首页> 外国专利> Continuous 3-step bulk copolymerisation of styrene - comprising continuous copolymerisation, monomer mixt. addn. and copolymerisation in flooded mixer

Continuous 3-step bulk copolymerisation of styrene - comprising continuous copolymerisation, monomer mixt. addn. and copolymerisation in flooded mixer

机译:苯乙烯的连续三步本体共聚-包括连续共聚,单体混合物。地址混合器中进行共聚

摘要

Continuous bulk polymerisation of monomers having different reactivities, i.e. (A) 22-92 mol. % styrene and/or alpha-Me styrene, (B) 0.78 mol% =1 nitrile gp.-contg. mono-olefinically unsatd. monomer and (C) 0-50 mol. % =1 mono-olefinically unsatd. monomer other than (A) or (B), where A + B + C = 100 mol. %, takes place in homogeneous liquid phase of 1-20 bar, by (I) 100 pts. wt./time unit of monomer mixt. of (A1) 4-99.6 mol. % (A), (B1) 0.-96 mol. % (B) and (C1) 0-80 mol. % (C), copolymerised to 10-60 mol. % conversion to copolymer abc at 60-150 degrees C, in presence of an initiator having half-life period at polymerisation temp. 1/10 of av. dwelling time and mixing time, in a tank reactor allowing continuous flow and ideal mixing, at av. periods of dwell 10-240 min. and mixing times 5-120 secs. (II) 0.5-100 pts. wt./time unit of monomer mixt. of (A2) 0-100 mol. % (A), (B2) 0-100 mol. % (B) and (C2) 0-100 mol. % (C), where sum of mol. % of A1B1C1 and of A2B2C2 is 100, is mixed with 0.01-0.5 wt. %, w.r.t. sum of residual monomers of A1B1C1 and of monomers A2B2C2, of an initiator having half-life period of polymerisation temp. of step (III) 1/10 dwelling period and mixing time of polymerisation batch. (III), continuous copolymerisation takes place, in bulk, homogeneous phase, in a completely flooded, self-cleaning polymerisation mixer with moving mixer devices stripping walls and one another, at 100-250 degrees C, with av. period of dwell 10-480 min. and mixing times 0.1-4 min., up to residual monomer content 10-50 mol. %, w.r.t. total monomers. Residual monomer-contg. copolymer ABC is purified from residual monomers, down to 0.5 wt. % w.r.t. copolymer, by setting up a vacuum or by blowing in inert gas. Products are used as thermoplastic moulding compsns. for injection moulded, ddep drawn and compressed articles, e.g. dishes, armatures, household goods, internal fitting for cars and boats, optical and electronic devices, and foils and containers for packing foods. Copolymers have av. mol. wt. 104 to 106, intrinsic viscosity 0.1-2 dl/g (in DMF at 25 degrees C), are transparent, glass-clear, and have heat shape stability at 90-130 degrees C. Notch impact strength according to DIN 7741 is 2-10 cm kp/cm2, melt index, at 200 degrees C and 21.6 kp loading, is 2.8-20 g/101.
机译:具有不同反应性,即(A)22-92 mol的单体的连续本体聚合。 %的苯乙烯和/或α-Me苯乙烯,(B)0.78mol%> = 1腈gp.-contg。单烯烃不饱和的。单体和(C)0-50摩尔。 %> = 1的单烯烃未饱和。 (A)或(B)以外的单体,其中A + B + C = 100摩尔。 %在1-20巴的均相液相中发生(I)100点。重量/单体混合物的时间单位。 (A1)的4-99.6摩尔。 %(A),(B1)0.-96摩尔(B)和(C1)%0-80mol。 %(C),共聚至10-60mol。在具有在聚合温度下具有半衰期的引发剂的存在下,在60-150℃下转化成共聚物abc的%转化率。平均值的1/10在罐式反应器中的停留时间和>混合时间,允许连续流动和理想混合,在av下。停留时间10-240分钟。和混合时间5-120秒。 (II)0.5-100点。重量/单体混合物的时间单位。 (A2)的0-100摩尔。 %(A),(B2)0-100摩尔(B)和(C2)%0-100mol。 %(C),其中mol的总和。将A1B1C1和A2B2C2的100重量%与0.01-0.5重量%混合。 %,w.r.t.具有聚合温度半衰期的引发剂的A1B1C1残余单体和A2B2C2残余单体之和。步骤(III)的停留时间为1/10,聚合批料的混合时间为1/10。 (III),连续共聚在本体均相中,在完全注满的,自清洁的聚合混合器中进行,该混合器具有移动混合器装置,在100-250℃下用AV分别剥离壁。停留时间10-480分钟。混合时间为0.1-4分钟,直至残余单体含量为10-50摩尔。 %,w.r.t.总单体。残留单体(含)。从残留的单体中纯化共聚物ABC,低至0.5 wt。 %w.r.t.通过设置真空或吹入惰性气体来形成共聚物。产品用作热塑性模塑组合物。用于注塑,压延和压缩制品的注塑,例如餐具,电枢,家庭用品,汽车和轮船的内部配件,光学和电子设备以及包装食品的箔和容器。共聚物具有摩尔重量104至106,特性粘度0.1-2 dl / g(在25摄氏度时于DMF中),透明,玻璃透明,在90-130摄氏度时具有热形稳定性。根据DIN 7741的缺口冲击强度为2-在200摄氏度和21.6 kp载荷下的10 cm kp / cm2熔体指数为2.8-20 g / 101。

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