CN1097351A - The preparation method of microspheroidal gama-alumina - Google Patents
The preparation method of microspheroidal gama-alumina Download PDFInfo
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- CN1097351A CN1097351A CN 93108631 CN93108631A CN1097351A CN 1097351 A CN1097351 A CN 1097351A CN 93108631 CN93108631 CN 93108631 CN 93108631 A CN93108631 A CN 93108631A CN 1097351 A CN1097351 A CN 1097351A
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Abstract
A kind of microspheroidal γ-Al
2O
3The preparation method of catalyst carrier is characterized in that using boehmite and the two binding agents of aluminium colloidal sol after the acidifying to prepare γ-Al
2O
3Microballoon, its preparation process comprises: boehmite and decationized Y sieve water are mixed making beating, add the hcl acidifying peptization, add the boehmite making beating again, add at last the making beating of aluminium colloidal sol, through steps such as aging, spray-drying, roastings, namely get product.Can make the γ-Al of high strength, bigger serface with the present invention
2O
3Microballoon, its abrasion index are 0.9-2.5% hour
-1, specific area is a 280-302 rice
2/ gram, pore volume is 0.20-0.28 milliliter/gram.
Description
The present invention relates to the technical field of gamma-alumina catalyst carrier, specifically about using the method for boehmite and the two adhesive preparation microspheroidal gamma-aluminas of aluminium colloidal sol after the acidifying.
Microspheroidal γ-Al
2O
3It is a kind of important petrochemical catalyst carrier.γ-the Al of preparation high strength bigger serface
2O
3Several different methods is arranged, and clear 63-17220 has reported preparation γ-Al such as Japan Patent
2O
3The method of microballoon, this method is: at first use sour peptization boehmite, use then the alkali neutralizing acid, can make the good γ-Al of scuff resistance finally by steps such as spray drying forming, roastings
2O
3Microballoon.In United States Patent (USP) 4301033, reported a kind of γ-Al of high bulk specific weight
2O
3Carrier and preparation method thereof, it is that two kinds of Al/Cl are mixed with Main Ingredients and Appearance than different aluminium colloidal sol is spherical gamma-Al
2O
3The catalyst carrier of particle, its bulk specific weight are the 0.65-0.71 grams per milliliter, and pore volume is 0.55-0.65 milliliter/gram, also has simultaneously preferably scuff resistance.
The purpose of this invention is to provide and a kind ofly prepare γ-Al with the two binding agents of boehmite after the acidifying and aluminium colloidal sol
2O
3The method of microballoon, this method combine boehmite acid adding peptisation and prepare γ-Al take aluminium colloidal sol as binding agent
2O
3The advantage of micro-sphere method has overcome its shortcoming, can make the γ-Al of high strength, bigger serface
2O
3Microballoon.Said γ-the Al of the present invention
2O
3The preparation method of microballoon, Fig. 1 is seen in its technological process, its preparation process comprises:
1, adds two kinds of boehmites: with Al
2O
3Content is 20-60m%, preferably the boehmite of 30-55m% and decationized Y sieve water mix making beating 25-35 minute, solid content is 10-15m% in the control slurries, add hcl acidifying, regulate PH to 1.5-4.0, and then the adding boehmite was pulled an oar 30-45 minute, solid content is 15-25m% in the control slurries, wherein acidifying is 0.5-1.5 with boehmite with the weight ratio of pulling an oar with boehmite, 0.8-1.2 preferably, solid content in the slurries refers to these slurries by 800 ℃ of calcinations residual solids content after 1 hour, and total addition of boehmite is with Al
2O
3The calcination base account for 90-95m% for calculating benchmark;
2, add aluminium sol adhesive: with Al
2O
3Concentration is that 21.5-23.5m%, Al/Cl weight ratio are that the aluminium colloidal sol of 1.15-1.25 joined in (1) making beating 30-60 minute, and the solid content in the control slurries is 15-25m%, and the addition of aluminium colloidal sol is with Al
2O
3The calcination base account for 5-10m% for calculating benchmark;
3, at 50-70 ℃ of aging 1-3 hour;
4, spray drying forming, the control exhaust temperature is 250-300 ℃, atomisation pressure is a 50-60 atmospheric pressure;
5, in 500-700 ℃ of roasting 1-3 hour.
The said boehmite of the present invention is a kind of alumine hydroxide colloid, and it is to add acid by sodium metaaluminate, or sodium metaaluminate adds CO
2Or sodium metaaluminate adds aluminium salt and makes, and also can add alkali by aluminium salt and make, and said acid is selected from HCl, HNO
3And H
2SO
4, said aluminium salt is selected from AlCl
3, Al(NO
3)
3, said alkali is selected from NH
3H
2O, NaOH.Boehmite can also make (as aluminium isopropoxide, aluminium butoxide, amylalcohol aluminium etc.) by the aluminium alcoholates hydrolysis.
γ-Al with the present invention's preparation
2O
3Microballoon has the following advantages:
1, production process simple, be easy to control.Production process mainly comprised for two steps, glue and moulding, as long as control the pH value of the boehmite after the acidifying well, making beating and the proportioning of acidifying usefulness boehmite and the addition of aluminium colloidal sol can obtain desirable purpose product.
2, can be according to the Liquified gas tanker of different catalysts, control γ-Al well
2O
3The anti-wear performance of microballoon, the physical propertys such as specific area and pore volume.
3, the present invention and boehmite acid adding peptisation compare, and be free from environmental pollution, can reduce spray-dired load simultaneously.Also can make high-intensity γ-Al with boehmite acid adding peptization
2O
3Microballoon, but must strengthen the consumption of acid, require HCl/Al
2O
3>7m%, a large amount of HCl overflows and causes equipment corrosion, contaminated environment when roasting like this.In addition, because the flowability problem that peptization causes, the solid content that has limited slurries can not be higher than 14m%, thereby has increased spray-dired load.
4, the present invention compares as binder method with aluminium colloidal sol, and cost is low, and is both economical.If only make binding agent with aluminium colloidal sol, also can make high-intensity γ-Al
2O
3Microballoon, but the necessary consumption that strengthens aluminium colloidal sol causes cost height, uneconomical, this method also has an outstanding shortcoming, and the granule that forms when being exactly the mixing of aluminium colloidal sol and boehmite is difficult to fragmentation with common stirring means, therefore, only make binding agent with aluminium colloidal sol, be not suitable for suitability for industrialized production.
5, the γ-Al that makes with the present invention
2O
3Microballoon, its anti-wear performance is more more advantageous than the product that makes under similarity condition with single binder method, as with boehmite acid adding peptisation, works as HCl/Al
2O
3When ratio is 3m%, the γ-Al that makes
2O
3The abrasion index of microballoon>10% hour
-1, the γ-Al that makes as binding agent with aluminium colloidal sol
2O
3Microballoon, when the addition of aluminium colloidal sol was 10m%, its abrasion index reached 10.8%/hour
-1, and the γ-Al that makes with the present invention
2O
3Microballoon, its abrasion index only has 0.9-2.5% hour
-1, can also keep bigger specific surface (280-302 rice simultaneously
2/ restrain), and pore volume (0.20-0.28 milliliter/gram).
Fig. 1 is the said γ-Al of preparation the present invention
2O
3The process chart of microballoon.Boehmite and decationized Y sieve water are mixed making beating, add hcl acidifying and carry out peptization, and then add boehmite and pull an oar, add aluminium colloidal sol and continue making beating, wear out at last, spray-drying, roasting, namely get product.
The following examples will the invention will be further described.
(1) the used analysis test method of the present invention:
1, Na
2O content: with a quantitative acetylene torch atomic absorption spectrophotometer.
2, Fe
2O
3Content: use atomic absorption spectrophotometer.
3, γ-Al
2O
3The mensuration of microballoon abrasion index: with a certain amount of γ-Al
2O
3Microballoon is put into the abrasion index determinator, ground 5 hours in the constant gas blowing down, except first hour, the fine powder sample less than 15 microns that produced in rear four hours accounts for the wear rate that is called catalyst greater than the percetage by weight of 15 microns catalyst, claim again abrasion index, unit is % hour
-1
4, γ-Al
2O
3The specific area of microballoon, pore volume are measured: low temperature ammonia absorption method.
5, the mensuration of bulk specific weight be with catalyst at the uniform velocity pour into shake in the graduated cylinder flat claim catalyst weight, and read the volume number and try to achieve.
(2) the raw materials used place of production and specification in the example of the present invention
1, boehmite: the Zhou village catalyst plant is produced, β-Al
2O
3<5m%, Na
2O<0.5m%, Fe
2O
3<0.1m%.
2, aluminium colloidal sol: the Zhou village catalyst plant is produced, Al
2O
3Content is 21.5-23.5m%, Al/Cl(m) be 1.15-1.25, Fe content is 0.025-0.07m%.
3, hydrochloric acid: technical grade, the Beijing Chemical Plant produces, concentration>31m%, Fe≤0.1m%.
4, decationized Y sieve water: running water makes the PH=2.8-3.1 of water, Na through the cation exchange column exchange
2O content<5ppm.
Example 1
In 12 kilograms of decationized Y sieve water, add 8.3 kilograms of boehmites and (contain Al
2O
334.2m%) making beating is 30 minutes, adds the technical hydrochloric acid acidifying, makes the PH=3.73 of slurries, adds 8.3 kilograms of boehmite making beating 30 minutes again, adds 1.4 kilograms of aluminium colloidal sol (Al
2O
3Content 22m%), pulled an oar 30 minutes, be heated to 60 ℃ and wore out 2 hours, spray-drying, 280 ℃ of its exhaust temperatures, 55 atmospheric pressure of atomisation pressure in 600 ℃ of roastings 2 hours, make γ-Al
2O
3Microballoon A, its raw material proportioning sees Table 1, and properties of product see Table 2.
Example 2
The preparation method, adds 14.7 kilograms of boehmites and (contains Al in 18.3 kilograms of decationized Y sieve water with example 1
2O
332.4m%) making beating is 30 minutes, adds the technical hydrochloric acid acidifying, makes slurries PH=2.67, add again 14.7 kilograms of boehmite making beating 30 minutes, add 2.3 kilograms of aluminium colloidal sols and continue making beating 30 minutes, be heated to 70 ℃ and wore out 2 hours, spray-drying in 600 ℃ of roastings 2 hours, makes γ-Al
2O
3Microballoon B, its raw material proportioning sees Table 1, and properties of product see Table 2.
Example 3
The preparation method, adds 13.2 kilograms of boehmites and (contains Al in 21.3 kilograms of decationized Y sieve water with example 1
2O
335.8m%) making beating is 30 minutes, adds the technical hydrochloric acid acidifying, makes slurries PH=3.19, adds 13.2 kilograms of boehmite making beating 30 minutes again, add 2.3 kilograms of aluminium colloidal sols, continue making beating 30 minutes, be heated to 70 ℃, left standstill aging 2 hours, spray-drying in 600 ℃ of roastings 2 hours, makes γ-Al
2O
3Microballoon C, its raw material proportioning sees Table 1, and properties of product see Table 2.
Example 4
The preparation method, adds 11.4 kilograms of boehmites and (contains Al in 24.9 kilograms of decationized Y sieve water with example 1
2O
341.6m%) making beating is 30 minutes, adds the technical hydrochloric acid acidifying, makes slurries PH=1.65, add again 11.4 kilograms of boehmite making beating 30 minutes, add 2.3 kilograms of aluminium colloidal sols and continue making beating 30 minutes, be heated to 70 ℃ and wore out 2 hours, in 600 ℃ of roastings 2 hours, make γ-Al after the spray-drying
2O
3Microballoon D, its raw material proportioning sees Table 1, and properties of product see Table 2.
Example 5
The preparation method, adds 14.7 kilograms of boehmites and (contains Al in 29 kilograms of decationized Y sieve water with example 1
2O
332.4m%) making beating is 30 minutes, adds the technical hydrochloric acid acidifying, makes slurries PH=2.7, adds 14.7 kilograms of boehmite making beating 30 minutes again, add 2.3 kilograms of aluminium colloidal sols, continue making beating 30 minutes, be heated to 60 ℃ and wore out 2 hours, after the spray-drying, in 600 ℃ of roastings 2 hours, make γ-Al
2O
3Microballoon E, its raw material proportioning sees Table 1, and properties of product see Table 2.
Example 6
The preparation method, adds 8.8 kilograms of boehmites and (contains Al in 30 kilograms of decationized Y sieve water with example 1
2O
353.9m%) making beating is 30 minutes, adds the technical hydrochloric acid acidifying, makes slurries PH=1.60, add again 8.8 kilograms of boehmite making beating 30 minutes, add 2.3 kilograms of aluminium colloidal sol making beating 30 minutes, be heated to 50 ℃ and wore out 2 hours, spray-drying in 600 ℃ of roastings 2 hours, makes γ-Al
2O
3Microballoon F, its raw material proportioning sees Table 1, and the physicochemical property of product sees Table 2.
Example 7
The preparation method, adds 9.1 kilograms of boehmites and (contains Al in 29.5 kilograms of decationized Y sieve water with example 1
2O
349m%) making beating is 30 minutes, adds the technical hydrochloric acid acidifying, makes slurries PH=1.94, add again 9.1 kilograms of boehmite making beating 30 minutes, add 2.3 kilograms of aluminium colloidal sols and continue making beating 30 minutes, be heated to 50 ℃ and wore out 2 hours, spray-drying in 600 ℃ of roastings 2 hours, makes γ-Al
2O
3Microballoon G, its raw material proportioning sees Table 1, and properties of product see Table 2.
Comparative Examples 1
Prepare γ-Al with boehmite acid adding peptisation
2O
3Microballoon.
In 16 kilograms of decationized Y sieve water, add 18 kilograms of boehmites and (contain Al
2O
328m%) making beating adds the technical hydrochloric acid acidifying, makes HCl/Al
2O
3Than being 3m%, be heated to 60 ℃ and wore out 2 hours, in 600 ℃ of roastings 2 hours, make γ-Al after the spray-drying
2O
3Microballoon H, properties of product see Table 2.
Comparative Examples 2
Prepare γ-Al take aluminium colloidal sol as binding agent
2O
3Microballoon.
In 9.0 kilograms of decationized Y sieve water, add 15.5 kilograms of boehmites and (contain Al
2O
334.5m%) making beating adds 2.7 kilograms of aluminium colloidal sols and (contains Al
2O
322.0m%) continue making beating, 60 ℃ aging 2 hours, spray-drying, 600 ℃ of roastings 2 hours make γ-Al
2O
3The microballoon I, its raw material proportioning sees Table 1, and the performance of product sees Table 2.
Can be found out the γ-Al that adopts the method for the invention to make by table 1,2
2O
3Microballoon A-G, its abrasion index only has 0.9-2.5% hour
-1, and the γ-Al that makes with boehmite acid adding peptisation
2O
3Microballoon H works as HCl/Al
2O
3Than when the 3m%, its abrasion index>10% hour
-1If, only make binding agent with aluminium colloidal sol, when the addition of aluminium colloidal sol is 10m% (with Al
2O
3The calcination base for calculating benchmark), prepared γ-Al
2O
3The abrasion index of microballoon I is 10.8% hour
-1, γ-Al that this explanation makes with the present invention
2O
3Microballoon, its anti-wear performance is more more advantageous than the same product that makes with single binding agent, can also keep bigger specific area (280-302 rice simultaneously
2/ restrain) and pore volume (0.20-0.28 milliliter/gram).
Claims (5)
1, a kind of microspheroidal γ-Al
2O
3The preparation method of catalyst carrier is characterized in that:
(1) with Al
2O
3Content is that boehmite and the decationized Y sieve water of 20-60m% mixes making beating 25-35 minute, solid content is 10-15m% in the control slurries, add hcl acidifying, regulate PH to 1.5-4.0, and then the adding boehmite was pulled an oar 30-45 minute, solid content is 15-25m% in the control slurries, and wherein acidifying is 0.5-1.5 with boehmite with the weight ratio of pulling an oar with boehmite, and total addition of boehmite is with Al
2O
3The calcination base account for 90-95m% for calculating benchmark;
(2) with Al
2O
3Concentration is 21.5-23.5m%, and the Al/Cl weight ratio is that the aluminium colloidal sol of 1.15-1.25 joins in (1), pulls an oar 30-60 minute, and the solid content in the control slurries is 15-25m%, and the addition of aluminium colloidal sol is with Al
2O
3The calcination base account for 5-10m% for calculating benchmark;
(3) at 50-70 ℃ of aging 1-3 hour;
(4) spray drying forming, the control exhaust temperature is 250-300 ℃, atomisation pressure is a 50-60 atmospheric pressure;
(5) in 500-700 ℃ of roasting 1-3 hour.
2,, it is characterized in that acidifying is 0.8-1.2 with boehmite with the weight ratio of pulling an oar with boehmite in (1) according to the said preparation method of claim 1.
3, according to the said preparation method of claim 1, it is characterized in that the Al of boehmite in (1)
2O
3Content is 30-55m%.
4,, it is characterized in that in (1) that said boehmite is to add acid or sodium metaaluminate adds CO by sodium metaaluminate according to the said preparation method of claim 1
2Or sodium metaaluminate adds aluminium salt and makes, and also can add alkali by aluminium salt and make, and said acid is selected from HCl, HNO
3And H
2SO
4, said aluminium salt is selected from AlCl
3, Al(NO
3)
3, said alkali is selected from NH
3H
2O, NaOH.
5,, it is characterized in that the solid content in the said slurries in (1), (2) is meant that these slurries are in 800 ℃ of calcinations residual solids content after 1 hour according to the said preparation method of claim 1.
Priority Applications (1)
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---|---|---|---|
CN93108631A CN1040845C (en) | 1993-07-16 | 1993-07-16 | Preparation of micro-ball gamma aluminum oxide |
Applications Claiming Priority (1)
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---|---|---|---|
CN93108631A CN1040845C (en) | 1993-07-16 | 1993-07-16 | Preparation of micro-ball gamma aluminum oxide |
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CN1097351A true CN1097351A (en) | 1995-01-18 |
CN1040845C CN1040845C (en) | 1998-11-25 |
Family
ID=4987216
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