CN1209355A - Macroporous alumina supporter and preparation method therefor - Google Patents
Macroporous alumina supporter and preparation method therefor Download PDFInfo
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- CN1209355A CN1209355A CN 97115255 CN97115255A CN1209355A CN 1209355 A CN1209355 A CN 1209355A CN 97115255 CN97115255 CN 97115255 CN 97115255 A CN97115255 A CN 97115255A CN 1209355 A CN1209355 A CN 1209355A
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Abstract
The present invention provides a macroporous alumina carrier and its preparation method. The pore volume of said invented carrier is 0.70-0.80 ml/g, and its specific surface area is 145-165 sq.m/g. It is characterized by that the pore volume of pore with diameter being 10-20 nm is 70-85% of total prore volume, and its strength is 15-25 N/mm. Said invented preparation method includes the following steps: at the temp. higher than room temp. using diasporite as raw material, making one undergo the processes of peptization or curing and extrusion-moulding, then using the compound containing ammonium ions to treat said formed material to obtain the invented product catalyst with large pore volume, centralized pore diameter and high strength, etc..
Description
The present invention relates to the macropore alumina supporter and the preparation thereof of a kind of alumina support and preparation thereof, particularly pore distribution concentration.
When preparation mink cell focus Hydrodemetalation catalyst, often need carrier to have bigger pore volume and suitable aperture.This is because large pore volume can provide bigger space for the deposition of the metal impurities in the mink cell focus on catalyst; The diffusion admittance that suitable aperture can facilitate for metal impurities.
According to people (Ind.Eng.Chem.Res.1987 such as Satoru Kobayashi, 26, result of study 2245-2250) shows, for the mink cell focus Hydrodemetalation catalyst that with the aluminium oxide is carrier, the catalyst pores diameter that the vanadium removal activity is the highest is 10-20nm, and the best bore dia of nickel removal is 10-15nm.So it is necessary to developing highly active demetalization (vanadium and nickel) catalyst that the preparation bore dia mainly concentrates on the macropore alumina supporter of 10-20nm.
For pore volume that improves alumina support and the aperture that obtains suitable size, generally adopt the method that adds filler at present, for example the introduction of US4448896 patent is a raw material with a kind of boehmite, and adding carbon powder, pinch through mixing, extrusion, drying and roasting obtain alumina support, the result makes support strength difference and pore size distribution disperse.
An object of the present invention is to provide a kind of method that alumina support pore distribution concentration and pore volume are increased, improve macropore alumina supporter intensity; Another object of the present invention provides that a kind of pore volume is big, pore distribution concentration, alumina support that intensity is high.
The main points of the inventive method are: 1) in the maturing process after with the Aci-Jel solvent boehmite being carried out peptization and/or peptization, provide certain heat, make material be kept above the temperature of room temperature; 2) after the extruded moulding, with the alkaline compound solution spray that contains ammonium ion or soak wet bar, carry out heat treated under the condition of room temperature being higher than then, perhaps after the extruded moulding, be higher than under the condition of room temperature, make wet bar and contain ammonia atmosphere and contact.
Macropore alumina supporter of the present invention, its pore volume are 0.70～0.80ml/g, and specific area is 145～165m
2/ g, bore dia be the pore volume of 10～20nm account for total pore volume 70～85%, intensity is 15～25N/mm.
Macropore alumina supporter of the present invention preferably, pore volume is 0.70～0.75ml/g, specific area is 150～160m
2/ g, bore dia be the pore volume of 10～20nm account for total pore volume 75～85%.
The preparation method of macropore alumina supporter of the present invention, comprise with the Aci-Jel solvent boehmite is carried out slaking behind peptization and the peptization, extruded moulding, drying and roasting, the material that different is behind the extruded moulding is being higher than under the condition of room temperature, handle with the alkali compounds that contains ammonium ion, the processing time is 0.1～2.0 hour, carries out drying and roasting then.
Said peptization is room temperature～95 ℃ peptization 0.3～1.5 hour, material behind the peptization was 40～95 ℃ of slakings 0.3～15 hour, material after the moulding sprays with the alkali compounds aqueous solution that contains ammonium ion or soaks, handled 0.1～2.0 hour at 40～95 ℃ then, or in 40～95 ℃ ammonia atmosphere, handled 0.1～2.0 hour.
The principle that the present invention increases alumina support pore distribution concentration and pore volume is: improve the effect that peptization and/or curing temperature help strengthening peptizing agent and boehmite.Make it more even, more abundant, thereby the raising concentrated and intensity that distributes for carrier hole lay the first stone; Handle after the moulding wet bar or make it contact with the alkali compounds that contains ammonium ion, can make boehmite after the acidifying be similar to neutralization reaction when preparing boehmite once more with containing ammonia atmosphere, thus the pore volume of raising alumina support.Because said this neutralization reaction occurs in after the extruded moulding, therefore moulding and the mechanical strength to carrier all do not exert an influence.
The preparation process of alumina support of the present invention is:
1) take by weighing the boehmite dry glue powder of constant weight, add the aqueous solution that contains the Aci-Jel solvent in right amount, room temperature～95 ℃ peptization 0.3～1.5 hour, slaking 0.3～15 hour under 40～95 ℃ of conditions then;
2) with the plasticity material extruded moulding on banded extruder after the slaking, its shape and particle diameter are determined by orifice plate;
3) with the wet bar that the alkali compounds aqueous solution that contains ammonium ion sprays or immersion is extruded, handled 0.1～2.0 hour at 40～95 ℃ then; The bar that maybe will wet was handled in 40～95 ℃ ammonia atmosphere 0.1～2.0 hour;
4) 105～140 ℃ of dryings 1～8 hour, put it into then in the roaster, rise to 850～1020 ℃ of constant temperature 1-8 hours with 200～300 ℃/hour speed.
Aci-Jel solvent of the present invention is nitric acid, acetic acid, formic acid and their aluminium salt, is nitric acid, acetic acid preferably, is preferably nitric acid.The described ammonium ion alkali compounds that contains is an ammoniacal liquor, and ammonium carbonate, ammonium phosphate, ammonium borate, ammonium acetate are preferably ammoniacal liquor, ammonium carbonate, ammonium carbonate preferably.The ammonium ion compound that contains that easily decomposes or volatilize is meant at the compound that can discharge ammonia below 90 ℃, as ammoniacal liquor, ammonium carbonate, carbonic hydroammonium.
The feature of alumina support of the present invention is, pore volume is at least 0.70ml/g, wherein the bore dia of at least 75% pore volume is 10～20nm, bore dia be the pore volume of 20～30nm account for total hole ratio less than 13%, bore dia accounts for the ratio in total hole less than 12% less than the pore volume of 10nm; Its surface area is 120～180m
2/ g.
The shape of alumina support of the present invention can change according to different requirements.
Alumina support of the present invention can be used as catalyst carrier for hydrgenating, and being specially adapted to vanadium removal, nickel is the mink cell focus Hydrodemetalation catalyst carrier and the hydrodesulfurization catalyst support of purpose.
The inorganic compound that can add elements such as boracic, silicon, phosphorus, titanium, magnesium in the preparing carriers method of the present invention is to obtain the macroporous catalyst carrier of the different pore distribution concentration of physico-chemical property.
Compare with the method for traditional expansion carrier pore volume, the advantage of the inventive method is:
1) do not add physics expanding agents such as carbon black, high molecular polymer.Eliminated thus because of adding the support strength decline that this type of material causes, bulk density reduces, problems such as pore size distribution disperse;
2) adopt heating peptization and/or curing process, overcome the problem that the normal temperature peptization makes carrier hole distribute and concentrate inadequately;
3) adopt the preparation technology of neutralisation treatment behind the extruded moulding, overcome shortcoming such as carry out the caused carrier insufficient formability of neutralisation treatment in the peptization course, mechanical strength is low, bulk density is little.
Below further specify feature of the present invention with embodiment.
Embodiment 1
Take by weighing the boehmite dry glue powder that 200g Fushun petrochemical corporation (complex) produces with Alchlor process, add the acetum 185ml of 2.3w%, mix under the room temperature and pinch 1hr, put into drying box, slaking 14hr under 45 ± 5 ℃ of conditions; Being squeezed into diameter then on the screw rod banded extruder is the bunge bedstraw herb shape bar of φ 1.2mm, the wet bar of just having extruded with the even spray of sal volatile of 36ml concentration 18w%, subsequently with it in 45 ± 5 ℃ drying box, constant temperature is handled 2.0hr; At 105～140 ℃ of dry 2hr.Insert again in the roaster, rise to 930 ℃ with the speed of 200～300 ℃/hr, constant temperature 3hr, cooling naturally obtains alumina support A then.
Embodiment 2
Take by weighing the boehmite dry glue powder of 200g Qilu Petroleum Chemical Corporation Institute, add the Burow's Solution 160ml of 3.0w%, mix under the room temperature and pinch 1hr, put into drying box, slaking 8hr under 55 ± 5 ℃ of conditions with the preparation of carbon dioxide neutralisation; Being extruded into diameter on the screw rod banded extruder is the bunge bedstraw herb shape bar of φ 1.2mm, is the wet bar that the even spray of ammonia spirit of 10w% has just been extruded with 36ml concentration, puts it into temperature subsequently and is in 55 ± 5 ℃ the drying box, constant temperature 1.6hr; Press method drying, the roasting sample of embodiment 1 again, get alumina support B.
Embodiment 3
Take by weighing the boehmite dry glue powder that petrochemical industry new and high technology development centre, 200g Fushun produces with the aluminum sulfate method, add the salpeter solution 176ml of 2w%, mix at 50+10 ℃ and pinched 35 minutes; Slaking 1.5hr in 75 ± 5 ℃ of drying boxes; Be extruded into the bunge bedstraw herb shape bar that diameter is φ 1.2mm with the screw rod banded extruder again, will wet then bar and 4g ammonium carbonate are together put into 75 ± 5 ℃ drying box constant temperature 1.5hr; Subsequent process by embodiment 1 carries out then, gets alumina support C.
Embodiment 4
Take by weighing the identical dry glue powder of 200g and embodiment 3, add the aluminum nitrate solution 176ml of 2.5w%, mix at 80 ± 10 ℃ and pinched 20 minutes; Slaking 0.5hr is extruded into the bunge bedstraw herb shape bar that diameter is φ 1.2mm with the screw rod banded extruder again in 90 ± 5 ℃ drying box, the bar that will wet then is to soak 1 minute in the 20w% ammonium phosphate solution in concentration, put into temperature after the taking-up and be in 90 ± 5 ℃ the drying box, constant temperature 0.5hr; Carry out subsequent process by the method for embodiment 1 again, get alumina support D.
Comparative example 1
Take by weighing the identical dry glue powder of 200g and embodiment 1, add the acetum 185ml of 2.3w%, mix under the room temperature and pinch 1hr, leave standstill 14hr again; Being extruded into diameter then on the screw rod banded extruder is the bunge bedstraw herb shape bar of φ 1.2mm, at room temperature places 2.0hr; Subsequent process by embodiment 1 carries out drying, roasting at last, gets this routine alumina support E.
Comparative example 2
Undertaken by embodiment 1 before the extrusion; Undertaken by comparative example 1 after the extrusion, get alumina support F.
Comparative example 3
Undertaken by comparative example 1 before the extrusion; Undertaken by embodiment 1 after the extrusion, get alumina support G.
Comparative example 4
In comparative example 1, in dry glue powder, sneak into the high wear-resistant carbon black that 13g Fushun Carbon Black Plant produces, get alumina support H.
Comparative example 5
In comparative example 1, acetum changes 3.0w%, 142ml into by 2.3w%, 185ml, and in the peptization course after adding acetum, adds the ammonia spirit that 43ml concentration is 2.8w% again, gets the alumina support I.
Comparative example 6
This example is the comparing result of the alumina support physico-chemical property of embodiment 1-4 and comparative example 1-5.
*Pore volume in a certain bore dia scope accounts for the percentage of total pore volume:
*Equivalent diameter 1.2mm.
| Project/carrier | Embodiment | Comparative example | |||||||
| ????A | ?B | ?C | ?D | ?E | ?F | ?G | ?H | ?I | |
| Pore volume, ml/g | ???0.75 | ?0.73 | ?0.73 | ?0.71 | ?0.65 | ?0.69 | ?0.69 | ?0.73 | ?0.75 |
| Specific area, m 2/g | ???151 | ?157 | ??161 | ?149 | ?158 | ?160 | ??154 | ?167 | ?143 |
| Pore size distribution, % * | |||||||||
| ????10-nm | ????10 | ??11 | ????8 | ???7 | ???16 | ??30 | ????4 | ??15 | ???8 |
| ????10-20nm | ????76 | ??75 | ???78 | ???81 | ???71 | ??67 | ????59 | ??69 | ??69 |
| ????20-30nm | ????11 | ??12 | ???11 | ???11 | ???11 | ???2 | ????29 | ??11 | ??14 |
| ????30+nm | ????3 | ???2 | ????3 | ????1 | ????2 | ???1 | ????8 | ???5 | ???9 |
| Intensity, N/mm ** | ????18 | ??17 | ????20 | ???19 | ????14 | ??18 | ????14 | ???13 | ??13 |
| Bulk density, g/ml | ???0.54 | ?0.54 | ???0.54 | ??0.54 | ???0.54 | ?0.54 | ??0.54 | ??0.49 | ??0.43 |
By above-mentioned comparing result as can be seen, the alumina support of making according to the inventive method, big, the pore distribution concentration of pore volume not only, and also intensity is good, and bulk density is suitable.
Claims (8)
1, a kind of macropore alumina supporter, its pore volume are 0.70～0.80ml/g, and specific area is 145～165m2/g, it is characterized in that bore dia is that the pore volume of 10～20nm accounts for 70～85% of total pore volume, and intensity is 15～25N/mm.
2, according to the carrier of claim 1, it is characterized in that pore volume is 0.70～0.75ml/g, specific area is 150～160m2/g, it is characterized in that bore dia is that the pore volume of 10～20nm accounts for 75～85% of total pore volume, intensity is 15～25N/mm.
3, a kind of preparation method of macropore alumina supporter, comprise with the Aci-Jel solvent boehmite is carried out slaking behind peptization and the peptization, extruded moulding, drying and roasting, it is characterized in that the material behind the extruded moulding is being higher than under the condition of room temperature, handle with the alkali compounds that contains ammonium ion, the processing time is 0.1～2.0 hour, carries out drying and roasting then.
4,, it is characterized in that the boehmite raw material was room temperature～95 ℃ peptization 0.3～1.5 hour according to the method for claim 3.
5,, it is characterized in that material behind the peptization was 40～95 ℃ of slakings 0.3～15 hour according to the method for claim 3.
6, according to the method for claim 3, it is characterized in that the material after the moulding sprays with the alkali compounds aqueous solution that contains ammonium ion, handled 0.1～2.0 hour at 40～95 ℃ then.
7,, it is characterized in that material after the moulding with the alkali compounds aqueous solution soaking that contains ammonium ion, handled 0.1～2.0 hour at 40～95 ℃ then according to the method for claim 3.
8,, it is characterized in that the material after the moulding was handled 0.1～2.0 hour in 40～95 ℃ ammonia atmosphere according to the method for claim 3.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN97115255A CN1089031C (en) | 1997-08-27 | 1997-08-27 | Macroporous alumina supporter and preparation method therefor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN97115255A CN1089031C (en) | 1997-08-27 | 1997-08-27 | Macroporous alumina supporter and preparation method therefor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1209355A true CN1209355A (en) | 1999-03-03 |
| CN1089031C CN1089031C (en) | 2002-08-14 |
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ID=5173245
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN97115255A Expired - Lifetime CN1089031C (en) | 1997-08-27 | 1997-08-27 | Macroporous alumina supporter and preparation method therefor |
Country Status (1)
| Country | Link |
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| CN (1) | CN1089031C (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1313374C (en) * | 2004-10-29 | 2007-05-02 | 中国石油化工股份有限公司 | Gama-Al2O3 preparation method |
| WO2007131436A1 (en) * | 2006-05-08 | 2007-11-22 | Zhaoqing Shunxin Coal Chemical Industry S.T. Co., Ltd. | A preload hydrogen catalyst for liquidizing coal to supply hydrogen and its preparation method |
| CN100496738C (en) * | 2004-12-28 | 2009-06-10 | 中国石油化工股份有限公司 | Alumina supporter possessing duplicate orifice, catalyst and preparation method |
| CN105642304A (en) * | 2014-12-04 | 2016-06-08 | 中国石油化工股份有限公司 | Preparation method of hydrodemetallization catalyst |
| CN105642369A (en) * | 2014-12-04 | 2016-06-08 | 中国石油化工股份有限公司 | Alumina carrier forming treatment method for reducing NOx emission |
| CN104549331B (en) * | 2013-10-23 | 2017-08-22 | 中国石油化工股份有限公司 | A kind of preparation method of Hydrodemetalation catalyst |
| CN108262075A (en) * | 2016-12-30 | 2018-07-10 | 中国石油天然气股份有限公司 | Residual oil hydrotreating catalyst carrier and preparation method thereof |
| CN110882683A (en) * | 2019-11-26 | 2020-03-17 | 青岛庄信恒瑞催化剂有限公司 | Dechlorination deoxidation catalyst and preparation method and application thereof |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100346873C (en) * | 2005-09-09 | 2007-11-07 | 清华大学 | Method for preparing large pore capacity, high specific surface area alumina |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4572778A (en) * | 1984-01-19 | 1986-02-25 | Union Oil Company Of California | Hydroprocessing with a large pore catalyst |
| JPH0593190A (en) * | 1991-03-29 | 1993-04-16 | Nippon Oil Co Ltd | Hydrogenation of residual oil |
| CN1048229C (en) * | 1994-07-01 | 2000-01-12 | 化学工业部天津化工研究院(熊尚彬) | Process for preparing spheric aluminium oxide with low density and big pore volume |
| US5620592A (en) * | 1994-07-29 | 1997-04-15 | Chevron U.S.A. Inc. | Low macropore resid conversion catalyst |
-
1997
- 1997-08-27 CN CN97115255A patent/CN1089031C/en not_active Expired - Lifetime
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1313374C (en) * | 2004-10-29 | 2007-05-02 | 中国石油化工股份有限公司 | Gama-Al2O3 preparation method |
| CN100496738C (en) * | 2004-12-28 | 2009-06-10 | 中国石油化工股份有限公司 | Alumina supporter possessing duplicate orifice, catalyst and preparation method |
| WO2007131436A1 (en) * | 2006-05-08 | 2007-11-22 | Zhaoqing Shunxin Coal Chemical Industry S.T. Co., Ltd. | A preload hydrogen catalyst for liquidizing coal to supply hydrogen and its preparation method |
| CN104549331B (en) * | 2013-10-23 | 2017-08-22 | 中国石油化工股份有限公司 | A kind of preparation method of Hydrodemetalation catalyst |
| CN105642304A (en) * | 2014-12-04 | 2016-06-08 | 中国石油化工股份有限公司 | Preparation method of hydrodemetallization catalyst |
| CN105642369A (en) * | 2014-12-04 | 2016-06-08 | 中国石油化工股份有限公司 | Alumina carrier forming treatment method for reducing NOx emission |
| CN105642304B (en) * | 2014-12-04 | 2018-08-14 | 中国石油化工股份有限公司 | A kind of preparation method of Hydrodemetalation catalyst |
| CN105642369B (en) * | 2014-12-04 | 2019-01-25 | 中国石油化工股份有限公司 | A kind of reduction NOxThe alumina support forming processing method of discharge |
| CN108262075A (en) * | 2016-12-30 | 2018-07-10 | 中国石油天然气股份有限公司 | Residual oil hydrotreating catalyst carrier and preparation method thereof |
| CN108262075B (en) * | 2016-12-30 | 2020-12-01 | 中国石油天然气股份有限公司 | Residual oil hydrotreating catalyst carrier and preparation method thereof |
| CN110882683A (en) * | 2019-11-26 | 2020-03-17 | 青岛庄信恒瑞催化剂有限公司 | Dechlorination deoxidation catalyst and preparation method and application thereof |
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| Publication number | Publication date |
|---|---|
| CN1089031C (en) | 2002-08-14 |
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Owner name: CHINA PETROCHEMICAL CORPORATION; CHINA PETROLEUM Free format text: FORMER OWNER: CHINA PETRO-CHEMICAL CORP.; FUSHUN PETRO-CHEMICAL INST., SINOPEC Effective date: 20010719 |
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