CN105478100A - Method for preparing silicon-containing gamma-Al2O3 microsphere - Google Patents
Method for preparing silicon-containing gamma-Al2O3 microsphere Download PDFInfo
- Publication number
- CN105478100A CN105478100A CN201510781628.4A CN201510781628A CN105478100A CN 105478100 A CN105478100 A CN 105478100A CN 201510781628 A CN201510781628 A CN 201510781628A CN 105478100 A CN105478100 A CN 105478100A
- Authority
- CN
- China
- Prior art keywords
- hours
- grams
- deionized water
- stir
- bead
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Catalysts (AREA)
Abstract
A disclosed method for preparing silicon-containing gamma-Al2O3 microsphere comprises stirring 200 g of Al(OH)3 powder and proper amount of deionized water to form a slurry, and controlling the liquid-solid mass ratio to be 3-10; adding 10 mL of diluted nitric acid with the volume ratio of 1:3, 10-15 g of urea and a predetermined amount of a sodium silicate solution, and enabling the silicon content in the solution is 0.30% by mass of dry aluminium oxide, stirring for 5 h, adding 40-50 g of kerosene and 5 g of fatty alcohol polyoxyethylene ether, stirring for 5 h, and dropping in an oil-ammonia column to form spheres; and solidifying the wet spheres in ammonia water with the mass concentration of 5% for 2 h, then filtering, flushing with deionized water for 6 times, drying at 80 DEG C for 4 h, drying at 100 DEG C for 2 h, and roasting at 800 DEG C for 3 h, so as to obtain the silicon-containing gamma-Al2O3 microsphere. The silicon-containing gamma-Al2O3 microsphere can be used as a catalyst for preparing propylene through dehydrogenation of propane, and possesses better effect compared with aluminium microspheres containing other elements.
Description
Technical field
The present invention relates to and a kind ofly prepare siliceous γ-Al
2o
3the method of bead.
Background technology
The reaction of preparing propylene by dehydrogenating propane is by balance controlled, and for making reaction carry out to dehydrogenation direction, need improve reaction temperature and reduce pressure, high reaction temperature often causes the sintering of platinum group metal catalyst with hydrogenation/dehydrogenation function and a large amount of carbon deposit.The stability of propane dehydrogenation catalyst and selective can be increased substantially by introducing IVA race metal and alkali metal or alkaline-earth metal.In actual applications, along with the lengthening of catalyst service time, need to carry out regeneration process to catalyst, namely by the carbon deposit in high-temperature roasting removing catalyst, recover the performance of catalyst.
In order to realize catalyst performance preferably, must improve aluminum oxide micro-sphere wherein, particularly in the catalyst of preparing propylene by dehydrogenating propane, microballoon of the prior art all well can not realize catalytic action,
Summary of the invention
In order to solve the problems of the technologies described above, the present invention proposes a kind of method that preparation method is specially the bead of the siliceous aluminium oxide of preparation, and its concrete technical scheme is as follows:
A kind ofly prepare siliceous γ-Al
2o
3the method of bead, obtains as follows: get 200 grams of AL (OH)
3powder and appropriate amount of deionized water stir pulp, Gu liquid/mass ratio is 3-10, adding 10 ml volumes ratios is the dust technology of 1: 3, the sodium silicate solution of 10-15 gram of urea and scheduled volume, the relative butt aluminium oxide of the silicon content in solution is made to be 0.30 quality %, stir 5 hours, add 40-50 gram of kerosene and 5 grams of AEOs stir 5 hours, in oil ammonia column, drip ball forming.Wet bulb solidifies 2 hours in the ammoniacal liquor of 5 quality %, then filters, and with deionized water rinsing 6 times, 80 DEG C dryings 4 hours, 100 DEG C of dryings, 12 hours, 800 DEG C roastings 3 hours, obtained siliceous γ-Al
2o
3bead.
Wherein preferred technical scheme is:
A kind ofly prepare siliceous γ-Al
2o
3the method of bead, obtains as follows: get 200 grams of AL (OH)
3powder and appropriate amount of deionized water stir pulp, Gu liquid/mass ratio is 8, adding 10 ml volumes ratios is the dust technology of 1: 3, the sodium silicate solution of 12 grams of urea and scheduled volume, the relative butt aluminium oxide of the silicon content in solution is made to be 0.30 quality %, stir 5 hours, add 45 grams of kerosene and 5 grams of AEOs stir 5 hours, in oil ammonia column, drip ball forming.Wet bulb solidifies 2 hours in the ammoniacal liquor of 5 quality %, then filters, and with deionized water rinsing 6 times, 80 DEG C dryings 4 hours, 100 DEG C of dryings, 12 hours, 800 DEG C roastings 3 hours, obtained siliceous γ-Al
2o
3bead.
A kind ofly prepare siliceous γ-Al
2o
3the method of bead, obtains as follows: get 200 grams of AL (OH)
3powder and appropriate amount of deionized water stir pulp, Gu liquid/mass ratio is 2, adding 10 ml volumes ratios is the dust technology of 1: 3, the sodium silicate solution of 10 grams of urea and scheduled volume, the relative butt aluminium oxide of the silicon content in solution is made to be 0.30 quality %, stir 5 hours, add 40 grams of kerosene and 5 grams of AEOs stir 5 hours, in oil ammonia column, drip ball forming.Wet bulb solidifies 2 hours in the ammoniacal liquor of 5 quality %, then filters, and with deionized water rinsing 6 times, 80 DEG C dryings 4 hours, 100 DEG C of dryings, 12 hours, 800 DEG C roastings 3 hours, obtained siliceous γ-Al
2o
3bead.
A kind ofly prepare siliceous γ-Al
2o
3the method of bead, obtains as follows: get 200 grams of AL (OH)
3powder and appropriate amount of deionized water stir pulp, Gu liquid/mass ratio is 10, adding 10 ml volumes ratios is the dust technology of 1: 3, the sodium silicate solution of 15 grams of urea and scheduled volume, the relative butt aluminium oxide of the silicon content in solution is made to be 0.30 quality %, stir 5 hours, add 50 grams of kerosene and 5 grams of AEOs stir 5 hours, in oil ammonia column, drip ball forming.Wet bulb solidifies 2 hours in the ammoniacal liquor of 5 quality %, then filters, and with deionized water rinsing 6 times, 80 DEG C dryings 4 hours, 100 DEG C of dryings, 12 hours, 800 DEG C roastings 3 hours, obtained siliceous γ-Al
2o
3bead.
Advantage of the present invention: the bead prepared by said method is applied to propane to be prepared in propylene catalyst and achieve good effect, and following instance investigates the regenerating stability of catalyst.Coke burning regeneration is the carbon deposit passed on air roasting removing catalyst at 560 DEG C, then at 600 DEG C with hydrogen reducing, recover the activity of catalyst.Catalyst after regeneration is evaluated, and finds that conversion of propane and Propylene Selectivity all achieve unexpected technique effect.
Detailed description of the invention
Embodiment 1
A kind ofly prepare siliceous γ-Al
2o
3the method of bead, obtains as follows: get 200 grams of AL (OH)
3powder and appropriate amount of deionized water stir pulp, Gu liquid/mass ratio is 2, adding 10 ml volumes ratios is the dust technology of 1: 3, the sodium silicate solution of 10 grams of urea and scheduled volume, the relative butt aluminium oxide of the silicon content in solution is made to be 0.30 quality %, stir 5 hours, add 40 grams of kerosene and 5 grams of AEOs stir 5 hours, in oil ammonia column, drip ball forming.Wet bulb solidifies 2 hours in the ammoniacal liquor of 5 quality %, then filters, and with deionized water rinsing 6 times, 80 DEG C dryings 4 hours, 100 DEG C of dryings, 12 hours, 800 DEG C roastings 3 hours, obtained siliceous γ-Al
2o
3bead.
Embodiment 2
A kind ofly prepare siliceous γ-Al
2o
3the method of bead, obtains as follows: get 200 grams of AL (OH)
3powder and appropriate amount of deionized water stir pulp, Gu liquid/mass ratio is 4, adding 10 ml volumes ratios is the dust technology of 1: 3, the sodium silicate solution of 12 grams of urea and scheduled volume, the relative butt aluminium oxide of the silicon content in solution is made to be 0.30 quality %, stir 5 hours, add 45 grams of kerosene and 5 grams of AEOs stir 5 hours, in oil ammonia column, drip ball forming.Wet bulb solidifies 2 hours in the ammoniacal liquor of 5 quality %, then filters, and with deionized water rinsing 6 times, 80 DEG C dryings 4 hours, 100 DEG C of dryings, 12 hours, 800 DEG C roastings 3 hours, obtained siliceous γ-Al
2o
3bead.
Embodiment 3
A kind ofly prepare siliceous γ-Al
2o
3the method of bead, obtains as follows: get 200 grams of AL (OH)
3powder and appropriate amount of deionized water stir pulp, Gu liquid/mass ratio is 10, adding 10 ml volumes ratios is the dust technology of 1: 3, the sodium silicate solution of 15 grams of urea and scheduled volume, the relative butt aluminium oxide of the silicon content in solution is made to be 0.30 quality %, stir 5 hours, add 50 grams of kerosene and 5 grams of AEOs stir 5 hours, in oil ammonia column, drip ball forming.Wet bulb solidifies 2 hours in the ammoniacal liquor of 5 quality %, then filters, and with deionized water rinsing 6 times, 80 DEG C dryings 4 hours, 100 DEG C of dryings, 12 hours, 800 DEG C roastings 3 hours, obtained siliceous γ-Al
2o
3bead.
Embodiment 4
A kind ofly prepare siliceous γ-Al
2o
3the method of bead, obtains as follows: get 200 grams of AL (OH)
3powder and appropriate amount of deionized water stir pulp, Gu liquid/mass ratio is 8, adding 10 ml volumes ratios is the dust technology of 1: 3, the sodium silicate solution of 14 grams of urea and scheduled volume, the relative butt aluminium oxide of the silicon content in solution is made to be 0.30 quality %, stir 5 hours, add 42 grams of kerosene and 5 grams of AEOs stir 5 hours, in oil ammonia column, drip ball forming.Wet bulb solidifies 2 hours in the ammoniacal liquor of 5 quality %, then filters, and with deionized water rinsing 6 times, 80 DEG C dryings 4 hours, 100 DEG C of dryings, 12 hours, 800 DEG C roastings 3 hours, obtained siliceous γ-Al
2o
3bead.
Embodiment 5
A kind ofly prepare siliceous γ-Al
2o
3the method of bead, obtains as follows: get 200 grams of AL (OH)
3powder and appropriate amount of deionized water stir pulp, Gu liquid/mass ratio is 10, adding 10 ml volumes ratios is the dust technology of 1: 3, the sodium silicate solution of 11 grams of urea and scheduled volume, the relative butt aluminium oxide of the silicon content in solution is made to be 0.30 quality %, stir 5 hours, add 40 grams of kerosene and 5 grams of AEOs stir 5 hours, in oil ammonia column, drip ball forming.Wet bulb solidifies 2 hours in the ammoniacal liquor of 5 quality %, then filters, and with deionized water rinsing 6 times, 80 DEG C dryings 4 hours, 100 DEG C of dryings, 12 hours, 800 DEG C roastings 3 hours, obtained siliceous γ-Al
2o
3bead.
Embodiment 6
A kind ofly prepare siliceous γ-Al
2o
3the method of bead, obtains as follows: get 200 grams of AL (OH)
3powder and appropriate amount of deionized water stir pulp, Gu liquid/mass ratio is 2, adding 10 ml volumes ratios is the dust technology of 1: 3, the sodium silicate solution of 15 grams of urea and scheduled volume, the relative butt aluminium oxide of the silicon content in solution is made to be 0.30 quality %, stir 5 hours, add 50 grams of kerosene and 5 grams of AEOs stir 5 hours, in oil ammonia column, drip ball forming.Wet bulb solidifies 2 hours in the ammoniacal liquor of 5 quality %, then filters, and with deionized water rinsing 6 times, 80 DEG C dryings 4 hours, 100 DEG C of dryings, 12 hours, 800 DEG C roastings 3 hours, obtained siliceous γ-Al
2o
3bead.
Embodiment 7
A kind ofly prepare siliceous γ-Al
2o
3the method of bead, obtains as follows: get 200 grams of AL (OH)
3powder and appropriate amount of deionized water stir pulp, Gu liquid/mass ratio is 2, adding 10 ml volumes ratios is the dust technology of 1: 3, the sodium silicate solution of 13 grams of urea and scheduled volume, the relative butt aluminium oxide of the silicon content in solution is made to be 0.30 quality %, stir 5 hours, add 49 grams of kerosene and 5 grams of AEOs stir 5 hours, in oil ammonia column, drip ball forming.Wet bulb solidifies 2 hours in the ammoniacal liquor of 5 quality %, then filters, and with deionized water rinsing 6 times, 80 DEG C dryings 4 hours, 100 DEG C of dryings, 12 hours, 800 DEG C roastings 3 hours, obtained siliceous γ-Al
2o
3bead.
Embodiment 8
A kind ofly prepare siliceous γ-Al
2o
3the method of bead, obtains as follows: get 200 grams of AL (OH)
3powder and appropriate amount of deionized water stir pulp, Gu liquid/mass ratio is 7, adding 10 ml volumes ratios is the dust technology of 1: 3, the sodium silicate solution of 14 grams of urea and scheduled volume, the relative butt aluminium oxide of the silicon content in solution is made to be 0.30 quality %, stir 5 hours, add 49.2 grams of kerosene and 5 grams of AEOs stir 5 hours, in oil ammonia column, drip ball forming.Wet bulb solidifies 2 hours in the ammoniacal liquor of 5 quality %, then filters, and with deionized water rinsing 6 times, 80 DEG C dryings 4 hours, 100 DEG C of dryings, 12 hours, 800 DEG C roastings 3 hours, obtained siliceous γ-Al
2o
3bead.
Claims (1)
1. prepare siliceous γ-Al for one kind
2o
3the method of bead, obtains as follows: get 200 grams of AL (OH)
3powder and deionized water and stirring pulp, Gu liquid/mass ratio is 3-10, adding 10 ml volumes ratios is the dust technology of 1: 3, the sodium silicate solution of 10-15 gram of urea and scheduled volume, the relative butt aluminium oxide of the silicon content in solution is made to be 0.30 quality %, stir 5 hours, add 40-50 gram of kerosene and 5 grams of AEOs stir 5 hours, ball forming is dripped in oil ammonia column, wet bulb solidifies 2 hours in the ammoniacal liquor of 5 quality %, then filter, with deionized water rinsing 6 times, 80 DEG C of dryings 4 hours, 100 DEG C of dryings 12 hours, 800 DEG C of roastings 3 hours, obtain siliceous γ-Al
2o
3bead.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510781628.4A CN105478100A (en) | 2015-11-13 | 2015-11-13 | Method for preparing silicon-containing gamma-Al2O3 microsphere |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510781628.4A CN105478100A (en) | 2015-11-13 | 2015-11-13 | Method for preparing silicon-containing gamma-Al2O3 microsphere |
Publications (1)
Publication Number | Publication Date |
---|---|
CN105478100A true CN105478100A (en) | 2016-04-13 |
Family
ID=55665585
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201510781628.4A Pending CN105478100A (en) | 2015-11-13 | 2015-11-13 | Method for preparing silicon-containing gamma-Al2O3 microsphere |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN105478100A (en) |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1465438A (en) * | 2002-06-27 | 2004-01-07 | 中国石油化工股份有限公司 | Spherical aluminium oxide carrier material and preparation process thereof |
CN1686812A (en) * | 2005-04-29 | 2005-10-26 | 邓少彬 | Method for producing alumina |
CN1958457A (en) * | 2006-10-27 | 2007-05-09 | 北京化工大学 | Round alumina of containing silicon, and preparation method |
US20140274818A1 (en) * | 2012-06-26 | 2014-09-18 | Brownwood Clay Holdings, Llc | Spherical pellets containing common clay particulate material useful as a proppant in hydraulic fracturing of oil and gas wells |
-
2015
- 2015-11-13 CN CN201510781628.4A patent/CN105478100A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1465438A (en) * | 2002-06-27 | 2004-01-07 | 中国石油化工股份有限公司 | Spherical aluminium oxide carrier material and preparation process thereof |
CN1686812A (en) * | 2005-04-29 | 2005-10-26 | 邓少彬 | Method for producing alumina |
CN1958457A (en) * | 2006-10-27 | 2007-05-09 | 北京化工大学 | Round alumina of containing silicon, and preparation method |
US20140274818A1 (en) * | 2012-06-26 | 2014-09-18 | Brownwood Clay Holdings, Llc | Spherical pellets containing common clay particulate material useful as a proppant in hydraulic fracturing of oil and gas wells |
Non-Patent Citations (1)
Title |
---|
唐博合金等: "含硅氧化铝催化剂的制备及性质", 《上海工程技术大学学报》 * |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN102451765B (en) | Preparation method for composite oxide carrier | |
CN102020289B (en) | Super-stable Y zeolite, preparation method and application thereof | |
CN103638963B (en) | P-xylene fluid catalyst prepared by performing alkylation of methylbenzene methyl alcohol and preparation method thereof | |
CN101264453A (en) | Titanium-silicon molecular sieve/tripolite composite catalyst and preparation | |
CN106881097B (en) | It is used to prepare the bismuth catalyst of copper containing carrier and preparation method thereof of 1,4- butynediols | |
CN108722408B (en) | Catalyst for synthesizing ethylene glycol by dimethyl oxalate gas phase hydrogenation and preparation method thereof | |
CN104276585B (en) | The method of a kind of compound clay microballoon in-situ crystallization synthesis NaY molecular sieve | |
JP2014509923A5 (en) | ||
CN104043477A (en) | ZSM-5/MCM-48 composite molecular sieve, preparation method and application thereof | |
CN110479251B (en) | Macroporous-mesoporous supported palladium catalyst, and preparation method and application thereof | |
CN105363456A (en) | Copper-based catalyst and preparation method and application thereof | |
WO2023036155A1 (en) | Solid base catalyst and preparation method therefor | |
CN101979136A (en) | Mesoporous composite oxide type solid super acidic catalyst and preparation method thereof | |
CN110681412A (en) | High-temperature-resistant high-activity Cu-based SCR catalyst and preparation method thereof | |
CN103406121B (en) | A kind of charcoal carries palladium oxide catalyst and its preparation method and application | |
CN106669780A (en) | Chemical type hydrocracking catalyst and preparation method thereof | |
CN103664440A (en) | Method for producing arene through conversion of methyl alcohol | |
CN107282102B (en) | Preparation method of metal-loaded molecular sieve catalyst | |
CN102773117A (en) | Medium-oil-type hydrocracking catalyst and preparation method thereof | |
CN105107491A (en) | Preparation method and application for hydrofluoroolefins hydrogenation catalyst | |
CN105983433B (en) | The method of methanol oxidation aromatic hydrocarbons, methanol arenes catalytic agent and preparation method thereof | |
CN108816227B (en) | Metal frame derived supported copper-based catalyst and preparation method thereof | |
CN104437474A (en) | Ordered mesoporous carbon material loaded platinum catalyst and application thereof to catalytic hydrogenation of aromatic nitro compound | |
CN105478100A (en) | Method for preparing silicon-containing gamma-Al2O3 microsphere | |
CN110548510A (en) | Fluidized bed ester hydrogenation Cu/SiO 2 microsphere catalyst, and preparation method and application thereof |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
WD01 | Invention patent application deemed withdrawn after publication | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20160413 |