭DSM 3140N PVC德國S4080 PBT美國杜邦SK652FR NC010 PA46荷蘭DSM HF4130 PBT日本寶理601MW ED3002 PBT德國朗盛T7331 PBT美國杜邦T805 BK851 PC日本三菱工程 EHR3500 GY EAA美國杜邦3460(1) PA12 日本宇部 3024U PA66深圳杜邦80G25HS BK117 PA12 阿科瑪 55R53 PA66美國杜邦FE15001 PBT日本寶理3116 PC基礎創(chuàng)新塑料(西班牙) 221R-111 PBT基礎創(chuàng)新塑料(南沙)420-1001 PP韓國大林EP1904 PC/ABS 韓國錦湖 EPG 111 TPEE日本東麗7247 PA612基礎創(chuàng)新塑料IFL-4034 BK TPU拜耳優(yōu)得95A PBT日本東麗2164GS30 PC日本三菱工程 GS2040 PC基礎創(chuàng)新塑料(南沙) ML7694-739 PA46荷蘭DSM TW248F6 BK COC日本G7810 PA6 ST811HSじPA6 ST811HS PA6 ST811HSじPA6 ST811HS 4. exhaust: in order to prevent the occurrence of problems such as bad exhaust, molten material burn and obvious seam line in the process of mold filling, we need to set up exhaust holes or exhaust tanks which are not more than 0.04mm, so as to discharge gas generated by melting material. 5. runner and gate: in order for ABS melt to fill all parts of the die cavity as quickly as possible, the diameter of the runner is not less than 5mm, and the thickness of the gate is over 30% of the product thickness. The length of the straight part (about the part that will enter the cavity) is about 1mm. The position of the gate should be determined according to the requirements of the products and the direction of the flow of the material. For the products that need to be treated with electroplating, it is not allowed to exist on the adhesion surface of the coating. Raw material preparation PA6 ST811HSじPA6 ST811HS POM 日本寶理 M270-38 PA46日本帝人N2030RB BK PP李長榮STM866 PA11 法國阿科瑪 BESVO A FDA LCP日本東麗L204M50 SG934 PC日本帝人 MH-3600HS PBT基礎創(chuàng)新塑料(南沙)DR51-1001 PEI 基礎創(chuàng)新塑料 9075 PA66惠州南亞6401G6 FNC1 EPDM 美國陶氏 3722P PA46荷蘭DSM TS350 PVC臺塑PR-450 PA6日本東麗CM1026 POM 美國泰科納 C13031 PA12 瑞士EMS L25W20X WH PPO 基礎創(chuàng)新塑料 N1250 TPEE荷蘭DSM EL630 PA66歐盟杜邦E42A NC010 PA6荷蘭DSM K222-D HIPS韓三星第一毛織NH-1904 BK PBT南亞140PG6 PPE 日本三菱工程 HGX410N BK TPU德國巴斯夫SP832-50 PA12 德國贏創(chuàng)德固賽 E40-S1PC/ABS 上�？扑紕�(chuàng)（拜耳） T65XF PA46荷蘭DSM TW421 RD POE泰國陶氏8200 PP泰國石化230 PA6美國EMS BZ2/3 BK LCP美國泰科納V143XL-BLACK PFA 美國蘇威 M640PC日本三菱工程 EGN-2020KR LLDPE中石油蘭州DFDA-7042N PBT日本東麗1184G-20 PA610 基礎創(chuàng)新塑料 QF-1006 BK PA6 ST811HSじPA6 ST811HS PA6 ST811HSじPA6 ST811HS LLDPE The most common method of production of PE is through slurry or gas processing, and a few are processed by solution. All these processes are exothermic reactions involving ethylene monomer, a- olefin monomer, catalyst system (probably more than one compound) and various kinds of hydrocarbon diluents. Hydrogen and some of the catalysts are used to control the molecular weight. The slurry reactor is usually a stirred tank or a more commonly used large ring reactor in which the slurry can be stirred. Polyethylene particles are formed when ethylene and copolymerized monomers are in contact with the catalyst. After removing the diluent, the polyethylene particles or particles are dried and added to the dosage according to the dosage to produce the granular material. The modern production line of a large reactor with a twin screw extruder can produce more than PE40000 pounds per hour. The development of the new catalyst contributes to the improvement of the performance of the new grade HDPE. The two most commonly used catalysts are Philip's chromium oxide based catalyst and an alkyl aluminum catalyst for titanium compounds. The HDPE produced by the Philip type catalyst has a medium - width molecular weight distribution, and the molecular weight distribution of the titanium - alkyl aluminum catalyst is narrow. The catalyst used in the production of narrow MDW polymers with a compound reactor can also be used to produce a wide MDW grade. For example, two series reactors that produce significantly different molecular weight products can produce Shuangfeng molecular weight polymer, which has a molecular weight distribution in the full width domain. molecular weight