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東莞千泰塑膠原料有限公司主要經(jīng)營耐高溫PA66料,耐磨POM料,TPU包膠料,PA66加纖阻燃,耐高溫PBT料,PC耐高溫料. 可提供原料:ROHS(SGS)報告,UL認(rèn)證,FDA認(rèn)證,材質(zhì)證明及物質(zhì)安全資料表(MSDS)。具有相當(dāng)規(guī)模的現(xiàn)代化中外合資企業(yè),產(chǎn)品絕大部分外銷及為國內(nèi)外廠家提供高品質(zhì)產(chǎn)品,深受國內(nèi)外客戶好評歡迎來電咨詢:15818465693 0769-33214396 QQ:275158775
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產(chǎn)品/服務(wù): 瀏覽次數(shù):61╝LCP LD-235 → 
型 號: 齊全 
規(guī) 格: 25KG 
品 牌: 進(jìn)口 
單 價: 電議/面議 
起訂量: 25 KG 
供貨總量: 666666 KG
發(fā)貨期限: 自買家付款之日起 3 天內(nèi)發(fā)貨
更新日期: 2018-10-11  有效期至:長期有效
聯(lián) 系 人: 周偉 (先生)
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產(chǎn)品屬性
 產(chǎn)品型號:  齊全
 產(chǎn)品規(guī)格:  25KG
 產(chǎn)品品牌:  進(jìn)口
產(chǎn)品優(yōu)勢
╝LCP LD-235 →歡迎來電咨詢:158-1846-5693(周生)電話:0769-3321-4396 QQ:275-158-775千泰塑膠 質(zhì)量保證,原產(chǎn)原包,提供SGS,UL黃卡,COA,出廠認(rèn)證報告
詳細(xì)信息
╝LCP LD-235 → →,TPU D118K 、→,PPO PX1391 、‖。PC/ABS C1200HF-111 、→,LDPE 722F 、→,PP PEA648 、‖。PMMA 99560-MR2R EPDM 4045 ABS HAG-5230 、‖。TPEE BT-1035D PA6 B27E01 EPDM 1045 PP 4101O PC ML945 、→,PP 20MBTF PC G-3410R 、→,PC 301-6 、‖。PA66 66MK4015H HDPE HE3495-LS 、‖。PMMA FT6125 PA6 A1030BRL 、‖。PPS 1140E7 、‖。POM M270LV 、‖。PP P0050FN 2 PP BI850 EVA PA-420 TPU 58197 PA6 C246V30 、→,PP BH3520 、→,PA66 A205F PBT 3216 PP 622L 、→,EVA AD2528EH2 PA6 6GF15HV 、‖。PMMA D60 PC G-3430H TPE 4675 PP AW864 PC 301-15 、→,TPU 58130 、‖。PBT 4521 PBT/ABS B2504 98953 BK PBT K4560 、→,LLDPE ER3344 LDPE D1102(20/80) TPU S-185A PP 1453 、‖。LCP A435 、‖。PC G2510 PA66 GYY01CP 、→,POM Z3010 PP K1514 、→,TPU ETE60DS3 、‖。POM M90-88 PA9T G1300H-F02 BK PP H2200 ABS 770 TPU 302EZ 、→,PC/ABS GF20MD 、→,EPDM PX-052 、→,PP 1088 PA66 RFL-4036M 、‖。TPV 223-50 、→,PP MX88028 PMMA CM-207 PC LD7800 PC/ABS T85MN 、‖。PP 、‖。PA66 91G40 、‖。PBT D201000NA TPV 4339DV0 、‖。TPU TE95AP 、‖。PMMA V045-101 LLDPE DMDB-8916 、‖。PP H02S-00 、→,EVA EA19150 ASA WR-9310 、‖。 28-03 、‖。PP 3C37F 、‖。PA66 1200 、‖。ABS AN-450 、‖。PP 42MH647 、‖。PP HJ646 、‖。PPO GFN1-520V 、→,PP 1111R ABS MG94U 、→,POM TC704 PA6 B700 G25H BK 、‖。ASA XC811 PC/ABS 210NHFL 、→,PA6 XP32-C1 PP 5140H PP PH-460 PP SG930MO 、→,PPS 0220A9 LDPE LD358 、→,PC/ABS NH-1015T 、‖。PPE AN60 ABS 3504 TPU BTP-98A POM FL2020 PC DEF42 ABS SP-0183 POM KE004 LCP A150 、→,PP TKC353N PA6 BG-15/2 、→,PSU R-7700 PA66 A30B041 PC 940-116L PP N4450 、‖。POM MF3025E 、‖。PBT 7300E PC SC5004T 、‖。PBT 4730 BK 、‖。PP R381M EPDM 774P 、‖。TPE TC4MGZ TPU C85A10 、→,EVA MU763000 POM UV140LG TPE 340S-UV PC HPR3500 、‖。PP 304E1 、‖。PA6 B 40E 、‖。PP BE60-7032 TPE G7960-1001-00 、‖。PA66 101 、→,PP EG6D 、‖。PC FL900S 、→,LDPE LD201.48 、‖。PC/ABS HI-1001BG TPE 901 ABS730 TPEE 1130LH 、 HIPS Impact resistant polystyrene (HIPS) is an impact resistant polystyrene product produced by adding polybutadiene rubber particles in polystyrene. introduce 475 is the HIPS machining The impact resistance of PS can be processed by many traditional molding methods, such as injection molding, structural foam molding, sheet and film extrusion, hot forming and blow molding. HIPS resin absorbs water slowly, so there is no need for drying in general. Sometimes excessive moisture on the surface of the material will be absorbed, which affects the appearance quality of the final product. Under the temperature of 160 F dry 23h can remove excess moisture. The extrusion of thin films, sheets and profiles is the most useful processing method for HIPS. Anti impact polystyrene has a wide range of processing, so it becomes one of the most easily thermoforming resins. Generally, the melting temperature of the resin is 400 - 500 F, and the melt index range of the resin is 1.5 - 4 g/10min. Rotating, series and shuttle type pressure and vacuum thermoforming equipment are often used. HIPS has excellent thermal stability and shear stability. It can be used for a lot of recycled materials without reducing the performance of products, and the amount of recycled material in hot forming can be as high as 60%. Injection molding is the most used processing method next to the extrusion. The injection molding of the resin is usually carried out on a reciprocating screw injection molding machine with a length to diameter ratio of 16:1 to 24:1 and a compression ratio of 2.5/1 - 3.0/1. The processing temperature is 350 - 500 degree F, but for the flame retardant HIPS, the processing temperature must be less than 470 F to prevent the additive from producing degradation reaction. The melt index of the resin processed by injection molding is generally 5 to 15 g/min. The forming method of structural foam plastics is a common process, using chemical and physical foaming agents. Although a variety of HIPS resin are compatible with each other, but before the operation to clean processing equipment, to ensure good product quality, the impact of acrylonitrile with a PS Th ene styrene copolymer (ABS), polyvinyl chloride (PVC), polypropylene (PP), polyethylene (PE), acrylic resin and most other plastics are not compatible, incompatible plastic mixture separation will produce delamination phenomenon in processing equipment, caused great decline of physical properties. application Impact resistance PS is easily machinability, good performance and low price, so it is used to manufacture products and industrial products of many uses. The main applications are packaging and disposable supplies, instruments, household appliances, toys and entertainment supplies, and construction industries. The largest use of HIPS is to be used as a packaging and disposable material, especially for food packaging and eating tableware. The main applications include the daily packaging container. A cup, a variety of covers, plates, bowls, etc. are used and distributed for the vending machine. Disposable products such as disc, bottle cap, safety razor, pen and so on are also a part of the use of HIPS. PVC carcinogen, which will undoubtedly affect the development of PVC to some extent. However, the residual VCM has been successfully reduced by vehicle and other ways, so that the content of VCM in PVC resin will be less than 10ppm, which will meet the requirement of hygienic grade resin and expand the application scope of PVC. Even the content of VCM in the resin is less than 5ppm, and the residual VCM is very few after processing. It is basically harmless to the human body and can be used as food and medicine packaging and children's toys. Main classification According to the different application range, PVC can be divided into general PVC resin, high degree of polymerization PVC resin and crosslinked PVC resin. The general PVC resin by polymerization of vinyl chloride monomer is formed under the action of initiator; high degree of polymerization of PVC resin is resin in the polymerization of vinyl chloride monomer added to the system, the chain growth polymerization crosslinking agent; PVC resin is added to the resin crosslinking agent containing dienes and polyenes in vinyl chloride monomer polymerization polymerization system. According to the method to distinguish the vinyl chloride monomer, can be divided into electric stone, and imported ethylene (EDC, VCM) monomer method (on the habits of the ethylene monomer and import system called ethylene method). According to polymerization method, PVC can be divided into four main categories: suspension polyvinyl chloride, emulsion polymerization, polyvinyl chloride, bulk polymerization, polyvinyl chloride and solution polyvinyl chloride. Suspension polyvinyl chloride (PVC) is one of the most productive varieties, accounting for about 80% of the total output of PVC. Polyvinyl chloride suspension method is divided into six models according to absolute viscosity: XS-1, XS-2... XS-6; XJ-1, XJ-2... XJ-6. The meaning of each letter in the model: X- suspension; S- loose type; J- compact. method polyvinyl chloride PVC can be made by substitution reaction of ethylene, chlorine and catalyst. Because of its fire prevention heat effect of PVC is widely used in all walks of life every kind of products: wire skin, skin fiber, shoes, handbags, bags, accessories, signs and billboards, building decoration supplies, furniture, ornaments, rollers, pipes, toys (such as the famous Italy "Rody" jumping horse), curtain, door, auxiliary medical supplies, gloves, some food preservation paper, some fashion etc.. Polymerization method PVC was prepared by free radical addition polymerization. The polymerization methods were mainly divided into suspension polymerization, emulsion polymerization and bulk polymerization, mainly by suspension polymerization, which accounted for about 80% of the total output of PVC. The pure water, liquefied VCM monomer and dispersant were added to the reactor, then initiator and other auxiliaries were added. After heating to a certain temperature, the VCM monomer was polymerized by free radical to form PVC particles. Continuous stirring makes the particle size uniform and makes the generated particles suspended in the water. In addition, the PVC paste resin was produced by micro suspension, and the properties and paste properties of the products were all good. The monomer droplets are dispersed in the aqueous phase suspension polymerization method, using oil soluble initiator were dissolved in monomer, polymerization reaction in the droplet, the polymerization heat absorbed by the water in time, in order to ensure that these droplets in water were bead dispersed, need to join the suspension the stabilizer, such as gelatin and polyvinyl alcohol, methyl cellulose, hydroxyethyl cellulose, etc.. Most of the initiators are organic peroxide and azo compounds, such as peroxide two, two isopropyl carbonate, peroxide two, bicarbonate, peroxide two, two ethylhexyl ester, azo two isoheptane, azo two isobutadiene and so on. The polymerization is carried out in a polymerizer with a agitator. After polymerization, the monomer material flows into the recovery tank?or?stripper recycle monomer. Then into the mixing kettle, water washing then centrifuge dehydration, drying and resin finished products. The vinyl chloride monomer should be removed from the resin as much as possible. As the PVC for food packaging, the content of free monomer should be controlled below 1ppm. During polymerization, the temperature and pressure of the polymerization process must be controlled to ensure that the specified molecular weight and molecular weight distribution range are obtained and the detonation is prevented. The particle size and particle size distribution of the resin is controlled by the stirring speed and the selection and dosage of the suspension stabilizer. The quality of resin is characterized by particle size and particle size distribution, molecular weight and molecular weight distribution, apparent density, porosity, fisheye, thermostability, color, impurity content and free mobility of powder. Polymerization reaction
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