詳細(xì)內(nèi)容：PC 1-9357/2╈PC 1-9357/2 PP李長榮8191 PBT惠州南亞140PG6 PA12 瑞士EMS L25W40X PC上海三菱瓦斯 GSH2010LR TPV 美國埃克森美孚 8271-55PC基礎(chǔ)創(chuàng)新塑料(南沙) 1000 PPO 基礎(chǔ)創(chuàng)新塑料 PPX640 PBT德國巴斯夫B 4300 G2POM 美國杜邦 500P PP福聚6524 PA6美國杜邦73G30T NC010 TPU德國科思創(chuàng)（拜耳）9392AU POM 日本寶理 KT-5M PP福聚6331 PBT新光B0620FC BK LCP日本寶理T130 PC日本高達(dá) R-10 PC基礎(chǔ)創(chuàng)新塑料 HF1130-112 PC臺化 AC2820-AH PC嘉興帝人 L-1225L BK PBT日本寶理727BM PBT日本寶理CRN7000N TPU美國RON R385U ABS奇美PA-709 電木粉 長春 T378J LCP美國杜邦77340 PPO 基礎(chǔ)創(chuàng)新塑料 GTX6009 PP基礎(chǔ)創(chuàng)新塑料MS-1002 BL5-002-5 PA66韓國杜邦70G13L NC010 PC日本帝人 LV-2225Y PCT 美國伊士曼 CG933 PC日本帝人 G-3120H PC日本出光 URC2501 W1248T PP福聚SJ3032 PA66美國杜邦70G35HSL BK267 PC 1-9357/2╈PC 1-9357/2 PC 1-9357/2╈PC 1-9357/2 LDPE The film can be used in packaging materials and capacitor films. For the food packaging industry, the gas permeability of the biaxially stretched PP film is lower. To reduce permeability, the first is to reduce the permeability of PP material, which can be achieved by filling and modifying, but the effect is not very obvious. The two is to reduce permeability through blocking the contact between PP film and gas. It is also easy to achieve the following 2 methods. BOPP can be used to separate gas by spraying, such as spraying two vinyl chloride or vinylidene ethyl alcohol to the surface of the membrane, with a thickness of about 0.0075 millimeters. Another method is vacuum aluminizing, with a thickness of about 0.0002 millimeters to block oxygen and so on. 3.PP needling omentumPC 1-9357/2╈PC 1-9357/2 PC德國科思創(chuàng)（拜耳） 6555 POE泰國陶氏7447 PPS日本油墨GB8411 PA66基礎(chǔ)創(chuàng)新塑料RYY3H4110 POM 德國赫斯特 C52021 PPE 日本旭化成 X1763 BK COC日本瑞翁340RPE蠟 泰國SCG化工 LP0020P POM 韓國工程塑料 FG2030 PA66深圳杜邦80G33HS1L-BK104 PP沙特5703P PA66深圳杜邦70G43L NC PP日本普瑞曼F-300SP PBT日本寶理330HR-ED3002TPO美國巴塞爾X1956A TPV 土耳其英菲力 VU424-40D PA12 瑞士EMS LCZ-15H PA66瑞士EMS AS/10 V0 BK PC日本三菱工程 LS-2020 PVDF 法國蘇威 1008-001 LCP寶理E463i BK210P TPU德國巴斯夫ESP 9339 PC日本帝人 LS-2250 POE泰國陶氏8180 PEEK 德國贏創(chuàng)德固賽 1000G PP日本EM622A PA66美國杜邦103HSL PBT韓國三養(yǎng)1551GN30 TPU德國科思創(chuàng)（拜耳）ES74D ABS日本UMGMG-2510A PP甘肅蘭港石化BL PA66日本杜邦420HSL NC010 電木粉 長春 T220NA PC/PET 基礎(chǔ)創(chuàng)新塑料 X7110 POM 日本大�；瘜W(xué) AT342 The membrane is an upgrading product of the tear film, and it can be used in sewing thread, carpet weaving, marine fishing and other industries. The process flow is as follows: Feeding, extrusion, film cooling, cutting and dividing wire, three roll traction, heating, stretching, needle forming fiber, heat treatment, cooling setting and winding. The temperature of the fuselage: 220, 230, 260, 255 C, the head temperature 250 C, the die head 250 centigrade, the PP melt index 1.5-4 g /10. The film cooling, water temperature 38 C, hot stretching temperature 150-165 degrees C, tensile multiple 5-6 times, cooling roll speed is lower than heat treatment roll speed 2-5%, stretching speed of 240 meters / points. 4.PP isolation membranePC 1-9357/2╈PC 1-9357/2 EVA美國杜邦670 EVA比利時(shí)�？松�美孚UL 05540EH2 HDPE中石化揚(yáng)子4803T PPO 日本三菱工程 AH40-9001 PA11 法國阿科瑪 BMN-10440 PA66法國羅地亞A218V33 BK TPU德國巴斯夫E1254D13U ABS鎮(zhèn)江奇美D-1000 ABS日本UMGVD100 ABS深圳東麗700 BK PP荷蘭利安德巴塞爾HP162 PA6日本東麗CM1011G-45 BK PA66集盛AFG30-FN00N1 ABS鎮(zhèn)江奇美D-120 PA46基礎(chǔ)創(chuàng)新塑料PDX-STN-98026 PP茂名實(shí)華040（粉） ABS基礎(chǔ)創(chuàng)新塑料Z48-1000 HIPS韓國錦湖HI-450W PVDF 法國蘇威 6008/0001 TPU深圳科思創(chuàng)（拜耳）U-98AU10 ABS臺達(dá)3100R PP日本卡爾普FR-240 PA6日本三菱工程1010G15 LCP美國伊士曼LG441 PMMA 日本旭化成 80NH ABS奇美PA-761 PC日本三菱工程 GSN-2050DF PP巴西H214 PBT漳州長春3030-104E PC日本三菱工程 GSV-2030R2 PC上海三菱瓦斯 S-3001R PPO 基礎(chǔ)創(chuàng)新塑料 PCN2910 PA66南亞6410G3 ABK2 LDPE伊朗國家石化LT750 EVA中石化燕山14J4 The PP isolation membrane can be used as an isolating layer between the conductor and the rubber insulation in the wire and cable. It can prevent adhesion between metal conductor and rubber sleeve. The process flow is as follows: Ingredients, kneading, extrusion, blowing and cooling, traction, cutting, winding, cutting and inspection. The melting index of the PP material is below 3.5 g /10. The extruder temperature is 180, 190-200, 200-210 C, and the temperature of the die head PC 1-9357/2╈PC 1-9357/2 TPEE美國杜邦82D TPEE美國杜邦4069 ABS日本東麗920 PP茂名實(shí)華450（粉） PBT惠州南亞1100 HNC1 ABS/PMMA 奇美 PA-718 HDPE韓國SKJM710 PA66基礎(chǔ)創(chuàng)新塑料RN001 BK1B599 PA66南亞640PG5 ANC1 POM 日本寶理 HW-02 K(Q)膠德國巴斯夫656C PC/ABS 日本帝人 TN-3713B POM 美國杜邦 311DP TPEE長春30C1NC010 TPEE長春1172LL AS(SAN)中石油蘭州BHF TPV 美國�？松�美孚 111-87 AS(SAN)日本旭化成783 ABS美國泰科納GF40-05 TPU拜耳優(yōu)得UT-74DU10 PP馬來大騰石化SM-240 PA612瑞士EMS CF6 S NATUR TPU德國巴斯夫E 1164 D 53U000 SIS臺橡DP-4411N PP韓國韓華道達(dá)爾BJ500 POM 日本寶理 FX-11J TPE美國吉力士OM 1255NX PA6韓國巴斯夫B3U PC泰國三菱工程 S-3000R PA6南亞2210G4 FNC1 HDPE泰國PTT化學(xué)HD1100JPC/ABS 上海科思創(chuàng)（拜耳） FR3008 PVDF 日本吳羽 W#8100(粉) PBT漳州長春1100-600S LCP日本杜邦5130L BK010 EEA In storage, we should keep away from the fire source, heat insulation, keep dry and clean in the warehouse, strictly prohibit any impurities mixed, strictly prohibit the sun and rain. Transportation should be stored in a clean, dry and roofed carriage or cabin, and no sharp objects such as iron nails are allowed. It is strictly prohibited to mix organic solvents such as flammable aromatic hydrocarbons and halogenated hydrocarbons. For example, the four liters of mineral water in a farmer's spring is a big bucket, which is the material. Recycling PC 1-9357/2╈PC 1-9357/2 POM 日本旭化成 2013A PBT漳州長春3030-104G PA66法國羅地亞A218V35 PA6德國巴斯夫DB2010C BKPC/ABS 沙伯基礎(chǔ) C6800 PA6T 德國巴斯夫 TKR4355G7 ABS韓國三星SD-0150 BK COC日本寶理8007 PP韓國SK B398G POM 美國杜邦 DE-9156 PA66惠州南亞640PG3 PA46荷蘭DSM TE341 PC上海三菱瓦斯 S-2000VR PC/ABS 韓國LG HR-5007A PA66美國杜邦HTNFR52G30NH GY101 PVC天津渤天化工MP1000F PA9T 日本可樂麗 GN2332 PC日本三菱工程 MB1801-BK TPEE美國杜邦30D PA66上海古比雪夫氮G20NC201 PC/ABS 日本三菱工程 3710-PA66美國杜邦FR50 ABS韓國三星HG-0760GPPC/ABS 沙伯基礎(chǔ) C2950 POM 美國泰科納 S9064 PP福聚6424 FEP 日本大金 NP101 POM 韓國可隆 LW301 PP新加坡聚烯烴FY4012 PC上�？扑紕�(chuàng)（拜耳） 9425 BK LCP美國泰科納A150D-2 PP沙特埃克森美孚7032E3 PMMA 日本住友化學(xué) MM PPS日本寶理1140A6 FT6134 POM 美國赫斯特 S 9244 (2) the typical representative of the ring tube reactor process ring tube reactor process is the Phillips process of Phillips company and the Innovene S process of INEOS company. Phillips process using isobutane as diluent, the chromium catalyst, the catalyst must be activated before use, isobutane activated catalyst powder with high purity under the protection of nitrogen formed catalyst slurry, and then enter the loop reactor, ethylene monomer after refining, and hydrogen, a TIGI olefin monomer 1 pre mixed and then injected into the loop reactor, the ethylene production of polyethylene in the presence of catalyst. The axial flow pump maintains the high speed flow and very uniform mixing of the material in the reactor, and the reaction heat is evacuated evenly from the jacket cooling water. The MI range of this process is 0.15 - 100, and the density is 0.936 - 0.972 g/cm3. The characteristics of the reactor loop is: less equipment, short process, low investment cost; do not produce wax and oligomer, not sticking to the wall; the powder of good shape, easy to transport; depending on the reaction heat jacket of the reactor cooling water out, heat removing easy, convenient adjustment; raw material demand is higher, need purification; copolymerization the monomer using hexene; using isobutane as solvent, the easy escape of residual solvents. The process flow is as follows: fresh polymerized ethylene is mixed with molecular weight regulator hydrogen, antifreeze and circulating diluent isobutane after drying, and then sent into a multi loop continuous flow reactor, and catalyst is added into isobutane into a reactor. The reaction temperature is 106.7 degrees centigrade, and the pressure is 3.9MPa. The polymer and the diluent residual pulp through the axial flow pump at the speed of 6m/s through the loop reactor. Reactor water cooling control reaction temperature set in the solid polymer by loop reactor outlet vertical settlement. As a result, the concentration of slurry can reach 55% and the conversion rate is 98% - 99%. The polymer is discharged after the flash evaporation to discharge the isobutane and the residual monomer into the diluent recovery unit. Other solid polymers are mixed with additives and granulation. 2, gas phase polymerization and gas phase polymerization (gas phase fluidized bed method) typical process for Innovene technology univation Technology chemical company DOW univation technology and INNOS company by low pressure gas phase fluidized bed reactor using z/n catalyst and catalyst, purification of raw material into the reactor, resulting in polymerization catalyst storage under the action of reaction in 85~110. [. Pressure was conducted for 2.41 MPa, the single pass conversion of ethylene is about 1% ~ 2%, the reaction heat removal mainly through the cooling cycle logistics, MI range of products for the production of 0.01 to 150, the density ranges from 0.915 to 0.970 g/cm3. The characteristics of gas phase fluidized bed polymerization process is: low operating pressure, low temperature; can produce full density polyethylene; catalyst system including titanium, chromium; metallocene catalyst; high purity of raw material, all raw materials are to be refined; without solvent, low energy consumption, low operation cost and maintenance. The production process is: dry monomers with PC 1-9357/2╈PC 1-9357/2 COC日本DX4900 HDPE沙特�？松�美孚FTA-001 PC基礎(chǔ)創(chuàng)新塑料 ERL0363 PC奇美 PC -6710 PP中石化茂名EPR300 PMMA 韓國LG IF830 TPU拜耳優(yōu)得3695AU PBT新光F202G30BK PA66法國羅地亞A216V50 ABS奇美PA-777E PC德國科思創(chuàng)（拜耳） APEC 1800 LLDPE榆林延長中煤DFDA-7042 PA6基礎(chǔ)創(chuàng)新塑料PX11311U SEBS日本可樂麗4055 POM 美國赫斯特 C13031XF PP李長榮7433 PA66日本杜邦HTN51G35L BK337 EVA臺塑7320M PP荷蘭利安德巴塞爾X M2 T24 PC基礎(chǔ)創(chuàng)新塑料(南沙) EXL1434T AS(SAN)鎮(zhèn)江奇美D-168 PA6T 日本三井化學(xué) C3000 POM 以色列普利朗 PM7109BK11T HIPS韓國LG405AF PC基礎(chǔ)創(chuàng)新塑料(南沙) MPX2-WH9G554 ETFE 美國杜邦 2195 EVOH 日本合成化學(xué) DC3023RB EMMA日本住友化學(xué)SWA210 POM 美國杜邦 DE-20199 LDPE亞聚F1100 PC基礎(chǔ)創(chuàng)新塑料 DFL4034 TPEE日本東麗7247W KI016 PP馬來大騰石化SM-388 POM 日本寶理 HP25X PBT日本寶理2002 EF2001 hydrogen added to a reactor system, the raw material into a large circulation steam flow circuit, and through the gas distribution by entering the large fluidized bed reactor at the bottom, according to the design of the reactor material 69.57% (ethylene vinyl content of 99.9%, 0.1%, 10.43%, 7.56% hydrogen oxide) ethane and 12.44% nitrogen. This raw gas consists of the production of the product with the 8g/10min melt index and the density of the 0.964g/cm3. The catalyst consists of titanium trichloride and tetrahydrofuran for two Magnesium Oxide mixture accelerator, AlEt3 catalyst. The catalyst enters the device in the form of solid state and nitrogen from the non pain reactor. The operating temperature is 105 centigrade, and the specific temperature is determined according to the brand name. The reactor pressure is 2.0MPa, and the reaction gas comes out from the top of the reaction. The cyclone separates the catalyst containing solid material and sends it back to the reactor. Then the gas from the cyclone separator is circulated to the bottom of the reactor after the compression and circulating coolers. The reactor discharge through an air lock system intermittently to product tank. Part of the gas entering the discharge tank enters the compressor cycle system through the upper buffer tank, filter, gas cooler, and separation tank. The polymer comes out from the lower part of the discharge tank and enters the washing tank and the post treatment system.