Catalyst

A catalyst, titanium catalyst technology, applied in the direction of chemical/physical processes, etc., can solve the problems of exhaustion and high cost, adverse effects on catalyst performance, etc.

Inactive Publication Date: 2003-12-24
SASOL TEKHNOLODZHI PROPRIEHJTEHRI LTD
View PDF3 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

All these methods are very exhausting and expensive
The use of desiccants is required in many cases, and

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 2

[0082] Catalyst (B) preparation

[0083] In a 250ml flask equipped with a reflux condenser and a stirring device, 2g of magnesium chloride with a total water content of 1.5% (mass ratio) was suspended in 60ml of highly purified hexane. The temperature of the suspension was heated to 45° C., and then 2 ml of dibutyl ether was added to the flask, and the heating was stopped. The mixture was stirred for 3 hours after the heating was stopped. To avoid excessive heat build-up, 9 g of triethylaluminum ('TEA') was added dropwise and the resulting slurry was cooled to room temperature with stirring. The slurry was washed 12 times with 50 ml of hexane solution each time to obtain a slurry containing the activated carrier.

[0084] 2 ml of a 3:1.5:1 molar ratio of ethanol:1-pentanol:1-hexanol mixture was added to the slurry containing the activated carrier, and the slurry was stirred for 3 hours. Then add 20ml TiCl to the slurry 4 , and the resulting mixture was stirred at reflux ...

Embodiment 3

[0086] Add 300 ml of highly purified n-heptane to a 11 stainless steel reactor equipped with a stirring device. The reactor was heated to 85°C, and 1 ml of a 10% by weight TEA solution was added thereto. 0.1 ml of Catalyst B was added to the reactor, the mixture was stirred for 5 minutes, after which time the reactor was pressurized to 15 bar with ethylene and the reaction started. The reaction was continued for 60 minutes at normal pressure maintained by ethylene, after which the ethylene supply was cut off and the reactor was evacuated. Isopropanol was added to deactivate the catalyst and the reaction mixture was cooled to room temperature. The slurry was filtered, washed with isopropanol and acetone, and the obtained polymer was dried under reduced pressure in a vacuum oven at 80° C. for 24 hours. The dry polymer in powder form was weighed to obtain 83 g of polymer. The activity of Catalyst B was calculated to be 83 kg / g catalyst per hour. Example 4

Embodiment 4

[0087] Add 300 ml of highly purified n-heptane to a 11 stainless steel reactor equipped with a stirring device. The reactor was heated to 85°C, and 1 ml of a 10% by weight TEA solution was added thereto. 0.1 ml of Catalyst A was added to the reactor and the mixture was stirred for 5 minutes after which time the reactor was pressurized to 15 bar with ethylene and the reaction started. The reaction was continued for 60 minutes at normal pressure maintained by ethylene, after which the ethylene supply was cut off and the reactor was evacuated. Isopropanol was added to deactivate the catalyst and the reaction mixture was cooled to room temperature. The slurry was filtered, washed with isopropanol and acetone, and the obtained polymer was dried under reduced pressure in a vacuum oven at 80° C. for 24 hours. The dry polymer in powder form was weighed to yield 58.1 g of polymer. The activity of catalyst A was calculated to be 58.1 kg / g catalyst per hour. Example 5

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

PropertyMeasurementUnit
Surface areaaaaaaaaaaa
Surface areaaaaaaaaaaa
Surface areaaaaaaaaaaa
Login to view more

Abstract

Disclosed are terpolymers and processes of terpolymerization, wherein the terpolymer comprises units derived from ethylene, 1-pentene and another alpha-olefin containing at least six carbon atoms.

Description

technical field [0001] The present invention relates to a catalyst. In particular, the present invention relates to catalysts and catalyst systems for the polymerization of olefins, as well as to methods of preparing such catalysts and to methods of polymerization. Background technique [0002] As is known, magnesium chloride can form five hydrates, namely MgCl 2 12H 2 O, MgCl 2 ·8H 2 O, MgCl 2 ·6H 2 O, MgCl 2 4H 2 O and MgCl 2 2H 2 O. From the point of view of application or general use, the most important hydrate form is the hexahydrate form, MgCl 2 ·6H 2 O, which is MgCl obtained by known methods 2 2H 2 General raw material of O. It is also known that olefin polymerization can be adversely affected by even traces of water present in the reaction medium or in the Ziegler-Natta catalyst used in the process. In the polymerization of olefins, the use of Ziegler-Natta catalysts supported on magnesium chloride and containing even a very low proportion of water c...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
IPC IPC(8): C08F4/654B01JC08FC08F2/02C08F2/04C08F2/06C08F2/34C08F4/02C08F4/60C08F4/642C08F4/651C08F4/655C08F4/658C08F10/00C08F210/14C08F210/16C08GC08J5/18C08L23/18
CPCC08F210/16C08F10/00Y10S526/916C08F4/6555C08F210/14C08F210/08C08F2500/12
Inventor 达维德·约翰尼斯·朱伯特伊格内修斯·亨德里克·波特吉特伊万·廷卡
Owner SASOL TEKHNOLODZHI PROPRIEHJTEHRI LTD
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products