CN1105654A - Method for making ceramic whitening agent by using deactivated low-temp. conversion catalyst and its products - Google Patents
Method for making ceramic whitening agent by using deactivated low-temp. conversion catalyst and its products Download PDFInfo
- Publication number
- CN1105654A CN1105654A CN 94100470 CN94100470A CN1105654A CN 1105654 A CN1105654 A CN 1105654A CN 94100470 CN94100470 CN 94100470 CN 94100470 A CN94100470 A CN 94100470A CN 1105654 A CN1105654 A CN 1105654A
- Authority
- CN
- China
- Prior art keywords
- whitening agent
- temp
- inactivation
- products
- low temperature
- 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
Landscapes
- Processing Of Solid Wastes (AREA)
- Catalysts (AREA)
Abstract
The present invention relates to a method for preparing ceramic whitening agent by using deactivated low-temp. transformation catalyst and its product. Said method is as follows: the low-temp. transformation catalyst waste residue is passed through such processes of hand-selecting, removing impurity, pulverizing and screening, and then fed into a high-temp. furnace to make calcination for 2-5 h., and its calcination temp. is controlled within 400-1400 deg.C, and then the above-mentioned material is discharged from furnace, and cooled to normal temp. Besides, in the material passed through the processes of hand-selecting and removing impurity, a rare earth synergistic solution is injected, and then the above-mentioned material is fed into the high-temp. furnace to make calcination said invention can change the industrial waste residue into in dustrial raw material, and its obtained product can resist high-temp. of above 1300 deg.C, and its whitening effect is notale.
Description
The present invention relates to a kind of manufacture method of ceramic whitening agent, especially a kind ofly utilize low temperature (containing wide temperature) the transformation catalyst waste residue behind the inactivation to make method of ceramic whitening agent and products thereof.
In recent years, some chemical plant, as being the synthesis ammonia plant etc. of raw material with the coal, for energy-conservation numerous and confused employing low temperature (containing wide temperature) transformation catalyst, this catalyzer just becomes industrial residue through producing after using inactivation, needs a large amount of manpower and materials of cost remove to handle these waste residues.
Once there was the ceramic whitening agent of trial sale to occur on the market, but all can not be high temperature resistant, so do not have whitening effect.
The object of the present invention is to provide that a kind of to utilize low temperature (containing wide temperature) the transformation catalyst waste residue behind the inactivation be raw material, manufacturing can be high temperature resistant, has the method and products thereof of the ceramic whitening agent of tangible whitening effect.
Technical solution of the present invention is:
A. the low temperature shift catalyst waste residue behind the inactivation is carried out picking, removes dirty foreign material wherein, pulverize with pulverizer again, cross 60~120 mesh sieves,
B. the material after above-mentioned the sieving is sent in the high-temperature calcination stove and calcined 2~5 hours under the condition that has air to exist, calcining temperature is controlled at 400~1400 ℃,
C. the material after the above-mentioned calcining is come out of the stove and reduce to normal temperature, promptly obtain finished product.
In the present invention, being preferably in the material behind the crushing screening is 0.1~0.2 with the ratio with material equably: ratio spray concentration 1(weight) is 10~15%(weight) rare earths salt, send into again in the high-temperature calcination stove and calcine.
In the present invention, calcining temperature is controlled at 650~1200 ℃ more satisfactory.
In the present invention, also the low temperature shift catalyst waste residue behind the inactivation can be carried out not pulverizing earlier after the picking removal of impurities, add rare earths salt or do not spray rare earths salt, send in the High Temperature Furnaces Heating Apparatus and calcine, reduce to normal temperature after calcining is come out of the stove, use the pulverizer crushing screening again, obtain finished product.
The low temperature shift catalyst of Shi Yonging mainly is meant various Co-Mo sulfur-tolerant shift catalysts in the present invention, as LHB301 low temperature sulfur-resistant transformation catalyst; B301, B302Q, each molded breadth temperature sulfur-resistant transformation catalyst of B303Q; And the K8-11 type co-mo antisulphuric transforming catalyst produced of BASF AG etc. all can.Its main chemical compositions is the oxide compound of cobalt, molybdenum and aluminium, uses the main chemical compositions of the catalyst waste slag behind the inactivation to be the sulfide of cobalt, molybdenum and oxide compound and a small amount of dirty foreign material of aluminium.
Used in the present invention high-temperature calcination stove can be electric furnace, rotary kiln etc., also can utilize the native stove, the native kitchen range that burn coal to calcine.
Processing method of the present invention also is applicable to utilizes the industrial low-temperature transformation catalyst to make ceramic whitening agent for raw material, but cost is higher.
The present invention becomes industrial residue into industrial raw material, turns waste into wealth; Can be high temperature resistant more than 1300 ℃ by the ceramic whitening agent that the present invention obtains, this whitening agent added in the enamel raw material by a certain percentage make glaze, can be directly into fired ceramic in the high temperature kiln; Ceramic whitening agent whitening effect of the present invention is obvious, and general fluorescent, gives aesthetic feeling, to those enamel material of yellowing slightly, add this agent after whitening effect better.This whitening agent is through Jing Dezhen ceramics factory, and high An County red plum architectural pottery head factory is on probation, and whitening effect is obvious.
Below in conjunction with embodiment the present invention is described in more detail.
Embodiment 1:
With the LHB301 low temperature sulfur-resistant transformation catalyst waste residue behind 2 kilograms of inactivations after the picking removal of impurities, grind with F-25 type pulverizing mill, cross 120 mesh sieves, evenly spray 0.3 kilogram of usefulness, 20 gram Yttrium trichloride and the formulated rare-earth synergistic solution of water, stir, then material is poured in the iron pan, again iron pan is placed on the blossom type honeycomb briquette stove and calcines, constantly stir, temperature is controlled at 700 ° ± 10 ℃, calcines after 3 hours, and material is transformed into light blue can taking the dish out of the pot by Steel Gray, be cooled to normal temperature, the packing warehouse-in.
Embodiment 2:
K8-11 type co-mo antisulphuric transforming catalyst waste residue behind 2 kilograms of inactivations after the picking removal of impurities is pulverized with pulverizer, cross 80 mesh sieves, this material is packed in the quartz crucible, put into electric furnace, 1000 ± 20 ℃ temperature lower calcinations 4 hours, material is transformed into sky blue by Steel Gray can come out of the stove, and is cooled to normal temperature, the packing warehouse-in.
Embodiment 3:
B302Q molded breadth temperature sulfur-resistant transformation catalyst waste residue behind 2 kilograms of inactivations after the picking removal of impurities is put into rotary kiln, come out of the stove after 3.5 hours, be cooled to normal temperature, pulverize, cross 100 mesh sieves, the packing warehouse-in with pulverizer at 1200 ± 20 ℃ temperature lower calcinations.
Claims (5)
1, a kind of method of making ceramic whitening agent with the inactivation low temperature shift catalyst and products thereof is characterized in that:
A. the low temperature shift catalyst waste residue behind the inactivation is carried out picking, removes dirty foreign material wherein, pulverize with pulverizer again, cross 60~120 mesh sieves,
B. the material after above-mentioned the sieving is sent in the high-temperature calcination stove and calcined 2~5 hours under the condition that has air to exist, calcining temperature is controlled at 400~1400 ℃,
C. the material after the above-mentioned calcining is come out of the stove and reduce to normal temperature, promptly obtain finished product.
2, method of making ceramic whitening agent with the inactivation low temperature shift catalyst according to claim 1 and products thereof, it is characterized in that: be 0.1~0.2 in the ratio with material equably in the material behind crushing screening: ratio spray concentration 1(weight) is 10~15%(weight) rare earths salt, send into again in the high-temperature calcination stove and calcine.
3, method of making ceramic whitening agent with the inactivation low temperature shift catalyst according to claim 1 and 2 and products thereof is characterized in that: preferably calcining temperature is controlled at 650~1200 ℃.
4, a kind of method of making ceramic whitening agent with the inactivation low temperature shift catalyst and products thereof is characterized in that:
A. the low temperature shift catalyst waste residue behind the inactivation is carried out picking, removes dirty foreign material wherein,
B. above-mentioned material is sent in the high-temperature calcination stove and calcined 2~5 hours under the condition that has air to exist, calcining temperature is controlled at 400~1400 ℃,
C. the material after will calcining is come out of the stove and is reduced to normal temperature, pulverizes with pulverizer, crosses 60~120 mesh sieves, obtains finished product.
5, method of making ceramic whitening agent with the inactivation low temperature shift catalyst according to claim 4 and products thereof, it is characterized in that: be 0.1~0.2 with the ratio with material equably in the material after the picking removal of impurities: ratio spray concentration 1(weight) is 10~15%(weight) rare earths salt, send into again in the high-temperature calcination stove and calcine.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 94100470 CN1105654A (en) | 1994-01-17 | 1994-01-17 | Method for making ceramic whitening agent by using deactivated low-temp. conversion catalyst and its products |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 94100470 CN1105654A (en) | 1994-01-17 | 1994-01-17 | Method for making ceramic whitening agent by using deactivated low-temp. conversion catalyst and its products |
Publications (1)
Publication Number | Publication Date |
---|---|
CN1105654A true CN1105654A (en) | 1995-07-26 |
Family
ID=5029676
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 94100470 Pending CN1105654A (en) | 1994-01-17 | 1994-01-17 | Method for making ceramic whitening agent by using deactivated low-temp. conversion catalyst and its products |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN1105654A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110981199A (en) * | 2019-12-27 | 2020-04-10 | 中国地质大学(北京) | Treatment method of waste SCR denitration catalyst, composite opacifier for ceramics, ceramic glaze and ceramic product |
-
1994
- 1994-01-17 CN CN 94100470 patent/CN1105654A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110981199A (en) * | 2019-12-27 | 2020-04-10 | 中国地质大学(北京) | Treatment method of waste SCR denitration catalyst, composite opacifier for ceramics, ceramic glaze and ceramic product |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101851063B (en) | Technology for preparing microcrystal glass by utilizing blast furnace water granulated slag and coal ash | |
CN101148779B (en) | Preparation method for potassium titanate crystal whisker | |
CN101381240B (en) | Method for preparing dichroite heat proof/refractory materials | |
CN1974475A (en) | Making process of electrofused mullite | |
CN102219530B (en) | Silicon mullite brick and preparation method thereof | |
CN100582035C (en) | Method for preparing cristobalite by calcining quartz | |
CN101602581A (en) | A kind of method that adopts the alloy slag to make aluminous cement | |
CN1105654A (en) | Method for making ceramic whitening agent by using deactivated low-temp. conversion catalyst and its products | |
CN1251994C (en) | Ti-Si carbide powder and its normal pressure synthesis process with Al as reaction assistant | |
CN108558353A (en) | A kind of diatomite environment-friendly insulating brick and preparation method thereof | |
CN100486698C (en) | Composite phase-change catalyst for preparing quartz and use | |
CN101045633A (en) | Method for preparing Ca-alpha-SiAlON material using iron selection tailings | |
EP0437067B1 (en) | Phosphate compounds, sintered bodies thereof and manufacture of the sintered bodies | |
CN1055526A (en) | Refined kaolin calcined from kaolinite | |
CN1394828A (en) | Preparation of low-temp. far infrared ceramic material | |
JPH09501645A (en) | Opacifier based on zirconia | |
CN1557713A (en) | Method for preparing aluminum oxide utilizing industrial sludge of aluminium section bar plant | |
CN1049325A (en) | High-strength cement having non-burning ceramic character and manufacture method thereof | |
CN109231961B (en) | Deformation-resistant rapid-fired fine pottery blank and preparation and application method thereof | |
CN1104612A (en) | Reclaiming of waste gypsum | |
CN100463857C (en) | Formula for preparing dimension stone of magnesia alumina spinel by using sludge from factory of aluminum section, and preparation method | |
CN105503163A (en) | Ceramic industry brick billet and preparation method thereof | |
CN103319162A (en) | Blue and white porcelain body prepared from industrial aluminium profile waste residues and method thereof | |
CN1066438A (en) | Chemical gypsum pottery | |
CN1475461A (en) | Magnesium aluminium vanadium refractor materiel and its production method |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C01 | Deemed withdrawal of patent application (patent law 1993) | ||
WD01 | Invention patent application deemed withdrawn after publication |