CN1417156A - Gelatilizer with cladding layer for gelatilizing formation of silicate slurry and its prepn process - Google Patents
Gelatilizer with cladding layer for gelatilizing formation of silicate slurry and its prepn process Download PDFInfo
- Publication number
- CN1417156A CN1417156A CN 02158759 CN02158759A CN1417156A CN 1417156 A CN1417156 A CN 1417156A CN 02158759 CN02158759 CN 02158759 CN 02158759 A CN02158759 A CN 02158759A CN 1417156 A CN1417156 A CN 1417156A
- Authority
- CN
- China
- Prior art keywords
- coating layer
- jelling agent
- mixture
- hexadecanol
- silicate
- 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
- Silicates, Zeolites, And Molecular Sieves (AREA)
Abstract
The gelatilizer is one kind of inorganic solidifying agent with coating layer of paraffin or higher alcohol, e.g. hexadecanol or the mixture of hexadecanol and dodecyl alcohol. The preparation process of the gelatilizer with coating layer includes the steps of: mixing inorganic solidifying agent and surfactant homogeneously; mixing the mixture of inorganic solidifying agent and surfactant with coating layer material in a heating and stirring machine; spray pelletizing; and sieving and collecting the product gelatilizer with coating layer. The gelatilizer of the present invention has coated organic waxy coating to prevent the calcium ion in the gelatilizer from fast dissolving to slurry and thus to delay the solidification of slurry.
Description
Technical field
The present invention relates to a kind of moulding new technology of silicate ceramic mud, be specifically related to a kind of manufacture method of impelling the jelling agent and this jelling agent of silicate slurry moulding.
Background of invention
Traditional ceramic mud moulding process need be made mould with porous material (as gypsum, resin etc.), so that the moisture in the mud is discharged mould, forms base substrate.Porous material is made mould and is brought many inconvenience, increases production cost and investment in fixed assets.The silicate slurry gelatinization formation technology that Chinese patent ZL99 1 00735.2 proposes need not to use the porous material mfg. moulding die, as long as inorganic powders such as sulplo-aluminate, silicate are added in the mud as jelling agent, dissolve in by high volence metal ion in the jelling agent and to impel mud in mould, to solidify in the mud, thereby form base substrate.But because the process that above-mentioned high valence ion dissolves in the mud comparatively fast and not is subjected to Artificial Control, whole moulding process has only the time of several minutes, and this brings very big inconvenience to forming operation, even can't operate.
Summary of the invention
Too fast at above jelling agent setting rate, molding time is too short, operate uppity problem, and main purpose of the present invention is to provide a kind of jelling agent with coating layer that can delay and control the mud setting time.
The present invention provides a kind of above-mentioned method with jelling agent of coating layer for preparing simultaneously.
The present invention at first provides a kind of jelling agent with coating layer that is used for silicate slurry gelling moulding, and it is a kind of outer inorganic peptizer that coating layer is arranged, and described coating layer is paraffin or higher alcohols.
The above-mentioned jelling agent with coating layer that is used for silicate slurry gelling moulding, described inorganic peptizer and coating layer ratio of weight and number are 100: 75 ~ 100.
The above-mentioned jelling agent with coating layer that is used for silicate slurry gelling moulding, described higher alcohols is the mixture of hexadecanol or hexadecanol and lauryl alcohol.
The above-mentioned jelling agent with coating layer that is used for silicate slurry gelling moulding, described hexadecanol and lauryl alcohol blended ratio of weight and number are 100: 0 ~ 27.
The above-mentioned jelling agent with coating layer that is used for silicate slurry gelling moulding, described inorganic peptizer are independent or blended calcium sulphoaluminate, calcium aluminate, Calucium Silicate powder and silicon oxide.
The above-mentioned jelling agent with coating layer that is used for silicate slurry gelling moulding, the chemical constitution of described inorganic peptizer is Al
2O
3: 0-55%, CaO:30-70%, SiO
2: 0-40%, SO
3: 0-13%.
The described preparation method with jelling agent of coating layer of a kind of claim 1-6 provided by the invention comprises the steps:
1). inorganic peptizer is mixed with tensio-active agent;
2). the mixture of step 1) is mixed in the Mixing Machine of heating with coating layer material;
3). with step 2) mixture add in the sponging granulator and carry out mist projection granulating;
4). the tablets press product is sieved, and collection screen powder off the net obtains the jelling agent that product has coating layer.
Among the preparation method of above-mentioned jelling agent with coating layer, described tensio-active agent is the mixture of oleic acid or vinyltriethoxysilane or vinyltriethoxysilane and ethylene glycol.
Among the preparation method of above-mentioned jelling agent with coating layer, described inorganic peptizer is separately or blended calcium sulphoaluminate, calcium aluminate, Calucium Silicate powder and silicon oxide, and described coating layer is paraffin or higher alcohols.
Described tensio-active agent is the mixture of oleic acid or vinyltriethoxysilane or vinyltriethoxysilane and ethylene glycol, described inorganic peptizer is independent or blended calcium sulphoaluminate, calcium aluminate, Calucium Silicate powder and silicon oxide, described coating layer is paraffin or higher alcohols, and described higher alcohols is that hexadecanol or hexadecanol and lauryl alcohol are 100 by ratio of weight and the number of copies: the mixture of (0 ~ 27); Described mesh size is 0.1 millimeter.
According to technique scheme, the present invention proposes to coat organic wax coating on the jelling agent surface, prevents that the calcium ion in the jelling agent from dissolving in the mud very soon, thereby has delayed the setting time of mud.This wax protective layer can melt at a certain temperature; calcium ion in the jelling agent of protective layer fusing back can dissolve in the mud very soon; impel mud to solidify; therefore can play the effect of control mud setting time by the temperature that changes mud; make this moulding process artificially to regulate, made things convenient for forming operation.
Embodiment
The present invention is one of achievement in research of national natural science fund subsidy project " research of silicate ceramics slip casting gelling moulding mechanism " (contract number 59972032).For opener, below be described in detail the present invention with specific embodiment.
Inorganic gel agent used among the present invention is calcium sulphoaluminate, calcium aluminate, Calucium Silicate powder, makes protective layer with paraffin, because paraffin is 55-60 ℃ of fusing, therefore mud is heated to and can triggers mud more than 60 ℃ and solidify.This protective layer is fit to the high place of temperature and uses.The ground low at temperature can will trigger temperature design between 40-50 ℃; protective layer can be selected hexadecanol (fusing point is 50 ℃) for use; or by in hexadecanol, dissolving in an amount of lauryl alcohol (fusing point is 22 ℃); the fusing point of mixture is set between 40-50 ℃, and the lauryl alcohol content fusing point of polyhybrid thing more is low more.The fusing point design is being inappropriate below 40 ℃, because can soften near wax coating layer in the room temp occasion, in addition local melting, causing the mutual adhesion of jelling agent particle easily, can't disperse.
The inorganic gel agent needs at first to mix with an amount of tensio-active agent; same again organic protective agent (paraffin or higher alcohols) mixes in the stirring mill of heating; mixture is poured in the storage tank of sponging granulator; utilize pressurized air; make mixed stream be sent into forth fine drop, and then be cooled to powder.Example 1:
100 gram calcium sulphoaluminate powders mix in mortar with 8 gram oleic acid; mixed 4 hours in the stirring mill of heating with 100 gram melt paraffins again; pour into then in the storage tank of sponging granulator; with 0.2MPa pressurized air mist projection granulating; sieve by aperture 0.1mm screen cloth, collected powder is standby.
The preparation solid load is the silicate ceramic mud of 77% (weight), takes by weighing 100 gram mud, adds the above-mentioned coating jelling agent powder of 6 grams, stirs, and pours in the mould of plastics.This mud that coats jelling agent that contains is placed and was still had flowability in 60 minutes, but places 40 minutes in 70 ℃ of baking ovens, and mud promptly solidifies fully.
In contrast, add uncoated calcium sulphoaluminate powder 1 gram in 100 same gram silicate slurries, stir promptly began to solidify in back 1.5 minutes.Example 2:
100 gram calcium aluminate powders mix in mortar with 8 gram vinyltriethoxysilanes; mixed 4 hours in the stirring mill of heating with 95 gram fusion hexadecanols again; pour into then in the storage tank of sponging granulator; with 0.2MPa pressurized air mist projection granulating; sieve by aperture 0.1mm screen cloth, collected powder is standby.
The preparation solid load is the silicate ceramic mud of 77% (weight), takes by weighing 100 gram mud, adds the above-mentioned coating jelling agent powder of 8 grams, stirs, and pours in the mould of plastics.This mud that coats jelling agent that contains is placed and was still had flowability in 60 minutes, but places 40 minutes in 60 ℃ of baking ovens, and mud promptly solidifies fully.
Reference examples: add uncoated calcium aluminate powder 4 grams in 100 same gram silicate slurries, stir promptly began to solidify in back 5 minutes.Example 3:
100 gram Calucium Silicate powder powders mix in mortar with 8 gram vinyltriethoxysilanes and 1 gram ethylene glycol; (wherein lauryl alcohol 12 restrains for same again 80 gram fused lauryl alcohols and hexadecanol mixture; hexadecanol 68 grams) in the stirring mill of heating, mixed 4 hours; pour into then in the storage tank of sponging granulator; with 0.2MPa pressurized air mist projection granulating; sieve by aperture 0.1mm screen cloth, collected powder is standby.
The preparation solid load is the silicate ceramic mud of 77% (weight), takes by weighing 100 gram mud, adds the above-mentioned coating jelling agent powder of 5 grams, stirs, and pours in the mould of plastics.This mud that coats jelling agent that contains is placed and was still had flowability in 40 minutes, but places 30 minutes in 55 ℃ of baking ovens, and mud promptly solidifies fully.
Reference examples: add uncoated Calucium Silicate powder powder 1 gram in 100 same gram silicate slurries, stir promptly began to solidify in back 1 minute.Example 4:
20 gram silicon oxide and 80 gram Calucium Silicate powder powders mix in mortar with 8 gram oleic acid; mixed 4 hours in the stirring mill of heating with 90 gram melt paraffins again; pour into then in the storage tank of sponging granulator; with 0.2MPa pressurized air mist projection granulating; sieve by aperture 0.1mm screen cloth, collected powder is standby.
The preparation solid load is the silicate ceramic mud of 77% (weight), takes by weighing 100 gram mud, adds the above-mentioned coating jelling agent powder of 5 grams, stirs, and pours in the mould of plastics.This mud that coats jelling agent that contains is placed and was still had flowability in 50 minutes, but places 30 minutes in 70 ℃ of baking ovens, and mud promptly solidifies fully.
Reference examples: add uncoated Calucium Silicate powder and silicon oxide powder 1 gram in 100 same gram silicate slurries, stir promptly began to solidify in back 3 minutes.Example 5:
90 gram calcium sulphoaluminates and 10 gram silicon oxide powders mix in mortar with 8 gram vinyltriethoxysilanes; mixed 4 hours in the stirring mill of heating with 75 gram fused lauryl alcohols and hexadecanol mixture (wherein lauryl alcohol 16 grams, hexadecanol 59 grams) again; pour into then in the storage tank of sponging granulator; with 0.2MPa pressurized air mist projection granulating; sieve by aperture 0.1mm screen cloth, collected powder is standby.
The preparation solid load is the silicate ceramic mud of 77% (weight), takes by weighing 100 gram mud, adds the above-mentioned coating jelling agent powder of 6 grams, stirs, and pours in the mould of plastics.This mud that coats jelling agent that contains is placed and was still had flowability in 60 minutes, but places 40 minutes in 45 ℃ of baking ovens, and mud promptly solidifies fully.
Reference examples: add uncoated silicon oxide and calcium sulphoaluminate powder 2 grams in 100 same gram silicate slurries, stir promptly began to solidify in back 4 minutes.
Claims (10)
1, a kind of jelling agent with coating layer that is used for silicate slurry gelling moulding is characterized in that: it is a kind of outer inorganic peptizer that coating layer is arranged, and described coating layer is paraffin or higher alcohols.
2, the jelling agent with coating layer that is used for silicate slurry gelling moulding according to claim 1, it is characterized in that: described inorganic peptizer and coating layer ratio of weight and number are 100: 75 ~ 100.
3, the jelling agent with coating layer that is used for silicate slurry gelling moulding according to claim 1 and 2, it is characterized in that: described higher alcohols is the mixture of hexadecanol or hexadecanol and lauryl alcohol.
4, the jelling agent with coating layer that is used for silicate slurry gelling moulding according to claim 3 is characterized in that: described hexadecanol and lauryl alcohol blended ratio of weight and number are 100: 0 ~ 27.
5, the jelling agent with coating layer that is used for silicate slurry gelling moulding according to claim 1 and 2 is characterized in that: described inorganic peptizer is independent or blended calcium sulphoaluminate, calcium aluminate, Calucium Silicate powder and silicon oxide.
6, the jelling agent with coating layer that is used for silicate slurry gelling moulding according to claim 5, it is characterized in that: the chemical constitution of described inorganic peptizer is Al
2O
3: 0-55%, CaO:30-70%, SiO
2: 0-40%, SO
3: 0-13%.
7, the described preparation method with jelling agent of coating layer of a kind of claim 1-6 comprises the steps:
1). inorganic peptizer is mixed with tensio-active agent;
2). the mixture of step 1) is mixed in the Mixing Machine of heating with coating layer material;
3). with step 2) mixture add in the sponging granulator and carry out mist projection granulating;
4). the tablets press product is sieved, and collection screen powder off the net obtains the jelling agent that product has coating layer.
8, the preparation method with jelling agent of coating layer as claimed in claim 7 is characterized in that: described tensio-active agent is the mixture of oleic acid or vinyltriethoxysilane or vinyltriethoxysilane and ethylene glycol.
9, the preparation method with jelling agent of coating layer as claimed in claim 7 is characterized in that: described inorganic peptizer is independent or blended calcium sulphoaluminate, calcium aluminate, Calucium Silicate powder and silicon oxide, and described coating layer is paraffin or higher alcohols.
10, the preparation method with jelling agent of coating layer as claimed in claim 7, it is characterized in that: described tensio-active agent is the mixture of oleic acid or vinyltriethoxysilane or vinyltriethoxysilane and ethylene glycol, described inorganic peptizer is independent or blended calcium sulphoaluminate, calcium aluminate, Calucium Silicate powder and silicon oxide, described coating layer is paraffin or higher alcohols, and described higher alcohols is that hexadecanol or hexadecanol and lauryl alcohol are 100 by ratio of weight and the number of copies: the mixture of (0 ~ 27); Described mesh size is 0.1 millimeter.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 02158759 CN1237023C (en) | 2002-12-26 | 2002-12-26 | Gelatilizer with cladding layer for gelatilizing formation of silicate slurry and its prepn process |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 02158759 CN1237023C (en) | 2002-12-26 | 2002-12-26 | Gelatilizer with cladding layer for gelatilizing formation of silicate slurry and its prepn process |
Publications (2)
Publication Number | Publication Date |
---|---|
CN1417156A true CN1417156A (en) | 2003-05-14 |
CN1237023C CN1237023C (en) | 2006-01-18 |
Family
ID=4753181
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 02158759 Expired - Fee Related CN1237023C (en) | 2002-12-26 | 2002-12-26 | Gelatilizer with cladding layer for gelatilizing formation of silicate slurry and its prepn process |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN1237023C (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108774015A (en) * | 2018-06-12 | 2018-11-09 | 金华市欣生沸石开发有限公司 | The preparation method of zeolite base heat of hydration slow-release material |
CN108947297A (en) * | 2018-06-12 | 2018-12-07 | 金华市欣生沸石开发有限公司 | Zeolite base heat of hydration slow-release material |
-
2002
- 2002-12-26 CN CN 02158759 patent/CN1237023C/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108774015A (en) * | 2018-06-12 | 2018-11-09 | 金华市欣生沸石开发有限公司 | The preparation method of zeolite base heat of hydration slow-release material |
CN108947297A (en) * | 2018-06-12 | 2018-12-07 | 金华市欣生沸石开发有限公司 | Zeolite base heat of hydration slow-release material |
CN108774015B (en) * | 2018-06-12 | 2021-04-02 | 金华市欣生沸石开发有限公司 | Preparation method of zeolite-based hydration heat slow-release material |
CN108947297B (en) * | 2018-06-12 | 2021-04-02 | 金华市欣生沸石开发有限公司 | Zeolite-based hydration heat slow-release material |
Also Published As
Publication number | Publication date |
---|---|
CN1237023C (en) | 2006-01-18 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JPH0314515B2 (en) | ||
WO1997003112A1 (en) | Powdery material and modifier for cementitious material | |
JPH0323214A (en) | Spherical particles of oxide of rare earth element and production thereof | |
CN114436578A (en) | Controlled-release quick-setting functional particles and application thereof in 3D printing of cement-based materials | |
CN1237023C (en) | Gelatilizer with cladding layer for gelatilizing formation of silicate slurry and its prepn process | |
CA1058792A (en) | Method of manufacturing constructional units | |
JP6056716B2 (en) | Granule, method for producing the same, and method for producing glass article | |
JP6350531B2 (en) | Granule, method for producing the same, and method for producing glass article | |
CN106045351A (en) | Water-granulated-slag-based oxalate chemical bonding material and application thereof | |
CN111606617A (en) | Tuff geopolymer composite material and preparation method thereof | |
CN110156382A (en) | Curing agent composition and preparation method thereof and environmentally friendly structural material comprising it | |
US5804154A (en) | Process for the production of a silica-substance containing materials and materials produced therefrom | |
JPS63262453A (en) | Ceramic-glass particle for thermal spraying and its production | |
JPH09124378A (en) | Formed lightweight cement its production | |
CN106278308A (en) | A kind of add the method that zirconium oxide metering nozzle prepared by magnesium-rich spinel micropowder | |
CN1113831C (en) | In-situ synthesis process for preparing complex-phase TiN/O'-sialon material | |
JP4047956B2 (en) | Method for forming silicon carbide powder | |
JP2002020145A (en) | Steelmaking slag treatment process for producing aggregate from steelmaking slag | |
JP2632252B2 (en) | Artificial stone | |
JP3176919B2 (en) | Spherical hydraulic substance and method for producing the same | |
JPH07206537A (en) | Porous concrete and production of molded article thereof | |
JP3839626B2 (en) | Resin-containing wax spherical granules and method for producing the same, and ceramic molded body and method for producing the same | |
CN102167526A (en) | Low-shrink alkali slag cement composition and preparation method thereof | |
JP4382937B2 (en) | Method for producing coal-ash quality artificial aggregate | |
JP2818235B2 (en) | Spherical cement and its production method |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20060118 Termination date: 20111226 |