Abstract:Polybutylene (PB) refers to a series of commercial semicrystalline resins derived from high molecular weight, predominantly isotactic poly(1‐butene) homopolymer or copolymer. 1‐Butene is manufacture by the catalytic oligomerization of ethylene. It can also be manufactured from mixed butylenes streams: acid extraction, the Sorbutene process, and the methyl
tert
‐butyl ether process. Isotactic poly (1‐butene) is manufactured by a stereospecific Zeigler‐Natta polymerization. In melt proces… Show more
Section: Metallocene Synthesis Synthesis Of 11mentioning
confidence: 99%
“…[1] The key aspect of iPB production is that it is a solution-bulk process, since this polyolefin is soluble in liquid 1-butene, in the temperature range 40-90 8C, up to concentrations of about 40 wt.-%.…”
Section: Introductionmentioning
confidence: 99%
“…[1,2,3] Following the acquisition of the isotactic poly(1-butene) business from Shell, Basell Polyolefins has recently started production of iPB in a new plant with a capacity of 45 kTon Á a À1 in the Netherlands. [4] This production is based on a tworeactor cascade process, [5] and uses a ZN catalyst largely improved [6] with respect to earlier ZN catalysts used for polybutene.…”
Section: Introductionmentioning
confidence: 99%
“…[4] This production is based on a tworeactor cascade process, [5] and uses a ZN catalyst largely improved [6] with respect to earlier ZN catalysts used for polybutene. [1,2,7] Much less information is available on PB produced with metallocene catalysts. In the case of poly(propylene), metallocene catalysts can produce almost any type of chain microstructure.…”
Summary: Isotactic polybutenes of variable isotacticity and melting points of form I in the range 100–125 °C have been prepared with both C2‐ and C1‐symmetric zirconocenes. The C1‐symmetric zirconocenes bearing the bilateral symmetric 2,5‐dimethyl‐7H‐cyclopenta[1,2‐b:4,3‐b′]dithiophene ligand connected by a dimethylsilandiyl bridge to a substituted indenyl ligand produce iPB with higher molecular mass, up to 400 000 at polymerization temperature of 70 °C in liquid butene. The degree of isotacticity depends on the substitution pattern of the indenyl ligand. The correlations between microstructure and melting points of the crystalline forms I and II of iPB have been defined. Some relevant differences in catalyst selectivity between propylene and 1‐butene polymerizations have been identified.Linear correlation of melting points of form I and form II in isotactic poly(1‐butene)s of different chain regularities.magnified imageLinear correlation of melting points of form I and form II in isotactic poly(1‐butene)s of different chain regularities.
Section: Metallocene Synthesis Synthesis Of 11mentioning
confidence: 99%
“…[1] The key aspect of iPB production is that it is a solution-bulk process, since this polyolefin is soluble in liquid 1-butene, in the temperature range 40-90 8C, up to concentrations of about 40 wt.-%.…”
Section: Introductionmentioning
confidence: 99%
“…[1,2,3] Following the acquisition of the isotactic poly(1-butene) business from Shell, Basell Polyolefins has recently started production of iPB in a new plant with a capacity of 45 kTon Á a À1 in the Netherlands. [4] This production is based on a tworeactor cascade process, [5] and uses a ZN catalyst largely improved [6] with respect to earlier ZN catalysts used for polybutene.…”
Section: Introductionmentioning
confidence: 99%
“…[4] This production is based on a tworeactor cascade process, [5] and uses a ZN catalyst largely improved [6] with respect to earlier ZN catalysts used for polybutene. [1,2,7] Much less information is available on PB produced with metallocene catalysts. In the case of poly(propylene), metallocene catalysts can produce almost any type of chain microstructure.…”
Summary: Isotactic polybutenes of variable isotacticity and melting points of form I in the range 100–125 °C have been prepared with both C2‐ and C1‐symmetric zirconocenes. The C1‐symmetric zirconocenes bearing the bilateral symmetric 2,5‐dimethyl‐7H‐cyclopenta[1,2‐b:4,3‐b′]dithiophene ligand connected by a dimethylsilandiyl bridge to a substituted indenyl ligand produce iPB with higher molecular mass, up to 400 000 at polymerization temperature of 70 °C in liquid butene. The degree of isotacticity depends on the substitution pattern of the indenyl ligand. The correlations between microstructure and melting points of the crystalline forms I and II of iPB have been defined. Some relevant differences in catalyst selectivity between propylene and 1‐butene polymerizations have been identified.Linear correlation of melting points of form I and form II in isotactic poly(1‐butene)s of different chain regularities.magnified imageLinear correlation of melting points of form I and form II in isotactic poly(1‐butene)s of different chain regularities.
“…[14] iPB is a high margin polyolefin with a relatively small world production (ca 50 kt/yr), which is however five-fold larger with respect to the market size in the 1980s; its properties and applications, and the production process based on ''classical'' heterogeneous Ziegler-Natta catalysts, have been reviewed. [15] The key aspect of iPB production is that it is a solution bulk process, since the polymer is soluble in liquid 1-butene in the temperature range of 40-90 8C up to concentrations of about 40% by weight. This makes the application of homogeneous catalysts particularly advantageous because the control of polymer morphology is not an issue, of course provided that catalysts with an adequate stereoselectivity and molecular mass capability are available.…”
In spite of the reputation to be a mature area, Ziegler‐Natta olefin polymerization continues to produce scientific and industrial breakthroughs at a surprising pace. The massive introduction of High Throughput Screening technologies has accelerated the innovation process even further. This Highlight aims at introducing the reader to a number of very recent publications in which novel metallocene and non‐metallocene (“post‐metallocene”) olefin polymerization catalysts, and new concepts of chain growth in insertion polymerization, are disclosed and elegantly and convincingly discussed.magnified image
The effect of the presence of a layered double hydroxide (LDH) nanofiller on the crystallization behavior of a random isotactic butene-1/ethylene copolymer was investigated. Addition of LDH enhanced heterogeneous nucleation of the ordering process of the polymer matrix leading to an increase of the temperature of formation of the Form II mesophase on cooling the melt. Consequently, the size of spherulites of the polymer matrix was markedly reduced in the nanocomposites. In contrast, the Form II mesophase-Form I crystal phase transition kinetics and the final crystallinity were not affected by the presence of LDH. Addition of the LDH nanofiller led to a beneficial increase of the stiffness which suggests a route for compensating of the lower stiffness of the random copolymer compared to the homopolymer. Random copolymerization accelerates the disadvantageous room-temperature mesophasecrystal transition, but results in a reduction of the crystallinity. The addition of LDH counterbalances the lowering of the crystal fraction.
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