CN1055877C - Large-pore alumina carrier and its preparation process - Google Patents
Large-pore alumina carrier and its preparation process Download PDFInfo
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- CN1055877C CN1055877C CN96103297A CN96103297A CN1055877C CN 1055877 C CN1055877 C CN 1055877C CN 96103297 A CN96103297 A CN 96103297A CN 96103297 A CN96103297 A CN 96103297A CN 1055877 C CN1055877 C CN 1055877C
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- Prior art keywords
- aluminium oxide
- boehmite
- preparation
- pore
- expanding agent
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- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 title claims abstract description 62
- 239000011148 porous material Substances 0.000 title claims abstract description 27
- 238000002360 preparation method Methods 0.000 title claims abstract description 12
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 39
- 238000000034 method Methods 0.000 claims abstract description 23
- 239000000126 substance Substances 0.000 claims abstract description 17
- 230000008569 process Effects 0.000 claims abstract description 9
- 239000006229 carbon black Substances 0.000 claims abstract description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 7
- 239000007864 aqueous solution Substances 0.000 claims abstract description 5
- 229910001593 boehmite Inorganic materials 0.000 claims description 15
- FAHBNUUHRFUEAI-UHFFFAOYSA-M hydroxidooxidoaluminium Chemical compound O[Al]=O FAHBNUUHRFUEAI-UHFFFAOYSA-M 0.000 claims description 15
- 239000000843 powder Substances 0.000 claims description 10
- 239000003292 glue Substances 0.000 claims description 9
- 239000007787 solid Substances 0.000 claims description 7
- 239000002245 particle Substances 0.000 claims description 6
- 229910052698 phosphorus Inorganic materials 0.000 claims description 6
- 239000011574 phosphorus Substances 0.000 claims description 6
- 230000009471 action Effects 0.000 claims description 4
- 229910052710 silicon Inorganic materials 0.000 claims description 4
- 239000010703 silicon Substances 0.000 claims description 4
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims description 3
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims description 3
- 150000001639 boron compounds Chemical class 0.000 claims description 3
- 150000001875 compounds Chemical class 0.000 claims description 2
- 238000001035 drying Methods 0.000 claims 1
- BHEPBYXIRTUNPN-UHFFFAOYSA-N hydridophosphorus(.) (triplet) Chemical compound [PH] BHEPBYXIRTUNPN-UHFFFAOYSA-N 0.000 claims 1
- 239000000295 fuel oil Substances 0.000 abstract description 2
- 238000004898 kneading Methods 0.000 abstract description 2
- 238000002156 mixing Methods 0.000 abstract description 2
- VXAUWWUXCIMFIM-UHFFFAOYSA-M aluminum;oxygen(2-);hydroxide Chemical compound [OH-].[O-2].[Al+3] VXAUWWUXCIMFIM-UHFFFAOYSA-M 0.000 abstract 1
- 239000000463 material Substances 0.000 abstract 1
- 150000003018 phosphorus compounds Chemical class 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 12
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 10
- 238000009826 distribution Methods 0.000 description 9
- 239000003054 catalyst Substances 0.000 description 8
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 6
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 5
- 238000001125 extrusion Methods 0.000 description 5
- 229960000583 acetic acid Drugs 0.000 description 3
- 239000012362 glacial acetic acid Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- -1 phosphorus compound Chemical class 0.000 description 3
- 238000007493 shaping process Methods 0.000 description 3
- 238000005245 sintering Methods 0.000 description 3
- 238000005303 weighing Methods 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 150000002484 inorganic compounds Chemical class 0.000 description 2
- 229910010272 inorganic material Inorganic materials 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 2
- 229910052753 mercury Inorganic materials 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 239000002243 precursor Substances 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 241000772415 Neovison vison Species 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- 239000012687 aluminium precursor Substances 0.000 description 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000003837 high-temperature calcination Methods 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000001935 peptisation Methods 0.000 description 1
- 238000002407 reforming Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
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- Catalysts (AREA)
Abstract
The present invention relates to a macroporous alumina supporter and a preparation method thereof. The macroporous alumina supporter is characterized in that the pore volume is 0.80 to 1.20 ml/g, the probable pore diameter is from 15.0 to 20.0 nm, the bulk density is from 0.50 to 0.60 g/ml, and the specific surface area is from 110 to 200 m<2>/g. The preparation method of the macroporous alumina supporter comprises: physical reaming agents (such as carbon black) and chemical reaming agents (such as phosphorus compounds) are added into the process of mixing and kneading pseudo-boehmite and water or aqueous solutions, the mixed materials are mixed and kneaded into a plastic body, the plastic body is extruded into bars for forming by a bar extruder, and the bars are dried and roasted at the temperature of 840 to 1000 DEG C for 1 to 5 hours. The alumina supporter prepared by the preparation method provided by the present invention can be used for preparing hydrodemetalization and/or hydrodesulfurization catallsts for heavy oil, particularly residuum.
Description
The present invention relates to the preparation of the preparation of alumina support, particularly large-pore alumina carrier.
Particularly when residuum hydrogenating and metal-eliminating and/or Hydrobon catalyst, general be carrier matrix with the bigger aluminium oxide in aperture to the preparation heavy distillate.Often need to use by the made aluminium oxide of extrusion shaping, so the key technology of large-pore alumina carrier preparation is to enlarge its aperture through reaming.
One of common expanding method is in the aluminium oxide precursor--add various expanding agents in the mixed pinching bar process of boehmite dry glue powder.
For example, the US4102822 patent proposes to add the aperture that expanding agent such as starch enlarges alumina support in mixing pinching bar process, and it is expanding agent that US4448896 then selects carbon black for use, and EP237240 proposes to add the charcoal fiber and forms macropore.The reaming mechanism of above-mentioned three kinds of expanding agents is: expanding agent mixes with solid form and boehmite dry glue powder, occupies certain spatial volume in the bar shaped particle of extruding.In the high-temperature calcination process of carrier, expanding agent is converted into gas, so form a certain amount of macropore.Chemical action does not take place in this expanding agent and boehmite, has been physical action, so can be described as the physics expanding agent.
And for example, Chinese patent ZL92112511.9 proposes to add Ludox in the mixed pinching bar process of boehmite and can play the reaming effect.Adding silicon (Si) and phosphorus (P) compound in addition in alumina support, can to play the reaming effect of reaming effect, particularly phosphorus compound more obvious.This expanding agent and boehmite generation chemical action are so can be described as the chemical enlargement agent.
When using the physics expanding agent merely, have following shortcoming: pore size distribution disperse after (1) reaming, carrier mechanical strength and bulk density obviously descend after (2) reaming.The decline of carrier mechanical strength, to make mechanical strength not meet the requirement that industry is used by its catalyst of making, and carrier hole distribution disperse and bulk density descend, effective internal surface area that the unit admission space that makes by its catalyst of making is had reduces, and the activity of catalyst corresponding volume air speed is reduced.
The simple peptization variation of using the chemical enlargement agent will make boehmite, thus bring difficulty for the extrusion shaping operation.In addition, when using the chemical enlargement agent in a large number, often make the pore size distribution disperse of the alumina support of making, thereby the reaming effect is restricted.
When aforesaid two class expanding agents use separately, its consumption all is subjected to certain limitation, therefore its reaming effect is also extremely limited, be difficult to prepare that pore volume is big, pore distribution concentration, and the alumina support that intensity and bulk density are suitable, particularly worked as expanding method not at that time, caused the aperture disperse, and will the efficient of catalyst be reduced greatly.
The objective of the invention is to seek a kind of effective ways that enlarge the carrying alumina body aperture, make that the carrying alumina body aperture made and pore volume are big, pore distribution concentration, mechanical strength and bulk density be moderate, and then improve the efficient of catalyst.
The present invention about the method main points that enlarge the carrying alumina body aperture is: in the precursor of aluminium oxide--in boehmite dry glue powder and water or the aqueous solution kneading process, add two kinds of dissimilar expanding agents simultaneously, a kind of is the physics expanding agent, and another kind is the chemical enlargement agent.
The physics expanding agent generally is the Flammable Solid Class 4.1 particle, and its reaming principle is: this solid particle under water or aqueous solution effect, is extruded into strip, high-temperature roasting in oxygen-containing atmosphere then with after the boehmite dry glue powder evenly mixes; In this roasting process, the physics expanding agent is converted into gas and overflows, and stays the macropore of certain volume, makes roasting gained bar shaped carrying alumina body aperture obtain enlarging.Its pore size is determined by factors such as physics expanding agent kind, solid particle size, sintering temperature, calcination atmospheres after the carrier reaming.
The chemical enlargement agent generally is the inorganic compound that can chemically react with aluminium oxide and precursor thereof, as phosphorus, silicon and boron compound etc.The reaming principle of chemical enlargement agent is: inorganic compound and the effect of boehmite generation surface chemistry as expanding agent, and the intergranular adhesion of dry glue powder is weakened, the space increases each other, thereby the part macropore occurs.
When simple use physics expanding agent or chemical enlargement agent, in order to reach obvious effects, use amount is often bigger, thereby its negative effect (shortcoming) is also apparent in view.In the present invention, propose to use simultaneously physics expanding agent and chemical enlargement agent, two kinds of expanding agent synergies, not only can reduce its each plant demand, overcome negative effect separately, reached tangible reaming effect simultaneously, prepared that pore volume is big, the alumina support of pore distribution concentration.
The preparation method of alumina support of the present invention is: take by weighing a certain amount of boehmite dry glue powder, (consumption is 3-10w% to the physics expanding agent, based on aluminium oxide) and extrusion aid, mix, add and dissolved the aqueous solution of chemical enlargement agent (when the chemical enlargement agent is phosphorus compound, the phosphorus compound addition is counted 0.1-1.5w% with aluminium oxide), mix and pinch evenly, become plastic, extrusion is shaped on banded extruder.Bar after the shaping places roaster then at 90-150 ℃ of following dry 2-8h or dry in the shade naturally, is warming up to 840-1000 ℃, and constant temperature 1-5h obtains alumina support at last.The pore volume of the made carrier of the method is that 0.80-1.20ml/g (mercury injection method mensuration), specific area are 110-200m
2/ g, can several apertures be that 15.0-20.0nm, bulk density are 0.50-0.60g/ml.
The advantage of expanding method of the present invention is: (1) is owing to not increasing additional step, and is simple and easy to do, grasps easily.(2) aperture of aluminium oxide can be regulated by the addition of adjusting two kinds of expanding agents as required.(3) owing to use two kinds of expanding agents simultaneously, can effectively control product property, can relax restriction, reduce production costs the aluminium oxide precursor.According to said method Zhi Bei alumina support has following characteristics: (1) aperture and pore volume are big, pore distribution concentration.(2) owing to exceed adding physics expanding agent, make mechanical strength and bulk density moderate.The alumina support that adopts the inventive method to make can be used for preparing mink cell focus particularly residuum hydrogenating and metal-eliminating and/or Hydrobon catalyst.
Further specify the present invention below in conjunction with embodiment.
Embodiment 1
Take by weighing Chinese Qilu Petroleum Chemical Corporation Institute with in the carbon dioxide and the prepared boehmite dry glue powder 300g (moisture 78g) of sodium metaaluminate, the granular size that takes by weighing the production of Chinese Fushun Carbon Black Plant again is 30 microns carbon black 18g and the blue or green powder 10g in extrusion aid field, mix, add by 2.0g phosphoric acid and 400g water (H
2O) solution that is made into mixes and pinches into plastic, is extruded into little of φ 0.9mm on banded extruder, and dry 4h under 120 ℃ is then at 900 ℃ of following roasting 2h.
Embodiment 2
In embodiment 1,2.0g phosphoric acid is changed into 1.0g phosphoric acid and 10g glacial acetic acid, i.e. cost example.
Embodiment 3
In embodiment 1,18g changes 11g into carbon black, i.e. the cost example.
Embodiment 4
In embodiment 1, sintering temperature changes 960 ℃ into, i.e. the cost example.
Embodiment 5
Sintering temperature changes 850 ℃ into, i.e. the cost example.
Embodiment 6
In embodiment 1, the boehmite dry glue powder change into Chinese Fushun No.3 Petroleum Factory by in the ammoniacal liquor and the alchlor method produce.
Comparative example 1
In embodiment 1, used carbon black 18g changes 60g into, and water 400g changes 380g into, and 2.0g phosphoric acid changes the 10g glacial acetic acid into, i.e. the cost example.
Comparative example 2
In embodiment 1, without carbon black, water 400g changes 380g into, and 2.0g phosphoric acid changes 6.0g into, and other adds the 15g glacial acetic acid, i.e. the cost example.
Embodiment 7
This example provides the physico-chemical property of the alumina support that above each example makes.
The physical property of the different alumina supports of table 1
| Comparative example 1 | Comparative example 2 | Embodiment | Embodiment 2 | Embodiment 3 | Embodiment 4 | Embodiment 5 | Embodiment 6 | ||
| Bulk density g/ml | 0.41 | 0.47 | 0.52 | 0.54 | 0.53 | 0.54 | 0.52 | 0.53 | |
| Crushing strength N/mm | 4.6 | 5.4 | 7.6 | 8.4 | 8.5 | 8.2 | 7.9 | 8.2 | |
| Pore volume (mercury injection method) ml/g | 1.08 | 1.05 | 1.00 | 0.90 | 0.86 | 0.85 | 0.98 | 0.92 | |
| Specific surface m 2/g | 177 | 168 | 162 | 157 | 160 | 148 | 159 | 160 | |
| Can a few bore dia nm | 13-20 | 14-18 | 17 | 16 | 17 | 18 | 16 | 17 | |
| Pore size distribution (%) | ＜10nm | 25 | 23 | 13 | 12 | 14 | 11 | 16 | 13 |
| 10-20nm | 44 | 49 | 60 | 70 | 61 | 65 | 58 | 68 | |
| ＞20nm | 31 | 28 | 27 | 18 | 19 | 24 | 26 | 19 | |
By table 1 data as can be seen, although used the expanding agent of a large amount of single kind in comparative example 1,2, the pore volume in the hole of aperture between 10-20nm also has only 44-49%, bulk density＜0.47g/ml, crushing strength＜5.4N/mm in the prepared carrier.With the carrier of the inventive method preparation, have the pore size distribution of concentrating very much, the pore volume of aperture 10-20nm accounts for 58-70%, and its bulk density＞0.52g/ml, crushing strength＞7.5N/mm, pore volume＞0.85ml/g, specific surface＞148m
2/ g can a few aperture＞16nm, are suitable for use as the carrier of heavy oil or residual oil reforming catalyst.
Claims (5)
1, a kind of large-pore alumina carrier is characterized in that pore volume is 0.80-1.20ml/g, can several bore dias be 15.0～20.0nm, and bulk density is 0.50～0.60g/ml, and specific area is 110～200m
2/ g.
2, a kind of preparation method of large-pore alumina carrier, its process are A, mixed boehmite dry glue powder and water or the aqueous solution, and mediating becomes plastic; B, on banded extruder, be extruded into bar by the plastic of A gained; C, carry out drying and 840～1000 ℃ of following roastings by the bar of B gained, it is characterized in that in the described process of A, add simultaneously with aluminium oxide count 3～10w% Flammable Solid Class 4.1 particle expanding agent and with aluminium oxide count 0.1～1.5w% can with phosphorous, the silicon of boehmite or aluminium oxide generation chemical action or the expanding agent of boron compound.
3,, it is characterized in that the Flammable Solid Class 4.1 granular size is 25～40 microns according to the described method of claim 2.
4,, it is characterized in that to be water-soluble phosphorus, silicon and boron compound with the compound of boehmite or aluminium oxide generation chemical action according to claim 2 or 3 described methods.
5,, it is characterized in that the Flammable Solid Class 4.1 particle is a carbon black according to the described method of claim 3.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN96103297A CN1055877C (en) | 1996-03-26 | 1996-03-26 | Large-pore alumina carrier and its preparation process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN96103297A CN1055877C (en) | 1996-03-26 | 1996-03-26 | Large-pore alumina carrier and its preparation process |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1160602A CN1160602A (en) | 1997-10-01 |
| CN1055877C true CN1055877C (en) | 2000-08-30 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN96103297A Expired - Lifetime CN1055877C (en) | 1996-03-26 | 1996-03-26 | Large-pore alumina carrier and its preparation process |
Country Status (1)
| Country | Link |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1296136C (en) * | 2004-01-19 | 2007-01-24 | 中国石油化工股份有限公司 | Macroporous aluminium oxide carrier and its preparing method |
| US9486795B2 (en) | 2007-06-27 | 2016-11-08 | China Petroleum & Chemical Corporation | Catalytic cracking catalyst, its preparation and use |
| CN108855024A (en) * | 2018-05-28 | 2018-11-23 | 中化泉州石化有限公司 | A kind of large aperture, high mechanical strength alumina support preparation method |
| WO2019196836A1 (en) | 2018-04-10 | 2019-10-17 | 中国石油化工股份有限公司 | Hydrorefining catalyst, preparation method therefor and use thereof |
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| CN1089039C (en) * | 1998-09-28 | 2002-08-14 | 中国石油化工集团公司 | Macroporous alumina carrier and preparing process thereof |
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1996
- 1996-03-26 CN CN96103297A patent/CN1055877C/en not_active Expired - Lifetime
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1296136C (en) * | 2004-01-19 | 2007-01-24 | 中国石油化工股份有限公司 | Macroporous aluminium oxide carrier and its preparing method |
| US9486795B2 (en) | 2007-06-27 | 2016-11-08 | China Petroleum & Chemical Corporation | Catalytic cracking catalyst, its preparation and use |
| WO2019196836A1 (en) | 2018-04-10 | 2019-10-17 | 中国石油化工股份有限公司 | Hydrorefining catalyst, preparation method therefor and use thereof |
| US11439989B2 (en) | 2018-04-10 | 2022-09-13 | China Petroleum & Chemical Corporation | Hydrofining catalyst, its preparation and application thereof |
| CN108855024A (en) * | 2018-05-28 | 2018-11-23 | 中化泉州石化有限公司 | A kind of large aperture, high mechanical strength alumina support preparation method |
| CN108855024B (en) * | 2018-05-28 | 2021-04-27 | 中化泉州石化有限公司 | A kind of preparation method of alumina carrier with large pore size and high mechanical strength |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1160602A (en) | 1997-10-01 |
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