CN108794668A - Silica-gel carrier and loaded catalyst and preparation method thereof - Google Patents
Silica-gel carrier and loaded catalyst and preparation method thereof Download PDFInfo
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- CN108794668A CN108794668A CN201710312575.0A CN201710312575A CN108794668A CN 108794668 A CN108794668 A CN 108794668A CN 201710312575 A CN201710312575 A CN 201710312575A CN 108794668 A CN108794668 A CN 108794668A
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F110/00—Homopolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F110/02—Ethene
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F4/00—Polymerisation catalysts
- C08F4/02—Carriers therefor
- C08F4/025—Metal oxides
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F4/00—Polymerisation catalysts
- C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
- C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
- C08F4/60—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
- C08F4/62—Refractory metals or compounds thereof
- C08F4/64—Titanium, zirconium, hafnium or compounds thereof
- C08F4/646—Catalysts comprising at least two different metals, in metallic form or as compounds thereof, in addition to the component covered by group C08F4/64
- C08F4/6465—Catalysts comprising at least two different metals, in metallic form or as compounds thereof, in addition to the component covered by group C08F4/64 containing silicium
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Abstract
The present invention relates to catalyst field, the silica-gel carrier for disclosing a kind of preparation method of silica-gel carrier and being prepared by this method, a kind of loaded catalyst, a kind of preparation method of loaded catalyst and the loaded catalyst being prepared by this method.The preparation method of the silica-gel carrier includes：(1) waterglass, polyalcohol, n-butanol and inorganic acid are mixed, and gained mixture after contact is filtered and/or carrying out washing treatment using purpose ceramic-film filter, obtain silica gel filter cake；(2) the silica gel filter cake for obtaining step (1) carries out ball milling, is then spray-dried, obtains silica-gel carrier.There is higher catalytic activity after silica-gel carrier load polyethylene catalysts using the present invention, obtained polyethylene product heap density and melt index are relatively low.
Description
Technical field
The present invention relates to catalyst fields, and in particular, to a kind of preparation method of silica-gel carrier and is prepared by this method
Obtained silica-gel carrier, a kind of loaded catalyst and are prepared a kind of preparation method of loaded catalyst by this method
Loaded catalyst.
Background technology
The development and application of polyethylene catalysts are the olefinic polymerization catalysis after traditional Ziegler-Natta catalyst
The another important breakthrough in agent field, this makes the research of polyethylene catalysts enter the stage of a fast development.Due to
The catalyst amount that homogeneous polyethylene catalyst reaches needed for high activity is big, and production cost is high, and obtained polymer is without grain
Shape can not use on widely used slurry process or gas phase polymerization technique, and it is exactly handle to overcome the effective way of the above problem
Soluble poly catalyst for ethylene carries out supported processing.
Catalyst carrier common at present is mesoporous material and silica-gel carrier.Wherein, silica-gel carrier is urged in load polyethylene
Catalytic activity after agent is not high enough, there is an urgent need for developing one kind to improve active catalyst carrier, to push carried catalyst
With the further development of polyolefin industry.
Invention content
The silica-gel carrier obtained the present invention provides a kind of preparation method of silica-gel carrier and by this method.
Current silica gel removes impurity usually using plate and frame type filter-press, but is existed using the silica-gel carrier that this method obtains
Catalytic activity after supported catalyst is relatively low, it may be possible to due to impurity removal not enough thoroughly.In addition, plate and frame type filter-press is also deposited
In shortcomings, for example, plate and frame type filter-press floor space is larger, simultaneously as plate and frame type filter-press runs for discontinuous, effect
Rate is low, and operation room environment is poor, there is secondary pollution, further, since using filter cloth, removal impurity effect is poor, and waste water can not
Regeneration extremely wastes water source in washing process, simultaneously because discharge waste water can not be handled, and causes environmental pollution and two
Secondary waste.And the present inventor has found after further investigation, and when being filtered processing to silica gel using ceramic membrane, institute
Obtained silica-gel carrier has higher catalytic activity, obtained polyethylene product heap density after loading polyethylene catalysts
It is relatively low with melt index.The present inventor is based on above-mentioned discovery, completes the present invention.
Specifically, in a first aspect, the present invention provides a kind of preparation method of silica-gel carrier, this method includes：
(1) waterglass, polyalcohol and inorganic acid are mixed, and gained mixture after contact is used into ceramic membrane
Filter is filtered and/or carrying out washing treatment, obtains silica gel filter cake；
(2) the silica gel filter cake for obtaining step (1) carries out ball milling, is then spray-dried, obtains silica-gel carrier.
Second aspect, the present invention provides the silica-gel carriers being prepared by the above method.
The third aspect, the present invention provides a kind of loaded catalyst, which contains silica-gel carrier and is supported on
Magnesium salts on the silica-gel carrier and/or titanium salt, wherein the silica-gel carrier is the silica-gel carrier that aforementioned present invention provides.
Fourth aspect, the present invention provides a kind of preparation method of loaded catalyst, this method includes：In inert gas
In the presence of, silica-gel carrier is contacted with the mother liquor containing magnesium salts and/or titanium salt；Wherein, the silica-gel carrier is aforementioned present invention
The silica-gel carrier of offer.
5th aspect, the present invention provides the loaded catalysts being prepared by the above method.
The method of ceramic membrane filter using the present invention prepares silica-gel carrier, has the following advantages：(1) separation process letter
Single, separative efficiency is high, and corollary apparatus is few, and low energy consumption, and operation operating is easy；(2) cross-flow filtration is used, higher film surface stream is used
Speed reduces accumulation of the pollutant in film surface, improves membrane flux；(3) chemical stability of ceramic membrane is good, and acid-fast alkali-proof is resistance to
Organic solvent, power of regeneration is strong, can be suitable for the preparation process of silica-gel carrier；(4) waste liquid yield significantly reduces, green ring
It protects.
Silica-gel carrier prepared by method using the present invention has large aperture and high-specific surface area, is conducive to catalyst component
Load；In addition, there is the silica-gel carrier spherical geometric shape, the shape to reduce the sides such as powder reuniting, improvement mobility
Mask has a clear superiority.The silica-gel carrier prepared using the present invention, it is anti-in catalyzed ethylene polymerization to be prepared loaded catalyst
There should be higher catalytic activity in the process, and the lower polyethylene product of heap density and melt index, institute can be obtained
It is spherical and uniform particle sizes to obtain polyethylene product.
Other features and advantages of the present invention will be described in detail in subsequent specific embodiment part.
Description of the drawings
Fig. 1 is the SEM scanning electron microscope (SEM) photographs of the microscopic appearance of silica-gel carrier A1 in embodiment 1；
Fig. 2 is the SEM scanning electron microscope (SEM) photographs of the microscopic appearance of loaded catalyst B1 in embodiment 1；
Fig. 3 is the graph of pore diameter distribution of silica-gel carrier A1 in embodiment 1；
Fig. 4 is the SEM scanning electron microscope (SEM) photographs of the microscopic appearance of polyethylene particle in EXPERIMENTAL EXAMPLE 1.
Specific implementation mode
The endpoint of disclosed range and any value are not limited to the accurate range or value herein, these ranges or
Value should be understood as comprising the value close to these ranges or value.For numberical range, between the endpoint value of each range, respectively
It can be combined with each other between the endpoint value of a range and individual point value, and individually between point value and obtain one or more
New numberical range, these numberical ranges should be considered as specific open herein.
The present invention provides a kind of preparation method of silica-gel carrier, this method includes：(1) by waterglass, polyalcohol and nothing
Machine acid is mixed, and gained mixture after contact is filtered and/or carrying out washing treatment using purpose ceramic-film filter, is obtained
To silica gel filter cake；
(2) the silica gel filter cake for obtaining step (1) carries out ball milling, is then spray-dried, obtains silica-gel carrier.
According to the present invention, in step (1), the dosage of the waterglass, polyalcohol and inorganic acid can be this field
Conventional selection, for example, the weight ratio of the waterglass, inorganic acid and polyalcohol dosage can be 3-6：0.5-4：1, preferably 3-
6：1-3：1.The dosage of the inorganic acid so that the pH value being mixed in step (1) is 2-4.
In the present invention, the waterglass typically refers to the aqueous solution of sodium metasilicate, and concentration can be 10-50 weight %,
Preferably 12-30 weight %.In dosage ratio, waterglass in terms of the weight of the aqueous solution of sodium metasilicate, i.e., wherein includes water
Weight.The inorganic acid can be various inorganic acids commonly used in the art, for example, can be sulfuric acid, nitric acid, hydrochloric acid and hydrogen
It is one or more in bromic acid.The inorganic acid uses preferably in the form of the aqueous solution of 3-20 weight %.In dosage ratio, nothing
Machine acid wherein includes the weight of water in terms of the weight of its aqueous solution.
In the present invention, there is no particular limitation for the type of the polyalcohol, such as can be glycerine and/or second two
Alcohol, preferably glycerine.
There is no particular limitation to the condition being mixed in step (1) by the present invention, can be the conventional choosing of this field
It selects.For example, the condition being mixed includes：Temperature can be 10-60 DEG C, and the time can be 1-5 hours, and pH value can be
2-4.In order to be more advantageous to the uniform mixing between each substance, the process being mixed preferably carries out under agitation.
In the present invention, ceramic filter is to be by a kind of collection filtering of core, deslagging, cleaning and regeneration of ceramic membrane element
The gas, liquid, solid separation of one and purifier.The purpose ceramic-film filter may include ceramic film component and ceramic membrane element,
The ceramic membrane element can be inorganic ceramic membrane element (referred to as inorganic ceramic membrane).Inorganic ceramic membrane typically refers to aoxidize
Aluminium, titanium oxide, zirconium oxide etc. through made of high temperature sintering with porous structure high technology ceramics filtering material, porous support layer,
Transition zone and microporous film layers are in asymmetric distribution, and filtering accuracy covers micro-filtration, ultrafiltration, nanofiltration.Ceramic membrane filter is a kind of " cross-flow
The fluid separation process of filtering " form：Material liquid flow at high speed in membrane tube, the driven by pressure clarification containing small molecule component
Penetrating fluid penetrates film outward along direction normal thereto, and the muddy concentrate containing macromolecular components is rejected by, to make fluid reach
To the purpose of separation, concentration, purifying.The ceramic membrane can be commercially available, such as can be purchased from Jiangsu my high-tech long
The inorganic ceramic membrane component of skill limited liability company, The concrete specification can be selected according to actual conditions.Ceramic film component can
To be determined according to the concrete condition of ceramic membrane element and sample to be treated.
According to a kind of specific embodiment, the parameter of inorganic ceramic membrane component used herein includes：Membrane material is
Aluminium oxide, shape are that multichannel is cylindrical, channel number 19, channel diameter 4mm, length 1016mm, outer diameter (diameter)
For 30mm, effective membrane area is 0.24m2。
In the present invention, described to be filtered using purpose ceramic-film filter and/or the condition of carrying out washing treatment includes：Operation pressure
Power can be 2.5-3.9bar, preferably 3-3.5bar；Circulation side into film pressure can be 3-5bar, preferably 3.5-
4.5bar；It can be 2-2.8bar, preferably 2.2-2.6bar that circulation side, which goes out film pressure,；Circulation side crossflow velocity can be 4-
5m/s, preferably 4-4.5m/s；Osmotic lateral pressure is 0.3-0.5bar；Temperature can be 10-60 DEG C.Wherein, operating pressure is
Circulation side goes out the average value of film pressure into film pressure and circulation side.
The present invention can using ceramic membrane to step (1) in be mixed after product handle before can be advanced
Row filters or filtering, and water and/or alcohol (such as ethyl alcohol) is then used to be carried out to the filter cake that suction filtration obtains in purpose ceramic-film filter
Carrying out washing treatment directly can also be filtered and be washed using purpose ceramic-film filter to the product after being mixed in step (1)
Wash processing.
Carrying out washing treatment can use water and/or alcohol (such as ethyl alcohol) to carry out.A kind of preferred embodiment party according to the present invention
Formula, when the sodium ions content in the cleaning solution for detecting purpose ceramic-film filter is 0.02 weight % or less, you can stop filtering,
Obtain silica gel filter cake.
According to the present invention, in step (2), there is no particular limitation for the condition and concrete operation method of ball milling, Ke Yiwei
The conventional selection of this field.For example, the ball milling can carry out in the ball mill, the inner wall of ball grinder is preferred in the ball mill
For polytetrafluoroethyllining lining, the diameter of the abrading-ball in ball mill can be 2-3mm；The quantity of abrading-ball can be according to the big of ball grinder
It is small reasonably to be selected, for the ball grinder that size is 50-150ml, it can usually use 1 abrading-ball；The material of the abrading-ball
Matter can be agate, polytetrafluoroethylene (PTFE) etc., preferably agate.The condition of the ball milling may include：The rotating speed of abrading-ball can be
300-500r/min, the temperature in ball grinder can be 15-100 DEG C, and the time of ball milling can be 0.1-100 hours.
According to the present invention, in step (2), the spray drying can be implemented according to conventional methods.Pressure can be selected from
At least one of gentle flow type spray seasoning of spray drying process, centrifugal spray drying method.According to of the invention a kind of preferred
Embodiment, the spray drying use centrifugal spray drying method.The spray drying can carry out in atomizer.The spray
Mist drying condition may include：Temperature is 100-300 DEG C, rotating speed 10000-15000r/min；Under preferable case, the spray
Mist drying condition include：Temperature is 150-250 DEG C, and the rotating speed of rotation is 11000-13000r/min.
In the preparation method of silica-gel carrier in the prior art, the removed template method after spray drying is also typically included
Step, such as pass through calcination method removed template method.Since the method for the present invention is filtered and/or washup using ceramic membrane
Reason, so it can not include the steps that calcining removed template method that the present invention, which is prepared in the method for silica-gel carrier,.
The present invention also provides the silica-gel carriers being prepared by the above method.
In the present invention, the average grain diameter of the silica-gel carrier is 30-60 μm, specific surface area 150-600m2/ g, hole body
Product is 0.5-2.5mL/g, aperture 5-25nm.
Under preferable case, the average grain diameter of the silica-gel carrier is 30-60 μm, specific surface area 200-400m2/ g, hole body
Product is 1-2mL/g, aperture 10-25nm.
In the present invention, the specific surface area, pore volume and aperture are measured according to nitrogen adsorption methods, and the average grain diameter is adopted
It is measured with laser fineness gage.The average grain diameter is average particle diameter.
The present invention also provides a kind of loaded catalyst, which contains silica-gel carrier and is supported on the silica gel
Magnesium salts on carrier and/or titanium salt, the silica-gel carrier are silica-gel carrier provided by the invention.
According to the present invention, silica-gel carrier in the loaded catalyst and the magnesium salts being supported on the silica-gel carrier
And/or the content of titanium salt can change in wide range.For example, on the basis of the total weight of the catalyst, with oxide
The sum of the magnesium elements of meter and the content of titanium elements can be 1-50 weight %, preferably 1-15 weight %；The silica-gel carrier
Content can be 50-99 weight %, preferably 85-99 weight %.
According to a preferred embodiment of the present invention, the dosage weight ratio of the magnesium salts and titanium salt is 1：0.1-2, it is excellent
It is selected as 1：0.5-2.
In the present invention, there is no particular limitation for the type of the magnesium salts and titanium salt, can be the conventional selection of this field.
For example, the magnesium salts can be one or more in magnesium chloride, magnesium sulfate, magnesium nitrate and magnesium bromide, preferably magnesium chloride；Institute
It can be titanium tetrachloride and/or titanium trichloride to state titanium salt.
In the present invention, the survey of X-ray fluorescence spectra analytic approach may be used in the content of each element in the catalytic component
?.
In the present invention, the loaded catalyst can be prepared according to various methods commonly used in the art, as long as
Magnesium salts and/or titanium salt are loaded on the silica-gel carrier.
The present invention also provides a kind of preparation method of loaded catalyst, this method includes：In the presence of an inert gas,
Silica-gel carrier is contacted with the mother liquor containing magnesium salts and/or titanium salt；Wherein, the silica-gel carrier is above-mentioned silicon provided by the invention
Glue carrier.
In the present invention, the mother liquor containing magnesium salts and/or titanium salt can be organic molten containing magnesium salts and/or titanium salt
Agent, the organic solvent can be isopropanol and tetrahydrofuran, and the volume ratio of tetrahydrofuran and isopropanol can be 1：1-3,
Preferably 1：1-1.5.
In the preparation process of the catalyst, the dosage of the magnesium salts and the titanium salt is preferably relative to silica-gel carrier
It is excessive.For example, the magnesium salts, the titanium salt and the dosage of the silica-gel carrier make in the loaded catalyst being prepared,
On the basis of the total weight of the catalyst, the sum of content of magnesium elements and titanium elements in terms of oxide is 1-50 weight %,
Preferably 1-15 weight %；The content of the silica-gel carrier is 50-99 weight %, preferably 85-99 weight %.
Preferably, the condition that the silica-gel carrier is contacted with the mother liquor containing magnesium salts and/or titanium salt includes：Temperature is 25-
100 DEG C, preferably 40-75 DEG C；Time is 0.1-5h, preferably 1-4h.
In the present invention, the preparation method of the loaded catalyst further includes：Silica-gel carrier with containing magnesium salts and/or
After the mother liquor contact of titanium salt, there is the silica-gel carrier of magnesium salts and/or titanium salt to be filtered and dry load.The item of the drying
Part is not particularly limited, and can be the conventional drying mode and condition of this field.It is preferred that the preparation of loaded catalyst is also
Process of lapping including washing process after filtration and before the drying, and/or after drying.Those skilled in the art
The condition of the washing and grinding can be selected according to practice situation, details are not described herein.
In the present invention, the inert gas is the gas not reacted with raw material and product, such as can be ability
At least one of group 0 element gas, preferably nitrogen in the nitrogen or the periodic table of elements of domain routine.
The present invention also provides the loaded catalysts prepared by the above method.
The present invention will be described in detail by way of examples below.
In following embodiment and comparative example,
Used purpose ceramic-film filter is that the number purchased from Jiangsu Jiuwu High-Tech Co., Ltd. is JWCM19*30
Inorganic ceramic membrane component and filling membrane area be 0.5m2Ceramic film component；The parameter of inorganic ceramic membrane component includes：Shape
Shape is that multichannel is cylindrical, channel number 19, channel diameter 4mm, length 1016mm, and outer diameter (diameter) is 30mm.
Scanning electron microscope analysis carries out in the scanning electron microscope purchased from the model XL-30 of FEI Co. of the U.S.；Kong Jie
Structure Parameter analysis carries out on the nitrogen adsorption desorption instrument of the model Autosorb-1 purchased from Kang Ta companies of the U.S., wherein carries out
Before test, sample is deaerated 4 hours at 200 DEG C；Model Axios-Advanced of the x-ray fluorescence analysis in dutch company
X-ray fluorescence analyzer on carry out；Size distribution curve is measured by Malvern laser particle analyzer.
The heap density of polyolefine powder is measured using method as defined in GB/T 1636-2008.
Melt index：It is measured according to ASTM D1238-99.
Embodiment 1
The present embodiment is used to illustrate silica-gel carrier and loaded catalyst of the present invention and preparation method thereof
(1) silica-gel carrier is prepared
By the waterglass of a concentration of 15 weight %, the sulfuric acid solution of a concentration of 12 weight % and glycerine with weight ratio for 5：
1：1 carries out mixing and haptoreaction 1.5 hours at 20 DEG C, then adjusts pH value to 3, so with the sulfuric acid of a concentration of 98 weight %
Obtained reaction mass is filtered afterwards, it is that 0.02 weight % obtains silicon to be used in combination purpose ceramic-film filter to wash to sodium ions content
Glue filter cake.Wherein, membrane module operating pressure is 3.3bar, and circulation side is 4bar into film pressure, and circulation side goes out film pressure and is
2.5bar, circulation side crossflow velocity are 4m/s, and osmotic lateral pressure 0.3bar, temperature is 20 DEG C.Obtain parts by weight silica gel filter
Cake uses the washings of three parts by weight.
The above-mentioned silica gel filter cake of 10g is put into the ball grinder of 100ml, wherein the material of ball grinder is polytetrafluoroethylene (PTFE),
Material quality of grinding balls is agate, and a diameter of 3mm of abrading-ball, quantity is 1, rotating speed 400r/min.Ball grinder is closed, in ball grinder
Temperature is ball milling 5h at 60 DEG C, and the slurry after ball milling is spray-dried at 200 DEG C in the case where rotating speed is 12000r/min, obtains target
Silica-gel carrier A1.
(2) loaded catalyst is prepared
In N2Under protection, by the MgCl of 1g2With the TiCl of 1g4It is dissolved in the tetrahydrofuran of 500mL and the double solvents of isopropanol
(volume ratio of tetrahydrofuran and isopropanol is 1：1.2) in, the catalyst mother liquor of element containing Mg and Ti elements is formed.Then 75
The above-mentioned silica-gel carrier A1 of 1g are added at DEG C and impregnate 4h.It after being cooled to room temperature, is then filtered, solid production is obtained after removing liquid
Object is used in combination tetrahydrofuran to wash solid product repeatedly 4 times, and obtained solid product is finally dried in vacuo to 4h at 75 DEG C, is obtained
Powdery loaded catalyst B1 with good flow performance.
Silica-gel carrier A1 is characterized with scanning electron microscope and nitrogen adsorption instrument, with scanning electron microscope to loaded catalyst B1
It is characterized.
Fig. 1 is the SEM scanning electron microscope (SEM) photographs of the microscopic appearance of silica-gel carrier A1, from figure 1 it appears that silica-gel carrier A1
Microscopic appearance is the microballoon that grain size is 30-60 μm, and its good dispersion property.
Fig. 2 is the SEM scanning electron microscope (SEM) photographs of the microscopic appearance of loaded catalyst B1, from figure 2 it can be seen that support type is urged
The microscopic appearance of agent B1 is the microballoon that grain size is 30-60 μm, and its good dispersion property.
Fig. 3 is the graph of pore diameter distribution of silica-gel carrier A1.It can be seen from the figure that silica-gel carrier A1 has single hole arrangements.
The pore structure parameter of silica-gel carrier A1 is as shown in table 1 below.
Table 1
It is obtained by x-ray fluorescence analysis, in the obtained catalyst B1 of the present embodiment, the magnesium elements in terms of oxide
Content be 1.89 weight %, the contents of the titanium elements in terms of oxide is 1.19 weight %, and content of Cl element is 10.28 weights
Measure %.
Embodiment 2
The present embodiment is used to illustrate silica-gel carrier and loaded catalyst of the present invention and preparation method thereof
(1) silica-gel carrier is prepared
By the waterglass of a concentration of 15 weight %, the sulfuric acid solution of a concentration of 12 weight % and glycerine with weight ratio for 6：
3：1 carries out mixing and haptoreaction 3 hours at 60 DEG C, then adjusts pH value to 3, then with the sulfuric acid of a concentration of 98 weight %
Obtained reaction mass is filtered, it is that 0.02 weight % obtains silica gel to be used in combination purpose ceramic-film filter to wash to sodium ions content
Filter cake.Wherein, membrane module operating pressure is 3bar, and circulation side is 3.5bar into film pressure, and it is 2.5bar that circulation side, which goes out film pressure,
Circulation side crossflow velocity is 4.5m/s, and osmotic lateral pressure 0.4bar, temperature is 60 DEG C.Obtain parts by weight silica gel filter cake use
The washings of three parts by weight.
The above-mentioned silica gel filter cake of 10g is put into the ball grinder of 100ml, wherein the material of ball grinder is polytetrafluoroethylene (PTFE),
Material quality of grinding balls is agate, and a diameter of 3mm of abrading-ball, quantity is 1, rotating speed 300r/min.Ball grinder is closed, in ball grinder
Temperature is that for 24 hours, the slurry after ball milling is spray-dried at 150 DEG C in the case where rotating speed is 13000r/min ball milling, obtains mesh at 30 DEG C
Mark silica-gel carrier A2.
(2) loaded catalyst is prepared
In N2Under protection, by the MgCl of 1g2With the TiCl of 2g4It is dissolved in the tetrahydrofuran of 500mL and the double solvents of isopropanol
(volume ratio of tetrahydrofuran and isopropanol is 1：1.5) in, the catalyst mother liquor of element containing Mg and Ti elements is formed.Then 60
The above-mentioned silica-gel carrier A2 of 1g are added at DEG C and impregnate 1h.It after being cooled to room temperature, is then filtered, solid production is obtained after removing liquid
Object is used in combination tetrahydrofuran to wash solid product repeatedly 4 times, and obtained solid product is finally dried in vacuo to 4h at 75 DEG C, is obtained
Powdery loaded catalyst B2 with good flow performance.
The pore structure parameter of silica-gel carrier A2 is as shown in table 2 below.
Table 2
It is obtained by x-ray fluorescence analysis, in the obtained catalyst B2 of the present embodiment, the magnesium elements in terms of oxide
Content be 1.55 weight %, the contents of the titanium elements in terms of oxide is 1.09 weight %, and content of Cl element is 10.2 weights
Measure %.
Embodiment 3
The present embodiment is used to illustrate silica-gel carrier and loaded catalyst of the present invention and preparation method thereof
(1) silica-gel carrier is prepared
It is with weight ratio by the sulfuric acid solution and glycerine of the waterglass of a concentration of 15 weight % and a concentration of 12 weight %
3：2：1 carries out mixing and haptoreaction 1 hour at 40 DEG C, then adjusts pH value to 3, so with the sulfuric acid of a concentration of 98 weight %
Obtained reaction mass is filtered afterwards, it is that 0.02 weight % obtains silicon to be used in combination purpose ceramic-film filter to wash to sodium ions content
Glue filter cake.Wherein, membrane module operating pressure is 3.4bar, and circulation side is 4.5bar into film pressure, and circulation side goes out film pressure and is
2.3bar, circulation side crossflow velocity are 4.2m/s, and osmotic lateral pressure 0.5bar, temperature is 40 DEG C.Wherein, a parts by weight are obtained
Silica gel filter cake uses the washings of three parts by weight.
The above-mentioned silica gel filter cake of 10g is put into the ball grinder of 100ml, wherein the material of ball grinder is polytetrafluoroethylene (PTFE),
Material quality of grinding balls is agate, and a diameter of 3mm of abrading-ball, quantity is 1, rotating speed 300r/min.Ball grinder is closed, in ball grinder
Temperature is ball milling 10h at 50 DEG C, and the slurry after ball milling is spray-dried at 250 DEG C in the case where rotating speed is 11000r/min, obtains mesh
Mark silica-gel carrier A3.
(2) loaded catalyst is prepared
In N2Under protection, by the MgCl of 2g2With the TiCl of 1g4It is dissolved in the tetrahydrofuran of 500mL and the double solvents of isopropanol
(volume ratio of tetrahydrofuran and isopropanol is 1：1) in, the catalyst mother liquor of element containing Mg and Ti elements is formed.Then at 40 DEG C
The lower above-mentioned silica-gel carrier A2 of addition 1g impregnate 2h.It after being cooled to room temperature, is then filtered, solid production is obtained after removing liquid
Object is used in combination tetrahydrofuran to wash solid product repeatedly 4 times, and obtained solid product is finally dried in vacuo to 4h at 75 DEG C, is obtained
Powdery loaded catalyst B3 with good flow performance.
The pore structure parameter of silica-gel carrier A3 is as shown in table 3 below.
Table 3
It is obtained by x-ray fluorescence analysis, in the obtained catalyst B3 of the present embodiment, the magnesium elements in terms of oxide
Content be 1.79 weight %, the contents of the titanium elements in terms of oxide is 1.05 weight %, and content of Cl element is 10.11 weights
Measure %.
Comparative example 1
This comparative example is used to illustrate the preparation method of the silica-gel carrier and loaded catalyst of reference
(1) silica-gel carrier is prepared
It is with weight ratio by the sulfuric acid solution and glycerine of the waterglass of a concentration of 15 weight % and a concentration of 12 weight %
5：1：1 carries out mixing and haptoreaction 1.5 hours at 20 DEG C, then with the sulfuric acid of a concentration of 98 weight % adjustment pH value to 3,
Then obtained reaction mass is handled using plate and frame type filter-press, it is 0.02 weight to be then washed with water to sodium ions content
% is measured, silica gel filter cake is obtained.Prepare silica gel filter cake consumption 11 parts by weight of water of a parts by weight.
The above-mentioned silica gel filter cake of 10g is put into the ball grinder of 100ml, wherein the material of ball grinder is polytetrafluoroethylene (PTFE),
Material quality of grinding balls is agate, and a diameter of 3mm of abrading-ball, quantity is 1, rotating speed 400r/min.Ball grinder is closed, in ball grinder
Temperature is ball milling 5h at 60 DEG C, and the slurry after ball milling is spray-dried at 200 DEG C in the case where rotating speed is 12000r/min, and spraying is dry
The product obtained after dry calcines 10h in nitrogen atmosphere in Muffle furnace at 400 DEG C, with eliminating hydroxide and residual moisture, obtains
Silica-gel carrier DA1.
(2) loaded catalyst is prepared
It is carried out according to the method for embodiment 1, unlike, silica-gel carrier A1 is replaced with into above-mentioned silica-gel carrier DA1, is obtained
Loaded catalyst DB1.
It is obtained by x-ray fluorescence analysis, in obtained catalyst DB1, the content of the magnesium elements in terms of oxide is
The content of 1.1 weight %, the titanium elements in terms of oxide are 1.6 weight %, and content of Cl element is 18.63 weight %.
Comparative example 2
This comparative example is used to illustrate the preparation method of the silica-gel carrier and catalyst of reference
(1) silica-gel carrier is prepared
Commercially available ES955 silica gel (GRACE companies) is calcined 10 hours for 400 DEG C under nitrogen protection, with eliminating hydroxide and
Residual water, to obtain the ES955 silica gel through thermal activation.
(2) loaded catalyst is prepared
Loaded catalyst is prepared according to the method for embodiment 1, unlike, it is living that silica-gel carrier A1 is replaced with into above-mentioned heat
The ES955 silica gel of change, obtains loaded catalyst DB2.
It is obtained by x-ray fluorescence analysis, in obtained catalyst DB2, the content of the magnesium elements in terms of oxide is
The content of 1.8 weight %, the titanium elements in terms of oxide are 1.2 weight %, and content of Cl element is 6.8 weight %.
EXPERIMENTAL EXAMPLE 1
This EXPERIMENTAL EXAMPLE is used to illustrate the application of loaded catalyst provided by the invention.
In the stainless steel polymerization autoclave of 2L, with nitrogen and ethylene, respectively three times, 200mL hexanes are then added in displacement, will
Kettle temperature rises to 80 DEG C, adds 800mL hexanes, and with the addition of hexane, the triethyl aluminum of a concentration of 1mol/L of 2mL is added
(TEA) hexane solution is subsequently added into the catalytic component B1 of 0.5g, is passed through ethylene gas, pressure is risen to 1.0MPa and is tieed up
It holds as 1.0MPa, separation is filtered after being reacted 1 hour at 70 DEG C, obtains polyethylene particle powder.Gained polyethylene particle powder
Heap density (BD), melt index MI2.16And the efficiency of catalyst is listed in Table 4 below.
Obtained polyethylene particle is characterized with scanning electron microscope.Fig. 4 is that the SEM of the microscopic appearance of polyethylene particle is swept
Retouch electron microscope.Figure 4, it is seen that gained polyethylene product particle is spherical shape, average grain diameter is 30-60 μm.
EXPERIMENTAL EXAMPLE 2
This EXPERIMENTAL EXAMPLE is used to illustrate the application of loaded catalyst provided by the invention.
In the stainless steel polymerization autoclave of 2L, with nitrogen and ethylene, respectively three times, 200mL hexanes are then added in displacement, will
Kettle temperature rises to 75 DEG C, adds 900mL hexanes, and with the addition of hexane, the triethyl aluminum of a concentration of 1mol/L of 2mL is added
(TEA) hexane solution is subsequently added into the catalytic component B2 of 0.1g, is passed through ethylene gas, pressure is risen to 1MPa and is maintained
For 1MPa, separation is filtered after being reacted 1.5 hours at 75 DEG C, obtains polyethylene particle powder.The heap of gained polyethylene particle powder
Density (BD), melt index MI2.16And the efficiency of catalyst is listed in Table 4 below.
EXPERIMENTAL EXAMPLE 3
This EXPERIMENTAL EXAMPLE is used to illustrate the application of loaded catalyst provided by the invention.
In the stainless steel polymerization autoclave of 2L, with nitrogen and ethylene, respectively three times, 200mL hexanes are then added in displacement, will
Kettle temperature rises to 85 DEG C, adds 700mL hexanes, and with the addition of hexane, the triethyl aluminum of a concentration of 1mol/L of 2mL is added
(TEA) hexane solution is subsequently added into the catalytic component B3 of 1g, is passed through ethylene gas, pressure is risen to 1MPa and is maintained
1MPa filters separation, obtains polyethylene particle powder after being reacted 2 hours at 85 DEG C.The heap density of gained polyethylene particle powder
(BD), melt index MI2.16And the efficiency of catalyst is listed in Table 4 below.
Experimental comparison's example 1-2
The application of loaded catalyst of this Experimental comparison example for illustrating reference
The polymerization of ethylene is carried out according to the method for EXPERIMENTAL EXAMPLE 1, unlike, the comparison of identical weight part is respectively adopted
Comparative catalyst DB1 and DB2 prepared by example 1 and 2 replaces the catalyst B1 being prepared by embodiment 1.Gained polyethylene particle
The heap density (BD) of powder, melt index MI2.16And the efficiency of catalyst is listed in Table 4 below.
Table 4
Method using the present invention, which is can be seen that, from the result of embodiment 1-3 and comparative example 1 prepares silica-gel carrier, water consumption
Amount is few, and the waste water of generation is few.After spray drying can direct supported catalyst, calcination process need not be carried out, simplify system
Standby technique.
Method using the present invention is can be seen that from the result of EXPERIMENTAL EXAMPLE 1-3 and Experimental comparison's example 1-2 to be prepared
The polyethylene catalysts that prepare of silica-gel carrier, catalytic activity is high, can obtain the lower spherical shape of heap density and melt index
Polyethylene product.
The preferred embodiment of the present invention has been described above in detail, and still, the present invention is not limited thereto.In the skill of the present invention
In art conception range, technical scheme of the present invention can be carried out a variety of simple variants, including each technical characteristic with it is any its
Its suitable method is combined, and it should also be regarded as the disclosure of the present invention for these simple variants and combination, belongs to
Protection scope of the present invention.
Claims (10)
1. a kind of preparation method of silica-gel carrier, which is characterized in that this method includes：
(1) waterglass, polyalcohol and inorganic acid are mixed, and gained mixture after contact is used into ceramic membrane filter
Device is filtered and/or carrying out washing treatment, obtains silica gel filter cake；
(2) the silica gel filter cake for obtaining step (1) carries out ball milling, is then spray-dried, obtains silica-gel carrier.
2. preparation method according to claim 1, wherein be filtered using purpose ceramic-film filter and/or carrying out washing treatment
Condition include：Operating pressure is 2.5-3.9bar, and circulation side is 3-5bar into film pressure, and it is 2- that circulation side, which goes out film pressure,
2.8bar, circulation side crossflow velocity are 4-5m/s；Osmotic lateral pressure is 0.3-0.5bar；Temperature is 10-60 DEG C.
3. preparation method according to claim 1, wherein in step (1), the waterglass, inorganic acid and polyalcohol
Dosage weight ratio be 3-6：0.5-4：1, the dosage of the inorganic acid so that the pH value being mixed in step (1) is 2-
4；
Preferably, the condition being mixed in step (1) includes：Temperature is 10-60 DEG C, and the time is 1-5 hours, pH value 2-4；
Preferably, in step (2), the condition of the ball milling includes：The rotating speed of abrading-ball is 300-500r/min, in ball grinder
Temperature is 15-100 DEG C, and the time of ball milling is 0.1-100h；
Preferably, the condition of the spray drying includes：Temperature is 100-300 DEG C, rotating speed 10000-15000r/min.
4. the silica-gel carrier being prepared by the preparation method described in any one of claim 1-3.
5. silica-gel carrier according to claim 4, wherein the average grain diameter of the silica-gel carrier is 30-60 μm, specific surface
Product is 150-600m2/ g, pore volume 0.5-2.5mL/g, aperture 5-25nm；
Preferably, the average grain diameter of the silica-gel carrier is 30-60 μm, specific surface area 200-400m2/ g, pore volume 1-
2mL/g, aperture 10-25nm.
6. a kind of loaded catalyst, the catalyst contain silica-gel carrier and the magnesium salts being supported on the silica-gel carrier and/
Or titanium salt, which is characterized in that the silica-gel carrier is the silica-gel carrier described in claim 4 or 5.
7. catalyst according to claim 6, wherein on the basis of the total weight of the catalyst, in terms of oxide
The sum of content of magnesium elements and titanium elements is 1-50 weight %, preferably 1-15 weight %；The content of the silica-gel carrier is 50-
99 weight %, preferably 85-99 weight %.
8. a kind of preparation method of loaded catalyst, which is characterized in that this method includes：In the presence of an inert gas, by silicon
Glue carrier is contacted with the mother liquor containing magnesium salts and/or titanium salt；Wherein, the silica-gel carrier is the silica gel described in claim 4 or 5
Carrier.
9. according to the method described in claim 8, wherein, the magnesium salts, the titanium salt and the silica-gel carrier dosage make
In the loaded catalyst being prepared, on the basis of the total weight of the loaded catalyst, the magnesium elements in terms of oxide
It is 1-50 weight %, preferably 1-15 weight % with the sum of the content of titanium elements；The content of the silica-gel carrier is 50-99 weights
Measure %, preferably 85-99 weight %.
10. the loaded catalyst prepared by the method described in claim 8 or 9.
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| CN113637100A (en) * | 2021-09-14 | 2021-11-12 | 无锡玖汇科技有限公司 | Silica gel composite carrier with high magnesium chloride content |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB788151A (en) * | 1953-10-19 | 1957-12-23 | Du Pont | Solid siliceous materials of high surface area, methods of making the same, and compositions containing them |
| US3948673A (en) * | 1973-10-19 | 1976-04-06 | Owens-Corning Fiberglas Corporation | Water soluble sizing for glass fibers and glass fibers sized therewith |
| CN102002120A (en) * | 2010-09-20 | 2011-04-06 | 中国海洋石油总公司 | Method for preparing special silica gel carrier with large pore volume and large specific surface area |
| CN103159220A (en) * | 2011-12-15 | 2013-06-19 | 中国石油天然气股份有限公司 | Method for preparing macroporous silica gel |
| CN106467581A (en) * | 2015-08-17 | 2017-03-01 | 中国石油化工股份有限公司 | Three hole silica-gel carriers and support type polyethylene catalysts and its preparation method and application |
| CN106554431A (en) * | 2015-09-25 | 2017-04-05 | 中国石油化工股份有限公司 | The method of bimodal porous silica carrier and support type polyethylene catalysts and its preparation method and application and vinyl polymerization |
-
2017
- 2017-05-05 CN CN201710312575.0A patent/CN108794668A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB788151A (en) * | 1953-10-19 | 1957-12-23 | Du Pont | Solid siliceous materials of high surface area, methods of making the same, and compositions containing them |
| US3948673A (en) * | 1973-10-19 | 1976-04-06 | Owens-Corning Fiberglas Corporation | Water soluble sizing for glass fibers and glass fibers sized therewith |
| CN102002120A (en) * | 2010-09-20 | 2011-04-06 | 中国海洋石油总公司 | Method for preparing special silica gel carrier with large pore volume and large specific surface area |
| CN103159220A (en) * | 2011-12-15 | 2013-06-19 | 中国石油天然气股份有限公司 | Method for preparing macroporous silica gel |
| CN106467581A (en) * | 2015-08-17 | 2017-03-01 | 中国石油化工股份有限公司 | Three hole silica-gel carriers and support type polyethylene catalysts and its preparation method and application |
| CN106554431A (en) * | 2015-09-25 | 2017-04-05 | 中国石油化工股份有限公司 | The method of bimodal porous silica carrier and support type polyethylene catalysts and its preparation method and application and vinyl polymerization |
Non-Patent Citations (1)
| Title |
|---|
| 丁启圣 等: "《新型实用过滤技术》", 31 July 2011 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113637100A (en) * | 2021-09-14 | 2021-11-12 | 无锡玖汇科技有限公司 | Silica gel composite carrier with high magnesium chloride content |
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