KR800001212B1 - Titanium-modified silyl chromate catalysts for ethylene polymerization - Google Patents

Abstract

H2 or coplymn. of CH2:CH2 and α-olefin was carried out over silylchromate catalyst(I; R = C1-4 hydrocarby1) which was deposed on Al, Ti-contg. silica carrier having large surface area. Thus, 20g polypor silica was impregnated in 1.5g Al(NO3)39H2O, slurried with 100ml C5H12, and impregnated in 2.8g Ti(OC3H7)4, and then was heated at 500-1000≰C to obtain the silica carrier base. The carrier base was mixed with 50ml n-C6H14 and bis-triphenyl silylchromate followed by heating in N2 to give silica catalyst.

Description

Ethylene Polymerization Process Using Titanium Modified Silyl Chromate Catalyst

The present invention relates to a process for polymerizing ethylene using a catalyst composed of silyl chromate deposited on a silica carrier comprising aluminum and titanium.

Although chromium oxide supported titanium containing catalysts for ethylene polymerization are known, they are required to be activated by heating at temperatures above 300 ° C. and temperatures up to 1,000 ° C. in the atmosphere of oxidation. This activation is carried out after the deposition of chromium oxide on the carrier (see US Pat. No. 3,622,521 and Dutch Patent Application No. 10,881 / 72).

In the present invention, the titanium / aluminum modified silica carrier is heated at high temperature prior to depositing the silyl chromate.

The catalyst for preparing a polymer of ethylene copolymerized with ethylene alone or with alpha-olefins containing 3 to about 6 carbon atoms contains silyl chromate having the following structural formula.

Where R is a hydrocarbyl group containing from 1 to about 14 carbon atoms adsorbed onto a high surface area silica carrier preheated to a temperature of 500-1,000 ° C., including aluminum and titanium. These catalysts can be used to produce ethylene polymers having a higher melt index than conventional catalysts.

In general, the catalysts of the present invention are prepared by heat treating a silica carrier containing aluminum and titanium followed by deposition of silyl chromate.

After the silyl chromate is deposited on the silica carrier, no heat treatment is performed on the catalyst. Depositing silyl chromate on a silica carrier is not strictly critical. It is convenient to deposit silyl chromate from a solution in which silyl chromate is dissolved in an organic solvent.

Suitable organic solvents include alkanes, such as pentane, hexane, heptane and octane, containing about 5 to 10 carbon atoms, for example cyclopentane cyclohexane and cycloheptane, containing about 5 to 7 carbon atoms; The same cycloalkanes, containing 6 to about 12 carbon atoms, for example aromatic compounds such as benzene, fluene, xylene and ethyl benzene.

Representative examples of high surface area silica carriers are microspherical medium density (MSID) silica (WR Grace G-) with a surface low of 300 square meters per gram, a pore diameter of 200 microns and an average particle size of 70 microns (0.0028 inches). 952 grade), medium density (ID) silica (WRGrace G-56 grade) with a surface area of 300 square meters per gram, a pore diameter of 160 mm and an average particle size of 103 microns (0.0040 inches), and 400 square per gram And Davidson Grade 967 silica having a meter surface area and a pore volume of 0.90 cc / g. Davidson Grade 967 silica contains 13 weight percent aluminum oxide.

Aluminum can be introduced into the catalyst of the present invention by selecting a silica with chemically bonded alumina as in the case of the Davidson 967 grade or by treating the silica with a solution of an aluminum compound such as aluminum nitrate.

Titanium compounds used in the preparation of the catalysts of the present invention are those described in US Pat. No. 3,622,521 and Dutch Patent Application No. 10,881 / 72. These compounds have the following structural formulas.

(I) (R ′) _n Ti (OR) _m

(II) (RO) _m Ti (OR ′) _n

Wherein m is 1,2,3 or 4, n is 0,1,2 or 3, m + n is 4, R is C ₁ -C ₁₂ alkyl, aryl or cycloalkyl group, and aralkyl and alka Their combinations, such as reels, TR 'are R, cyclopentadienyl, and C ₂ -C ₁₂ alkenyl groups such as ethenyl, propenyl, isopropenyl, or butenyl.

(III) TiX ₄

Where X is a halogen atom and is fluorine, chlorine, bromine or iodine. Titanium compounds include titanium tetrachloride, titanium tetraisopropoxide and titanium tetrabutoxide. Titanium compounds are more conveniently deposited on silica carriers from their hydrocarbon solvent solutions.

The amount of titanium in the catalyst of the present invention is 2-30% by weight based on the weight of silica calculated as TiO ₂ .

Aluminum may be bound on the silica carrier by treating the silica carrier with a solution of an aluminum compound or present from the beginning in the silica precursor in the form of alumina. Although 0.01-50% by weight of alumina may be present on the entire carrier, it is preferable to adopt a carrier containing 0.05-20% by weight of alumina based on the weight of the carrier.

Although the R substituent in the silicate salt of the present invention may contain 1-14 carbon atoms, the substituent preferably contains about 3-10 carbon atoms. Examples of these hydrocarbon groups are, for example, methyl, ethyl, propyl, isopropyl, n-butyl, isobutyl, n, pentyl, isopentyl, t-pentyl, hexyl2-methylpentyl, decyl, tridecyl, tedadedecyl, Benzyl, phenylethyl, P-methylbenzyl, phenyl, tolyl, xylyl, niphthyl, ethylphenyl, methylnaphthyl and dimethylnaphthyl. Silicates containing alkyl substituents can be used with proper care in advance, but they are unstable.

Examples of suitable silicate salts which may be used in the present invention include the following compounds. Bis-triphenylsilyl chromate, bis-tritolylsilyl chromate, bis-trixylyl chromate, bis-trinarylsilyl chromate, and polydiphenylsilyl chromate.

It is advantageous to use fluorinating agents with these catalysts where changes in the molecular weight distribution and the copolymerization rate of ethylene and comonomers are desired. If a fluorinating agent is used, it is combined with the silica carrier prior to the deposition of the silylchromate. On the other hand, if up to about 10% by weight of fluorinating agent can be used based on the weight of silica, it is preferable to use about 0.05-1.0% by weight of fluorinating agent.

Fluorine compounds that can be used include HF, or any fluorine compound that produces HF under catalytic preparation conditions. Fluorine compounds other than HF that can be used are described in Dutch Patent Application No. 10881/72.

These compounds include ammonium hexafluorophosphate, ammonium hexafluorosilicate, ammonium tetrafluorosilicate, ammonium tetrafluoroborate and ammonium hexafluoro titanate.

Fluorine compounds are conveniently deposited on their silica carriers from their aqueous solutions or by dry mixing the solid fluorine compounds with other components of the catalyst during production.

The invention will be described in more detail by the examples described below. All parts and percentages are by weight.

[Control Example 1]

A. Silica Carrier Preparation

To a solution in which 1.5 g of Al (NO ₃ ) ₃ .9H ₂ O was dissolved in 150 ml of water, 20 g of polypor silica obtained from the National Petrochemical Company was added. The silica had a pore texture of 250-270 mm ₃ and a surface area of 370-400 m ₂ / g. The mixture was filtered to recover 74 ml of filtrate. The silica residue was then dried. Some of the dried residue was heated to 820 ° C. for 16 hours under nitrogen gas and then cooled. The aluminum concentration of the produced silica carrier was 0.5% by weight based on Al ₂ O ₃ .

B. Polymerization Catalyst Preparation

A polymerization catalyst was prepared by mixing 0.98 g of the silica carrier prepared in Step A with 50 ml of n-hexane and 0.030 g of bis-triphenylsilyl chromate. This mixture was stirred at room temperature for 1 hour under nitrogen gas. The resulting slurry was used as a polymerization catalyst.

C. Evaluation of Polymerization Catalyst

The slurry prepared in Process B was charged to a 1000 ml stirred high pressure reaction vessel together with 500 ml of n-hexane and 40 ml of l-hexane. The vessel was then sealed and pressurized to 200 psig with ethylene. The polymerization was carried out at 86 ° C. for 75 minutes. If 185 g of ethylene polymer were obtained, it had a melt index of 0.28 dg / min, a flow index of 11.7 dg / min and a density of 0.939 g / cc.

[Control Example 2]

Repeated as described in Comparative Example 1 except that .093 g of silica carrier was used with 0.030 g of bis-triphenylsilylchromate to prepare the catalyst. l-hexane was replaced with 20 psig of propylene.

Using the same polymerization catalyst evaluation method as in Comparative Example 1, 31 g of ethylene copolymer was obtained after 110 minutes, which gave a melt index of 2.69 dg / min, a flow index of 243 g / min and a density of 0.904 g / cc. Had

[Control Example 3]

Repeated as described in Comparative Example 1 except that 0.98 g of silica carrier was used with 0.030 g of bis-triphenylsilylchromate to prepare the catalyst, except that no comonomer was used with ethylene. to be. When using the same catalyst evaluation method as in Comparative Example 1, 150 g of ethylene homopolymer was obtained after polymerization for 105 minutes.

This homopolymer showed no melt index and a flow index of 1.0 dg / min.

Example 1

A. Preparation of Silica Carrier.

To a solution of 1.50 grams of Al (NO ₃ ) ₃ .9H ₂ O dissolved in 150 ml of water was added 20 grams of polyfosyl silica described in Control Example 1. The mixture was filtered to recover 74 ml of filtrate. The residue was then dried. 9.3 grams of residue dried at 200 ° C. was slurried with 100 ml of pental and then combined with 2.8 g of titanium tetraisopropoxide. The solvent was evaporated and the residue was heated in oxygen gas at 810 ° C. for 17 hours to form a carrier. The Al content was calculated as Al ₂ O ₃ , 0.5%, and the Ti content was calculated as TiO ₂ , 7.5%.

Polymerization catalyst manufacturing

The polymerization catalyst was prepared by mixing 1.0 g of the silica carrier prepared in item A, 50 ml of n-hexane, and 0.030 g of bis-triphenylsilyl chromate. The mixture was stirred for 1 hour at room temperature in the presence of nitrogen. The resulting slurry was used as a polymerization catalyst.

Polymerization catalyst evaluation

The catalyst slurry prepared in the above section B was charged in the stirred high pressure reaction vessel described in Comparative Example 1 together with 500 ml of hexane and 40 ml of l-hexane. The vessel was then sealed and pressurized to 200 psig with ethylene. The polymerization was carried out at 86 ° C. for 40 minutes. A copolymer of 136 g of ethylene and l-hexane was obtained, which had a melt index of 2.81 dg / min, a flow index of 92.1 dg / min and a density of 0.932 g / cc.

Example 2

The method of Example 1 was repeated with the same catalyst slurry, except that l-hexane was replaced by charging 20 psig of propylene into the polymerization reactor. The polymerization was carried out at 86 ° C. for 90 minutes, and a copolymer of 99 g of ethylene and propylene having a melt index of 27.5 dg / min and a density of 0.895 g / cc was obtained.

Example 3

A. Preparation of Silica Carrier

The sample of polyporous silica described in Control Example 1 was dried at 200 ° C., and then 10.1 g of this silica was slurried with 100 ml of pentane. To this slurry was added a solution in which 0.115 grams of aluminum trisphotooxide was dissolved in toluene, followed by 3.0 grams of titanium tetraisotopoxide. This solvent was removed by evaporation and the residue was heated at 770 ° C. for 16 hours in oxygen gas. Al content calculated by Al ₂ O ₃ was 0.3% by weight, and Ti content calculated by TiO ₂ was 7.6% by weight.

B. Polymerization Catalyst Preparation

The polymerization catalyst was prepared by mixing 1.0 gram of the silica carrier prepared in the above section A with 0.040 gram of bis-triphenylsilyl chromate and 50 ml of hexane. This mixture was stirred for 1 hour at room temperature in the presence of nitrogen. The resulting slurry was used as a polymerization catalyst.

C. Polymerization Catalyst Evaluation

The slurry prepared in the above section B was charged with 500 ml of n-hexane to the reaction vessel described in Comparative Example 1C. The vessel was sealed and pressurized to 200 psig with ethylene. After polymerization for 50 minutes at a polymerization temperature of 86 ° C., 108 g of ethylene homo copolymer was obtained, which had a flow index of 4.0 d / min. There was no flow in the standard melt index test. Table 1 shows the comparison data.

TABLE 1

Example 4

The procedure described in Example 3 was repeated, except that the catalyst slurry was prepared from 0.96 grams of silica carrier and 0.040 grams of bis-triphenicylyl chromate prepared in section A, and 30 psig of hydrogen was charged to the reaction vessel. The pressure was raised to 200 psig with ethylene. Using a reaction temperature of 86 ° C. and a reaction time of 45 minutes, 17 g of ethylene homopolymer was obtained, which had a melt index of 0.19 dg / min and a flow index of 31.0 dgmin. Hydrogen increases the resulting ethylene homopolymer and melt index.

Example 5

A. Preparation of Silica Carrier

The method described in Example 3A was repeated, except that 9.0 g of polyposilica, 0.110 g of aluminum triisopropoxide, 2.7 g of titanium tetraisopropoxide and additionally 0.09 g of ammonium hexafluor The exception is to use low silicate, (NH ₄ ) ₂ siF ₆ .

This mixture was then heated at 750 ° C. for 17 hours under oxygen gas and then cooled. The silica carrier prepared as described above had an aluminum content of 0.3 wt% based on Al ₂ O ₃ and a titanium content of 7.8 wt% calculated by TiO ₂ .

B. Polymerization Catalyst Preparation

The catalyst slurry was prepared using 0.93 grams of silica carrier, 50 ml of n-hexane and 0.04 grams of bis-triphenylsilyl chromate prepared in the above section A, using the method described in Section B of Example 1. .

C. Polymerization Catalyst Evaluation

The catalyst slurry prepared in the above section B was charged with 500 ml of n-hexane to the reaction vessel described in section C of the comparative example 1. The vessel was sealed and pressurized to 200 psig with ethylene. After reacting for 30 minutes at a polymerization temperature of 86 ° C., 55 grams of ethylene homopolymer with no flow in the melt index test but with a flow index of 9.5 dgmin were obtained.

Example 6

A. Preparation of Silica Carrier

967 grade siO ₂ -Al ₂ O ₃ (12.8 g) manufactured by Davidson Chemical Company was dried at 200 ° C and slurried by addition of 100 ml of pentane. The slurry was then combined with 3.8 g titanium tetraisopropoxide. The solvent was removed and the residue was heated at 750 ° C. for 17 hours under oxygen gas and then cooled. The resulting silica carrier had an aluminum content of 13% by weight calculated by Al ₂ O ₃ and a titanium content of 7.5% by weight calculated by TiO ₂ .

B. Polymerization Catalyst Preparation

The catalyst slurry was prepared using the method described in Section B of Example 1 using 1.0 g of the silica carrier prepared in Section A, 50 ml of n-hexane, and 0.03 g of bis-triphenylsilyl chromate. It became.

C. Polymerization Catalyst Evaluation

The catalyst slurry prepared in Section B was charged with 500 ml of n-hexane and 40 ml of l-hexane in the reaction vessel described in C of Control Example 1. The vessel was sealed and pressurized with ethylene to a pressure of 200 psig. The polymerization was carried out at 86 ° C. for 90 minutes. 80 g of ethylene copolymer was obtained, which had a flow index of 3.4 dgmin and a density of 0.933 g. Although the flow index of such copolymers is lower than that of the above examples and control examples, it should be understood that the flow index is greatly influenced by the physical structure of the intrinsic silica carrier.

The flow index will therefore vary depending on the structure of the particular silica carrier used to prepare the ethylene polymerization catalyst. However, titanium modified silylchromate catalysts on silica carriers produce ethylene polymers with higher flow indices than catalysts prepared without titanium treatment.

Example 7

The method described in Example 6 was followed as is, except that 40 ml of l-hexene was replaced with 20 psig of propylene as ethylene comonomer. The reaction time was 90 minutes, yielding 85 g of ethylene and propylene copolymer, which had a melt index of 2.88 dg / min, a flow index of 137 dg / min and a density of 0.905 g / cc.

Example 8

Fluidized Bed Polymerization of Ethylene

Several experiments were conducted to demonstrate the usefulness of the silica supported silylchromate catalyst of the present invention for polymerizing ethylene in a fluidized bed reactor using the fluidized bed reactor and two processes described in US Pat. No. 3,687,920. The data obtained in these experiments are shown in Table II.

The nature of the polymerization technique also affects the flow index of the ethylene polymer obtained using the catalyst of the present invention. Thus, an ethylene polymer having a lower melt flow index in the fluidized bed than in the slurry process is obtained. The preparation method of the catalyst used in this experiment is as follows.

Polyporous silica (500 g) was mixed with a solution of Al (No ₃ ) ₃ .9H ₂ O dissolved in ₃ L of water. This mixture was filtered and 1.5 L of filtrate was recovered. The residue dried at 200 ° C. was used as catalyst carrier. The dried carrier was slurried with isopentane and 35 g of titanium tetrasulfoxide was added per 100 g of carrier. The solvent was then evaporated. The residue was first heat treated at 150 ° C. for 2 hours under gas, then at 300 ° C. for 2 hours in air, and finally at 850 ° C. for 8 hours in air.

After cooling, the heat treated 458 g of support was slurried with isopentane and 18.4 g of bis-triphenylsilylchromate was added. After stirring for 1 hour, the solvent was evaporated.

TABLE II

Melt index was measured according to ASTMD-1238 at 190 ° C. and expressed in decigrams / minute. The flow index was determined at 10 times the weight used for the melt index test according to ASTMD-1238. Melt flow ratio is defined as the ratio of flow index to melt index.

The cyclohexane extraction rate was determined by measuring the percent of extracted ethylene polymer sample by refluxing cyclohexane after 18 hours. Cyclohexane extraction rate values indicate the amount of low molecular weight polymer formed with a particular catalyst.

Claims (1)

As described above, ethylene is characterized by the use of a silyl chromate salt of the following formula as a catalyst, pre-heated to a temperature of 500-1000 ° C. and deposited on a high surface area silica carrier containing aluminum and titanium. Single polymerization and copolymerization method of ethylene and alpha-olefins.

R is a hydrocarbyl group containing 1-14 carbon atoms.