LCP E6810╣LCP E6810

詳細內(nèi)容：LCP E6810╣LCP E6810 POM 日本旭化成 LA501 TPEE韓國LG BT-1155D PVC德國P80EMA美國杜邦1124AC PBT基礎創(chuàng)新塑料(上海)457-1001 PA12 法國阿托菲納 AESN P302TL HIPS韓國錦湖HFH407N LCP日本寶理T150 BK005P LCP日本寶理A130 BK010 GPPS江蘇綠安擎峰LV-T6 TPEE美國泰科納MT9663 PC基礎創(chuàng)新塑料 D-EP BK1A644 PA12 瑞士EMS LV-2H POM 韓國可隆 LW301 PA12 法國阿科瑪 P40 PC日本帝人 G-3110G LCP日本住友化學E5008 PP廣州LG GP-2209FA PBT惠州南亞1403G6 GBK3 LDPE北歐化工FT4119 PBT江蘇長春4830 NCF PC/ABS 德國科思創(chuàng)（拜耳） T85 XF PA6荷蘭DSM K-FKGS6/A BK PC基礎創(chuàng)新塑料 DX10311 PA612美國杜邦77G33L PA11 法國阿科瑪 BZM65 BK PC/ABS 日本三菱工程 TMB4312 PA6日本東麗CM1014-V0 ABS韓國三星VH-0800 TPE荷蘭DSMEL150EMA美國杜邦12024SAC PA66上海羅地亞A60G1V30 PBT美國泰科納3300D PC基礎創(chuàng)新塑料 PDX-D-04522 MVLDPE(茂金屬)日本普瑞曼SP0540 LCP E6810╣LCP E6810 LCP E6810╣LCP E6810 (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. LCP E6810╣LCP E6810 PPS日本東麗A504 BK PC日本出光 R2200-920100 MVLDPE(茂金屬)美國埃克森美孚27-03CH ABS韓國LGAF-312F BK PC日本帝人 G-3130M BK PA66基礎創(chuàng)新塑料RFL-4536 BK PA66上海羅地亞A216 BK PA610 基礎創(chuàng)新塑料 QCL-4036 BK PA66德國巴斯夫A3U PA66日本杜邦HTN53G50HSLRHF BK618A PA12 瑞士EMS XS1332 PP沙特國家石化B45ML TPU深圳科思創(chuàng)（拜耳）UDS-75A10 PP韓國曉星J440W POM 美國泰科納 LW90-SC K(Q)膠荷蘭菲利浦KR-03 PBT深圳杜邦SK601 NC010 PVDF 美國蘇威 460-NC PP韓國韓華道達爾HY200 PC基礎創(chuàng)新塑料 DF-FR BK PC/ABS 美國陶氏 7560 IP7700053 PA612 美國杜邦 350PHS PC韓國三星 CF-1070 ABS奇美PA-747H PP沙特HP528N LDPE沙特巴塞爾LP 2427K MBS日本鐘淵M210 LDPE中石化上海N220 PVDF 美國蘇威 TA-6010/0000 EVA美國埃克森美孚UL 00728CC TPU德國亨斯邁90AHT PVDF 美國蘇威 20810-19 PA6德國朗盛BG-50S PBT美國杜邦CE7931 BK507 PC/ABS 廣州LG HR5007A-KA02 LCP E6810╣LCP E6810 LCP E6810╣LCP E6810 (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 LCP E6810╣LCP E6810 POM 美國泰科納 CFX-0261 POM 韓國工程塑料 MF3020 PA12 日本宇部 3030JI6L PC日本三菱工程 7022FD2 PA66美國杜邦MIN121 NC010 PA46基礎創(chuàng)新塑料STNAL-4022 HS PP中石化鎮(zhèn)海006 PPS韓國三星XP-4240 PBT荷蘭DSMTV4 241 SN BK PA66美國杜邦7304 NC010 POM 泰國三菱工程 FX-11 PA12 瑞士EMS L25 A NZ BK TPV 美國埃克森美孚 211-87 PC日本三菱工程 HL－3000U LCP日本油墨NC-301 LDPE中石化茂名951-025 PP美國埃克森美孚PP1055E2 PP韓國SK BY3500 PA66美國泰科納GF50-01 PA66美國杜邦FR72G25 PC韓國LG 1261-03 PC基礎創(chuàng)新塑料(西班牙) LS2-111 PA9T 日本可樂麗 GW2458 BK PP韓國曉星J842 POM 基礎創(chuàng)新塑料 KFX-1004 ABS臺化AG15A0 PA66日本杜邦FR52G30LX-NC010 PA6日本三菱工程1010GN2-15 PPO 基礎創(chuàng)新塑料 SE1GFN1 PC日本帝人 GN-3630LM POE泰國陶氏8999 PC德國科思創(chuàng)（拜耳） TP0370 HIPS韓國LG405AF PBT廣州LGGP-2156FT LCP美國泰科納S135-BK010P LCP E6810╣LCP E6810 LCP E6810╣LCP E6810 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. LCP E6810╣LCP E6810 PA6/66德國巴斯夫1C PEI 基礎創(chuàng)新塑料 ATX3562R PP沙特巴塞爾TKG-300N PBT基礎創(chuàng)新塑料WF-7007 PA12 德國贏創(chuàng)德固賽 L1833 PA66德國朗盛A31S PC基礎創(chuàng)新塑料 EXL1492C PA6德國朗盛B40SK POM 美國杜邦 577 TPE德國膠寶TF6AAG PC上海三菱瓦斯 HL-5000 PA66歐盟杜邦FR50 NC010 PC日本出光 AZ2201 PP韓國SK R390Y PPS四川得陽HMR61FC PC/ABS 韓國LG MP-5000AM PMMA 法國阿科瑪 V150 SEBS中石化巴陵YH-502TPBT/PET 基礎創(chuàng)新塑料(歐盟) 815-BK1066 PA6T 日本三井化學 C230 PP基礎創(chuàng)新塑料(上海)37T1020U-00900 AS(SAN)臺化NF2200AE ABS韓國三星TX0510T PA66基礎創(chuàng)新塑料RF0077E POM 美國杜邦 DE-20076 PBT南亞1403G3 GBK4PC/ABS 沙伯基礎 CY4000 COC日本大阪天然氣OKP4HT PP福聚6331F PC/ABS 上海科思創(chuàng)（拜耳） T90 XG PC泰國三菱工程 DS3220VUR PP韓國韓華道達爾FH44PW214 PP日本普瑞曼MF20G PA66意大利LATIH2G/50 PP中石化揚子PPB-M02-V LCP E6810╣LCP E6810 LCP E6810╣LCP E6810 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. LCP E6810╣LCP E6810 PA66歐盟杜邦101L NC010 PA66瑞士EMS AG-15 PC臺化 AC2856 PA66美國杜邦73G45 LDPE中石化茂名868-000 PBT長春1100 211LPC基礎創(chuàng)新塑料(南沙) 3412ECR ABS奇美PA-757A01 WH TPE荷蘭DSMEM630 POM 臺塑 M90 PPS日本東麗A756M PA6德國巴斯夫B3M8 POM 韓國工程塑料 FG2020 BK LCP日本住友化學E6006L PP韓國樂天化學J-550S LLDPE沙特222W POE美國埃克森美孚9361 TPV 美國埃克森美孚 211-45 PBT新光D202G20 BK POM 南通寶泰菱 M90-88 PPO 基礎創(chuàng)新塑料 WCD801A PC/ABS 廣州LG GN-5001TF PC/ABS 韓國三養(yǎng) 200NH PP茂名實華085(粉) PC日本三菱工程 LGV-2220KR PA66德國巴斯夫A3WG5-BK PA66美國杜邦105 BK010A PBT長春1100-211LC TPE美國杜邦60A ABS日本電氣化學CL-301Q PC臺化 AC3830-AN PC基礎創(chuàng)新塑料 HPS6 PA66美國杜邦ST801 BK PC日本帝人 GN-3730SI BK ABS日本東麗700-314 LCP E6810╣LCP E6810 LCP E6810╣LCP E6810 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 LCP E6810╣LCP E6810 PBT基礎創(chuàng)新塑料PDXW96084S WT90485 ABS臺化AG12A0 PA12 荷蘭DSM G-4/45 PC/ABS 日本三菱工程 PL2020 LCP美國杜邦3226 BK POM 法國塞拉尼斯 M90 CF2001 PP中石化海南Z30S PC/ABS 韓國三星 NH1015L PPO 基礎創(chuàng)新塑料 PX1700X-80403 PC基礎創(chuàng)新塑料 DF1007 POM 韓國可隆 EL304 TPU德國科思創(chuàng)（拜耳）365X GPPS惠州仁信RG-535N PA66德國巴斯夫A3HG7 PA6美國杜邦73G20HSIL BK LDPE韓國LGMB9500 POM 美國杜邦 500AL PVC河北金牛SE-800 PP沙特國家石化HP150G PA12 法國阿科瑪 G-350 PC日本三菱工程 EFR3000 PA610 基礎創(chuàng)新塑料 QF-1006 BK PA66美國杜邦HTNFR52G30NH BL563A PBT寶理3316 PP北歐化工RB707CF PBT日本東麗1184GA-15 PC基礎創(chuàng)新塑料(南沙) EXL1483C PA66基礎創(chuàng)新塑料RL-4030 BK PBT長春4115 BK PA12 日本宇部 3030JI5 PC/ABS 德國科思創(chuàng)（拜耳） 3005 HDPE中石油大慶6200 PBT廣州LGGP2156FM PA6德國巴斯夫B3ZG6 PEI 基礎創(chuàng)新塑料 EC002RPQ LCP E6810╣LCP E6810 LCP E6810╣LCP E6810 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