CN1363514A - macroreticular silica gel and its preparing process - Google Patents
macroreticular silica gel and its preparing process Download PDFInfo
- Publication number
- CN1363514A CN1363514A CN 01100425 CN01100425A CN1363514A CN 1363514 A CN1363514 A CN 1363514A CN 01100425 CN01100425 CN 01100425 CN 01100425 A CN01100425 A CN 01100425A CN 1363514 A CN1363514 A CN 1363514A
- Authority
- CN
- China
- Prior art keywords
- silica gel
- soak
- salt
- macroporous silica
- manufacture method
- 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.)
- Granted
Links
Landscapes
- Silicon Compounds (AREA)
Abstract
A process for preparing maroreticular silica gel includes such steps as reaction of sodium silicate solution on diluted sulfuric acid to obtain n-silicic acid, coagulating, breaking, granulating, washing in water, immersing in alkali solution, treating with steam, immersing in salt solution and baking. Its resultant product has 10-60 nm of average pore diameter, 250-350 sq.m/g of average specific surface area, and 1-2 ml/g and average pure volume.
Description
The present invention relates to silica gel and production technique thereof, specifically is a kind of macroporous silica gel, and it belongs to technical field of inorganic chemical industry.
Silica gel generally is divided into silochrom and Kiselgel A with its aperture difference, and wherein the aperture of silochrom is generally: 8-10nm; The aperture of Kiselgel A is generally: 1-4nm.Also have a kind ofly by the disclosed macroporous silica gel of CN1157260 document, its aperture is generally: 20-15000nm.This silica gel is in manufacture method, is scattered in the water-insoluble solid particle in the alkaline silicate solution or in the mineral acid, utilizes the reaming promoter action of solids, realizes increasing significantly the purpose in silica gel aperture.Yet, require to use the solids of strict grain graininess and the alkaline silicate solution and the mineral acid of use should have the following viscosity of 20 centipoises in this manufacture method.The raw materials technology preparation trouble of this manufacture method, the processing requirement height is unfavorable for scale production in enormous quantities.
The purpose of this invention is to provide a kind of macroporous silica gel and manufacture method thereof.The physical and chemical performance of this silica gel is: mean pore size is at 10-60nm, average specific surface area 250-350m
2/ g, average pore volume 1.00-2.00ml/g.The manufacture method of this silica gel is on the basis of traditional silica gel production method, what keep traditional technology generates positive silicic acid by sodium silicate solution and dilute sulphuric acid in reactor, solidify through leaving standstill again-→ broken granulation-→ washing-→ treatment process that alkali bubble is handled, design after chambering process handle, make the physical and chemical performance of this silica gel reach aforementioned index request.
Task of the present invention is realized by following technical scheme, has developed a kind of macroporous silica gel, and its outward appearance is irregular bulk, spherical opal glass shape particle.The physical and chemical performance of this silica gel is: mean pore size is at 10-60nm, average specific surface area 250-350m
2/ g, average pore volume 1.00-2.00ml/g.
The manufacture method of this macroporous silica gel, it generates positive silicic acid by sodium silicate solution and dilute sulphuric acid in reactor, by traditional adhesive-preparing technology, solidify through leaving standstill-→ broken granulation-→ washing-→ processing of alkali bubble, treatment process afterwards is:
A, steam treatment, the alkali lye that is about to soak bleeds off, and from the washing bath bottom, wet micelle is heaped layer feed steam;
B, soak salt and handle, what be about to steam treatment should wet micelle, places content 0.01-0.7% (W/L) salts solution to soak; Through traditional stoving process, make the finished product macroporous silica gel again.
The processing condition of the described A of the manufacture method of this macroporous silica gel, step steam treatment are: the vapour pressure that feeds steam is: 0.1-0.3MPa, and 80-120 ℃ of control heap glue temperature, logical vapour time 2-25hr, this wet micelle heap layer thickness and are: 10-3500mm.
The described B of the manufacture method of this macroporous silica gel, step are soaked the soak time 4-40hr of salt treatment process, temperature 20-70 ℃ of controlling soak solution.
The described B of the manufacture method of this hole silica gel, step are soaked the salts solution of salt treatment process, and salt wherein is: zirconates, or aluminium salt, or zinc salt, or lithium salts.
The described silica gel of this macroporous silica gel is to generate positive silicic acid by sodium silicate solution and dilute sulphuric acid in reactor, by traditional adhesive-preparing technology, solidify through leaving standstill-→ broken granulation-→ washing-→ processing of alkali bubble-→ steam treatment-→ soak salt to handle, handle through traditional stoving process again, the physical and chemical performance that makes macroporous silica gel is: mean pore size is at 10-60nm, average specific surface area 250-350m
2/ g, average pore volume 1.00-2.00ml/g.
The invention has the advantages that: because the reaming aftertreatment technology that the present invention adopts, promptly steam treatment and soak salt and handle makes the physical and chemical performance of this silica gel reach mean pore size at 10-60nm, average specific surface area 250-350m
2/ g, the index request of average pore volume 1.00-2.00ml/g.Whole technological process all is to carry out under normal pressure, need not high-temperature roasting, need not service requirements strict process raw material, as the raw materials technology that need not to use the viscosity of the solids of strict grain graininess and reaction solution to require.Steam treatment of the present invention designs from strengthening virgin rubber framework deformation resistibility.Micelle rearrangement, all SiO of virgin rubber inside may take place in the hydrogel of virgin rubber in the steam treatment process
4Structure interacts with the water molecules with certain energy (gasification energy) between the tetrahedron particle, condensation can take place grow up.This SiO
4Rearrangement between the water molecules of tetrahedron particle and gasification energy may make the skeleton of virgin rubber obtain strong solid.This rearrangement result also carries out the basis for next step soaks the salt processing simultaneously.It is of the present invention that to soak that salt handles be that elite metal ion is in certain soak time, by metal ion and SiO
4The end group of tetrahedron particle is had an effect, and makes the intensity that connects further raising virgin rubber skeleton between all this particles each other, thereby has determined the macroporous structure of virgin rubber skeleton.Through traditional stoving process, the macroporous structure of silica gel is fixed up at last again.The present invention has simplified traditional silica gel production process, produces the qualified macroporous silica gel of physical and chemical performance on the production unit of common silochrom.Manufacture method of the present invention is simple, is easy to scale production.
Protection scope of the present invention not only is confined in following examples.
The embodiment of macroporous silica gel of the present invention is to explanation of the present invention.Formulation content is 20% ± 0.5% sodium silicate solution on the production unit of common silochrom, with formulation content be that 20% sulphuric acid soln reacts and makes virgin rubber: control glue reaction pressure is at 0.28-0.4Mpa, and temperature of reaction is at 25 ± 5 ℃; Through the aging Gel Treatment that leaves standstill: the gel water temperature is at 25-40 ℃, and aging time of repose is at 32-40hr, pH value 1.0-3.0; Through rubber tapping crusher machine granulation: make irregular bulk or spherical opal glass shape particle less than 4cm; Handle through washing: control water temperature is at 55-60 ℃ again, pH value 〉=5.3; Handle through the alkali bubble then: the caustic soda soln with pH value 8.0 soaks 32hr, keeps 30 ± 5 ℃ of solution temperatures, again through steam treatment and the aftertreatment technology that soaks the salt processing, its experimental data such as following table 1, table 2.This silica gel of aftertreatment is handled through 120 ℃ ± 5 ℃ indoor oven dry, gets the macroporous silica gel of water content≤4%.Table 1: the aftertreatment embodiment table of macroporous silica gel;
Annotate: (6)-(20) are expressed as experiment number; Zirconates is: zirconium sulfate, aluminium salt is: Tai-Ace S 150, zinc salt is: zinc sulfate, lithium salts is: lithium chloride.Table 2: the physical and chemical performance table of macroporous silica gel embodiment;
| (connect table content :) | Mean pore size nm | Average specific surface area m 2/g | Average pore volume ml/g |
| ????12 | ????18.7 | ????295 | ????1.38 |
| ????13 | ????13.3 | ????325 | ????1.08 |
| ????14 | ????20.3 | ????287 | ????1.46 |
| ????15 | ????24.5 | ????262 | ????1.61 |
| ????16 | ????10.7 | ????344 | ????0.92 |
| ????17 | ????15.6 | ????293 | ????1.15 |
| ????18 | ????12.6 | ????328 | ????1.03 |
| ????19 | ????14.9 | ????298 | ????1.11 |
| ????20 | ????18.8 | ????290 | ????1.40 |
Annotate: the physical and chemical performance testing method in the table 2 adopts the test method of the relevant chapters and sections of HG/T2765.5, and the instrument that is adopted is: specific surface area, the pore analysis instrument of the SA3100 type that U.S. Beckman company produces.
Claims (6)
1, a kind of macroporous silica gel, its outward appearance are irregular bulk, spherical opal glass shape particle, and it is characterized in that: the physical and chemical performance of this silica gel is: mean pore size is at 10-60nm, average specific surface area 250-350m
2/ g, average pore volume 1.00-2.00ml/g.
2, according to the manufacture method of the described macroporous silica gel of claim 1, it generates positive silicic acid by sodium silicate solution and dilute sulphuric acid in reactor, by traditional adhesive-preparing technology, solidify through leaving standstill-→ broken granulation-→ washing-→ processing of alkali bubble, treatment process afterwards is characterized in that:
A, steam treatment, the alkali lye that is about to soak bleeds off, and from the washing bath bottom, wet micelle is heaped layer feed steam;
B, soak salt and handle, what be about to steam treatment should wet micelle, places content 0.01-0.7% (W/L) salts solution to soak; Through traditional stoving process, make the finished product macroporous silica gel again.
3, according to the manufacture method of the described macroporous silica gel of claim 2, it is characterized in that: the processing condition of described A, steam treatment are: the vapour pressure that feeds steam is: 0.1-0.3MPa, 80-120 ℃ of control heap glue temperature, logical vapour time 2-25hr, this wet micelle heap layer thickness and are: 10-3500mm.
4, according to the manufacture method of the described macroporous silica gel of claim 2, it is characterized in that: described B, soak the soak time 4-40hr of salt treatment process, temperature 20-70 ℃ of control soak solution.
5, according to the manufacture method of claim 2 and 4 described macroporous silica gels, it is characterized in that: described B, soak the salts solution of salt treatment process, salt wherein is: zirconates, or aluminium salt, or zinc salt, or lithium salts.
6, according to claim 1 and 2 described macroporous silica gels, it is characterized in that: described silica gel is to generate positive silicic acid by sodium silicate solution and dilute sulphuric acid in reactor, by traditional adhesive-preparing technology, solidify through leaving standstill-→ broken granulation-→ washing-→ processing of alkali bubble-→ steam treatment-→ soak salt to handle, handle through traditional stoving process again, the physical and chemical performance that makes macroporous silica gel is: mean pore size is at 10-60nm, average specific surface area 250-350m
2/ g, average pore volume 1.00-2.00ml/g.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB011004258A CN1186254C (en) | 2001-01-11 | 2001-01-11 | macroreticular silica gel and its preparing process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB011004258A CN1186254C (en) | 2001-01-11 | 2001-01-11 | macroreticular silica gel and its preparing process |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1363514A true CN1363514A (en) | 2002-08-14 |
| CN1186254C CN1186254C (en) | 2005-01-26 |
Family
ID=4651581
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB011004258A Expired - Lifetime CN1186254C (en) | 2001-01-11 | 2001-01-11 | macroreticular silica gel and its preparing process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1186254C (en) |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100337912C (en) * | 2005-12-23 | 2007-09-19 | 李永兆 | Process for mfg. water resisting type large pore spherical silica gel |
| CN100376480C (en) * | 2003-02-21 | 2008-03-26 | 青岛海洋化工有限公司 | Production of macroporous silica gel |
| CN100445360C (en) * | 2006-10-13 | 2008-12-24 | 李永兆 | Vinegar clarifying agent and method for treating vinegar precipitate |
| CN101205066B (en) * | 2007-12-17 | 2010-06-02 | 李永兆 | Macroporous microsphere silica gel preparation thereof |
| CN103030150A (en) * | 2012-12-26 | 2013-04-10 | 青岛中能集团有限公司 | Technological process of mesoporous silica gel |
| CN103043670A (en) * | 2012-12-26 | 2013-04-17 | 青岛中能集团有限公司 | Process flow of novel water-absorbent silica gel |
| CN103043669A (en) * | 2012-12-26 | 2013-04-17 | 青岛中能集团有限公司 | Microporous silica gel preparing flow |
| CN103769226A (en) * | 2012-10-24 | 2014-05-07 | 中国石油化工股份有限公司 | Silica gel carrier, and preparation method and applications thereof |
| CN112717874A (en) * | 2020-12-08 | 2021-04-30 | 福建南平三元循环技术有限公司 | Novel reaming manufacturing method of macroporous silica gel |
| CN113908798A (en) * | 2021-07-30 | 2022-01-11 | 冷水江三A新材料科技有限公司 | Preparation method of silicon dioxide for edible oil refining agent |
| CN115219490A (en) * | 2022-08-05 | 2022-10-21 | 青岛美高集团有限公司 | PH color-changing indicating silica gel and preparation method thereof |
-
2001
- 2001-01-11 CN CNB011004258A patent/CN1186254C/en not_active Expired - Lifetime
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100376480C (en) * | 2003-02-21 | 2008-03-26 | 青岛海洋化工有限公司 | Production of macroporous silica gel |
| CN100337912C (en) * | 2005-12-23 | 2007-09-19 | 李永兆 | Process for mfg. water resisting type large pore spherical silica gel |
| CN100445360C (en) * | 2006-10-13 | 2008-12-24 | 李永兆 | Vinegar clarifying agent and method for treating vinegar precipitate |
| CN101205066B (en) * | 2007-12-17 | 2010-06-02 | 李永兆 | Macroporous microsphere silica gel preparation thereof |
| CN103769226B (en) * | 2012-10-24 | 2015-09-30 | 中国石油化工股份有限公司 | A kind of silica-gel carrier and its preparation method and application |
| CN103769226A (en) * | 2012-10-24 | 2014-05-07 | 中国石油化工股份有限公司 | Silica gel carrier, and preparation method and applications thereof |
| CN103043669A (en) * | 2012-12-26 | 2013-04-17 | 青岛中能集团有限公司 | Microporous silica gel preparing flow |
| CN103043670A (en) * | 2012-12-26 | 2013-04-17 | 青岛中能集团有限公司 | Process flow of novel water-absorbent silica gel |
| CN103030150A (en) * | 2012-12-26 | 2013-04-10 | 青岛中能集团有限公司 | Technological process of mesoporous silica gel |
| CN112717874A (en) * | 2020-12-08 | 2021-04-30 | 福建南平三元循环技术有限公司 | Novel reaming manufacturing method of macroporous silica gel |
| CN113908798A (en) * | 2021-07-30 | 2022-01-11 | 冷水江三A新材料科技有限公司 | Preparation method of silicon dioxide for edible oil refining agent |
| CN115219490A (en) * | 2022-08-05 | 2022-10-21 | 青岛美高集团有限公司 | PH color-changing indicating silica gel and preparation method thereof |
| WO2024027848A1 (en) * | 2022-08-05 | 2024-02-08 | 青岛美高集团有限公司 | Color-changing ph-indicating silica gel and preparation method therefor |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1186254C (en) | 2005-01-26 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101830474B (en) | Method for preparing white carbon black | |
| CN1186254C (en) | macroreticular silica gel and its preparing process | |
| CN101244825A (en) | Method for producing silicon dioxide silica aerogel with tripolite as raw material | |
| CN101053819B (en) | Method for producing variable-pressure adsorption silica gel | |
| CN106829975B (en) | A kind of preparation method of green tire high-dispersion white carbon black | |
| CN108101068A (en) | A kind of high degree of structuration, the preparation method of high-reinforcement white carbon black and white carbon therefrom | |
| CN106167581A (en) | A kind of preparation method of antibacterial polypropylene | |
| JPH0479976B2 (en) | ||
| CN109012517B (en) | Method for preparing composite silicon-based aerogel by taking iron tailings as raw materials | |
| CN102500315A (en) | LiX molecular sieve adsorbent and preparation method thereof | |
| CN1522958A (en) | Process for manufacturing macroreticular spherical silica gel | |
| CN1291916C (en) | Process for preparing fluorine reducing ion sieve of aquatic body | |
| CN117680088A (en) | Water remover and preparation method and application thereof | |
| CN109205619A (en) | Method for extracting and utilizing main components of rice hulls step by step | |
| CN101760242B (en) | Continuous stripping process and device for chlorinated paraffin | |
| CN104014300B (en) | Diatomite preparation is with the method for drainage functional beer stabilizing agent | |
| CN110589943A (en) | Method for treating chromium-containing wastewater through gelation and additive for glass obtained by method | |
| CN216879352U (en) | A recovery unit for handling reation kettle contains sulphur tail gas | |
| CN1669927A (en) | Method for preparing nano 4A zeolite using gangue as raw material | |
| CN108975341A (en) | Using the precipitation method prepare silica method and its silica obtained | |
| CN111807377B (en) | White carbon black for improving winter tire performance | |
| CN100348495C (en) | Method of producing aluminium fluoride | |
| CN103043670A (en) | Process flow of novel water-absorbent silica gel | |
| CN113908798A (en) | Preparation method of silicon dioxide for edible oil refining agent | |
| CN103030150A (en) | Technological process of mesoporous silica gel |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C06 | Publication | ||
| PB01 | Publication | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20050126 |