Abstract:
Pre-treatment methods for polyolefin-based feed streams before depolymerization are described. Polyolefins are separated from other material in the polyolefin-based feed stream using density differences in an aqueous solution, which allows for a pre-treatment method that does not affect the depolymerization catalyst. By removing the non-polyolefin materials from the feed stream, the depolymerization of the polyolefin material can proceed at lower temperatures for longer cycles. This results in a more efficient process with a smaller carbon footprint.
Abstract:
A pre-polymerized catalyst component for the polymerization of olefins endowed with high activity and morphological stability comprises a non-stereospecific solid catalyst component containing Ti, Mg and a halogen, and an amount of an ethylene/alpha-olefin block (co)polymer ranging from 0.1 up to 5g per g of said solid catalyst component, said prepolymerized catalyst component being characterized by a mercury porosity, due to pores having radius up to 1 μm, ranging from 0.15 to 0.5 cm 3 /g and by the fact that at least 55% of said porosity is due to pores having pore radius up to 0.2μm.
Abstract:
Solid adducts comprising MgCl 2 and water and optionally an organic hydroxy compound (A) selected from hydrocarbon structures containing at least one hydroxy group, said compounds being present in molar ratio defined by the following formula MgCl 2 •(H 2 0) n (A) p in which n is from 0.6 to 6, p ranges from 0 to 3, said adduct having a porosity (P F ), measured by the mercury method and due to pores with radius equal to or lower than 1μm, of at least 0.15 cm 3 /g with the proviso that when p is 0, (P F ) is equal to or higher than 0.3 cm 3 /g.
Abstract translation:包含MgCl 2和水以及任选的选自含有至少一个羟基的烃结构的有机羟基化合物(A)的固体加合物,所述化合物以限定的摩尔比存在 通过以下公式MgCl 2·(H 2 O)n(A)p·p其中n为从 0.6至6,p的范围为0至3,所述加合物具有通过汞法测量的孔隙率(P F)和由于半径等于或低于1μm的孔隙而至少为0.15 cm 3 / g,条件是当p为0时,(P F)等于或高于0.3 cm 3 / g / g。 p>
Abstract:
A solid catalyst component comprising Ti, Mg, halogen and a couple of monofunctional electron donor compounds MD1 and MD2 selected from esters and ethers, said donors being present in amounts such that the molar ratio MD1/MD2 ranges from 20 to 800. The so obtained catalyst component when converted into a catalyst is able to produce ethylene polymers with good morphological properties even under drastic polymerization conditions.
Abstract:
A method of depolymerizing plastic waste using a supported heteropolyacids catalyst is described herein. The method provides with high efficiency a high quality liquid depolymerization product usable as cracker feedstock.
Abstract:
Catalytic compositions for depolymerizing polyolefin-based waste material into useful petrochemical products and methods of use are described. The compositions are a composite of at least one zeolite catalyst with one or more co-catalyst(s) that is a solid inorganic material. These composite catalysts, along with heat, are used to both increase the depolymerization reaction rate of the feed streams and suppress poisoning effects of non-polyolefin polymers that may be present. This results in a shorter residence time in the depolymerization unit and more efficient process.
Abstract:
A process for preparing a catalyst component comprising Mg, Ti, and at least an electron donor compound (ID) said process comprising two or more steps of reaction in which in a first step (a) carried out at a temperature ranging from 0 to 150°C, a Mg based compound is reacted with a Ti compound, having at least a Ti-Cl bond, in an amount such that the Ti/Mg molar ratio is greater than 3 so as to generate an intermediate solid catalyst component containing Mg and Ti and, in a following step (b), the intermediate solid catalyst component (a) is contacted, in a gaseous dispersing medium, with a gaseous stream containing the electron donor compound (ID) thereby obtaining a final solid catalyst component having an ID/Ti molar ratio ranging from 0.5:1 to 20:1.
Abstract:
A process for the preparation of a solid catalyst component comprising a Ti compound, a coloring agent and optionally an electron donor on a Mg chloride based support, said process comprising one or more steps (a) carried out at a temperature ranging from 0 to l50°C in which a Mg based compound of formula (MgCl m X 2-m )·nLB, in which m ranges from 0 to 2, n ranges from 0 to 6, X is, independently R 1 , OR 1 , -OCOR 1 or O-C(O)-OR 1 group in which R 1 is a C 1 -C 20 hydrocarbon group and LB is a Lewis base, is reacted with a liquid medium comprising a Ti compound having at least a Ti-Cl bond in an amount such that the Ti/Mg molar ratio is higher than 3; said process being characterized by the fact that in at least one of said steps an organic coloring agent is present either associated to the Mg compound or dispersed in said liquid medium comprising the titanium compound.
Abstract:
A catalyst mixture comprising (a) particles of solid catalyst component comprising Ti, Mg, Cl, and from 0.2 to 5.0% by weight of particles of an inorganic solid compound having particle size ranging from 0.1 µm to 1 mm containing more than 50% by weight of SiO 2 units.
Abstract:
Solid adducts comprising MgCl 2 , ethanol and water characterized in that the amount of ethanol ranges from 50% to less than 57% by weight, the amount of water is ranges from 0.5 to 5% by weight, the ethanol/water weight ratio is lower than 60 and the porosity determined with Hg method due to pores with radius up to 1μm and expressed in cm 3 /g, is lower than 0.2.