CN102557583A - Energy-saving dry powder production method for building ceramics - Google Patents
Energy-saving dry powder production method for building ceramics Download PDFInfo
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- CN102557583A CN102557583A CN201210058977XA CN201210058977A CN102557583A CN 102557583 A CN102557583 A CN 102557583A CN 201210058977X A CN201210058977X A CN 201210058977XA CN 201210058977 A CN201210058977 A CN 201210058977A CN 102557583 A CN102557583 A CN 102557583A
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- 239000000843 powder Substances 0.000 title claims abstract description 75
- 238000004519 manufacturing process Methods 0.000 title abstract description 4
- 239000000919 ceramic Substances 0.000 title abstract description 3
- 239000000463 material Substances 0.000 claims abstract description 33
- 238000000034 method Methods 0.000 claims abstract description 27
- 238000002156 mixing Methods 0.000 claims abstract description 27
- 238000005469 granulation Methods 0.000 claims abstract description 21
- 230000003179 granulation Effects 0.000 claims abstract description 21
- 239000007779 soft material Substances 0.000 claims abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 26
- 239000002245 particle Substances 0.000 claims description 18
- 238000005516 engineering process Methods 0.000 claims description 15
- 239000002689 soil Substances 0.000 claims description 14
- 238000004134 energy conservation Methods 0.000 claims description 12
- 238000005457 optimization Methods 0.000 claims description 10
- 229910052573 porcelain Inorganic materials 0.000 claims description 10
- 239000004575 stone Substances 0.000 claims description 10
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 8
- 239000010433 feldspar Substances 0.000 claims description 8
- 239000012530 fluid Substances 0.000 claims description 8
- 239000004576 sand Substances 0.000 claims description 8
- 239000000454 talc Substances 0.000 claims description 8
- 229910052623 talc Inorganic materials 0.000 claims description 8
- 235000012222 talc Nutrition 0.000 claims description 8
- 239000002010 green coke Substances 0.000 claims description 6
- -1 ripe Jiao Substances 0.000 claims description 6
- 238000012216 screening Methods 0.000 claims description 5
- 239000004927 clay Substances 0.000 claims description 4
- 239000010437 gem Substances 0.000 claims description 4
- 229910001751 gemstone Inorganic materials 0.000 claims description 4
- NWXHSRDXUJENGJ-UHFFFAOYSA-N calcium;magnesium;dioxido(oxo)silane Chemical compound [Mg+2].[Ca+2].[O-][Si]([O-])=O.[O-][Si]([O-])=O NWXHSRDXUJENGJ-UHFFFAOYSA-N 0.000 claims description 3
- 229910052637 diopside Inorganic materials 0.000 claims description 3
- 239000003795 chemical substances by application Substances 0.000 claims description 2
- 238000009826 distribution Methods 0.000 claims description 2
- 238000010298 pulverizing process Methods 0.000 claims description 2
- 239000007787 solid Substances 0.000 claims description 2
- 239000008187 granular material Substances 0.000 abstract description 2
- 239000002002 slurry Substances 0.000 abstract 2
- 238000012856 packing Methods 0.000 description 15
- 238000001035 drying Methods 0.000 description 9
- 239000002994 raw material Substances 0.000 description 9
- 239000003638 chemical reducing agent Substances 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 239000011236 particulate material Substances 0.000 description 3
- 238000001694 spray drying Methods 0.000 description 3
- 238000000227 grinding Methods 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000011449 brick Substances 0.000 description 1
- 238000000748 compression moulding Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000010881 fly ash Substances 0.000 description 1
- 238000003801 milling Methods 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
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- Preparation Of Clay, And Manufacture Of Mixtures Containing Clay Or Cement (AREA)
Abstract
The invention relates to an energy-saving dry powder production method for building ceramics. The method is characterized in that the method includes the following steps: (1) hard materials and soft material in a green body formula are separated; (2) a ball mill is used for processing the soft material with high moisture content into slurry with 40 to 70 percent of moisture content for later use; (3) a pulverizer is used for respectively processing the hard materials into fine powders meeting requirement and conveying the fine powders into respective bins; (4) according to the green body formula, an automated batching system is used for mixing the processed fine hard material powders in batches according to proportion; and the prepared slurry as humidizer and the mixed fine hard material powders are forcibly mixed and granulated in a mixing granulator; (5) after granulation, granules are screened and optimized, and are then dried into the needed granular powder in a fluidized-bed dryer, and the granular powder can be used after being aged for 24 hours. The invention has the advantages of energy saving, consumption reduction and little pollution.
Description
Technical field
The present invention is specifically related to the energy-conservation dry method flouring technology of a kind of architectural pottery.
Background technology
The automatic production line of existing architectural pottery, especially ceramic wall and floor bricks, so long as use the producer of great tonnage press compression moulding, employed powder all prepares with wet processing.Be after raw material enters factory,, simultaneously, add 30%～40% water, carry out 10～18 hours grinding then being delivered into ball mill after the various raw material weighing.After meeting the requirements of fineness, put into suction pit, pass through the spray-drying tower mist projection granulating again, process needed powder at last.
This technology has two main aspects to have the phenomenon that energy consumption is big and waste.The one, ball mill is relatively wasted electric energy.Because several kinds of raw materials in the body recipe; Their grindability can have very large difference; The soft material that grinds easily can meet the requirements of fineness within by two hours, the hard material then needs several times even longer milling time just can meet the requirements of fineness.Just there was the grinding phenomenon in this.The 2nd, spray-drying tower need evaporate the most of water in the mud of moisture 30%--40% when mist projection granulating, processes moisture at 5%～7% qualified powder at last.This process will consume a large amount of heat energy.And after waste gas after burning and the water vapour mixing emptying, also can cause pollution to a certain degree to surrounding environment.
Summary of the invention
The objective of the invention is to solve prior art wet powder-making technology and have the deficiency that energy consumption is big and waste, provide a kind of architectural pottery that can significantly cut down the consumption of energy energy-conservation dry method flouring technology.
The present invention adopts following technical scheme to realize:
Be the energy-conservation dry method flouring technology of a kind of architectural pottery, it is characterized in that comprising the following steps:
1) hard material in the body recipe and soft material are separated;
2) it is subsequent use to use the ball mill soft material that water content is high to be processed into moisture 40%～70% mud;
3) hard material that different water contents is low uses pulverizing mill to be processed into respectively and meets the requirements of fine powder, is delivered into feed bin separately;
4),,, become batch proportioning to mix with the hard material fine powder that processes by automatic material-dispensing system according to body recipe; Then the mud for preparing is carried out the powerful mixing granulation as moistening agent and the hard material fine powder that mixes in the mixing granulation machine, the weight percent of mud is 24%～28%, and the weight percent of hard material fine powder is 72%～76%;
5) after the granulation, screening and particle optimization, the influent stream bed dryer is dried to needed particulate state powder then, can use after old 24 hours.
As a preferred version of the present invention: hard material granularity＜40mm.
As a preferred version of the present invention: the moil fineness that soft material processes is controlled at 325 orders～400 orders, tails over 1%～3%.
As a preferred version of the present invention: the fine powder fineness that the hard material processes is controlled at 250 orders～325 orders, tails over 1%～8%.
As a preferred version of the present invention: the material powder water ratio after granulation and the particle optimization is 9～12%.
As a preferred version of the present invention: be controlled at 4%～7% through the dried material powder of fluid bed dryer water ratio, the material powder particles becomes normal distribution at 0.2mm～0.8mm, is the circular solids shape.
As a preferred version of the present invention: the hard material is feldspar, porcelain stone, green coke, ripe Jiao, talcum, high alumina sand, diopside, agalmatolite, Tangxian County soil, Hebei is native, Laiyang is native, a kind of or multiple combination arbitrarily among the Wen Zushi, green coke jewel, useless base, sandstone.
As a preferred version of the present invention: soft material is the combination of any or two kinds in black mud, the clay.
That the present invention has is energy-saving and cost-reducing, pollute little advantage.Use dry method powder process novel process of the present invention, can make the performance of made powder, like granule strength, indexs such as the flowability of powder are identical with the prepared powder of spray-drying tower basically.Can normally use building on the pottery production line of robotization.Use the present invention to make powder and can economize on electricity more than 30%, practice thrift heat energy more than 80%, the comprehensive energy consumption index can descend more than 60%.
Description of drawings
Fig. 1 is a process flow sheet of the present invention.
Embodiment
Embodiment 1
Each raw material and weight percent thereof are following:
Black mud: 18%
Tangxian County soil: 5%
Ripe Jiao: 5%
Feldspar: 32%
Porcelain stone: 35%
Talcum 2%
High alumina sand: 3%
Black mud is soft material in the above-mentioned raw materials, and other are the hard material.
The concrete operations step:
1) according to aforementioned proportion, in 6: 4 the ratio ball mill of packing into, the ball mill that turns round then is ground to fineness with it and reaches 325 orders, tails over 1% mud with black mud and water.Look local water quality, when the dress mill, will add suitable water reducer, guarantee that mud has reasonable flowability.
2) feldspar is worn into 325 orders with Vertical Mill, tail over 3% fine powder, the feed bin of packing into is for use.
3) porcelain stone is worn into 325 orders with Vertical Mill, tail over 3% fine powder, the feed bin of packing into is for use.
4) with Tangxian County soil, ripe Jiao, talcum, the high alumina sand proportional mixing is good, and one reinstates vertical mill becomes 325 orders, tails over 3% fine powder, and the feed bin of packing into is for use.
5) use automatic batching system, press formula rate, once join the good dry powder of 820kg mill, wherein:
Feldspar Powder 320kg;
Porcelain stone powder 350kg;
Tangxian County soil, ripe Jiao, talcum, the mixing fine powders 150kg of high alumina sand;
The 820kg fine powder for preparing is transported to carries out mixing granulation in the mixing granulation machine.
6) use 1000 liters powerful mixing tablets press, with dry powder powerful mixing 2-3 minute, with rampump mud is squeezed into the mixing granulation machine then and carry out the humidification granulation earlier.Mud will fully atomize, and the time was controlled at 3-5 minute.The straying quatity of mud is 300kg.The particle water ratio of making is about 11%.
7) the particulate material powder that will make is emitted from tablets press; Being transported to 30 purpose vibratory screening apparatuss through conveying belt sieves; Qualified material powder enters into multi layer vibrating fluid bed and carries out drying; Underproof larger particles enters into particle optimization machine and carries out particle optimization, and then enters into the multi layer vibrating fluid bed drying.
8) be controlled at about 6.5% through the powder water ratio behind the fluidised bed drying.It is old to be transported to feed bin then, just can use after 24 hours excessively.
Embodiment 2
Each raw material and weight percent thereof are following:
Black mud: 20%
Hebei soil: 4%
Tangxian County soil: 3.5%
High alumina sand: 3%
Porcelain stone 18.5%
Feldspar 32%
Agalmatolite 8%
Wen Zushi 4%
Ripe burnt 6%
Talcum 1%
Black mud is soft material in the above-mentioned raw materials, and other are the hard material.
The concrete operations step:
1) according to aforementioned proportion, in 5: 3 the ratio ball mill of packing into, the ball mill that turns round then is ground to fineness with it and reaches 370 orders, tails over 2% mud with black mud and water.Look local water quality, when the dress mill, will add suitable water reducer, guarantee that mud has reasonable flowability.
2) feldspar is worn into 300 orders with Vertical Mill, tail over 4% fine powder, the feed bin of packing into is for use.
3) porcelain stone is worn into 300 orders with Vertical Mill, tail over 4% fine powder, the feed bin of packing into is for use.
4) Hebei soil, Tangxian County soil, ripe Jiao, talcum, high alumina sand mixes by formula rate in advance, and one reinstates vertical mill becomes 300 orders, tails over 4% fine powder, and the feed bin of packing into is for use.
5) with agalmatolite, Wen Zushi mixes by formula rate in advance, and one reinstates vertical mill becomes 300 orders, tails over 4% fine powder, and the feed bin of packing into is for use.
6) use automatic batching system, press formula rate, once join the good dry powder of 820kg mill, wherein:
Feldspar Powder 320kg;
Porcelain stone powder 185kg;
Hebei soil, Tangxian County soil, ripe Jiao, talcum, the mixing fine powders 175kg of high alumina sand;
Agalmatolite, the mixing fine powders 120kg of Wen Zushi;
The 820kg fine powder for preparing is transported to carries out mixing granulation in the mixing granulation machine.
7) use 1000 liters powerful mixing tablets press, with dry powder powerful mixing 2-3 minute, with rampump mud is squeezed into the mixing granulation machine then and carry out the humidification granulation earlier.Mud will fully atomize, and the time was controlled at 3-5 minute.The straying quatity of mud is 320kg.The particle water ratio of making is about 11%.
8) the particulate material powder that will make is emitted from tablets press; Being transported to 30 purpose vibratory screening apparatuss through conveying belt sieves; Qualified material powder enters into multi layer vibrating fluid bed and carries out drying; Underproof larger particles enters into particle optimization machine and carries out particle optimization, and then enters into the multi layer vibrating fluid bed drying.
9) be controlled at about 6.5% through the powder water ratio behind the fluidised bed drying.It is old to be transported to feed bin then, just can use after 24 hours excessively.
Embodiment 3
Each raw material and weight percent thereof are following:
The above-mentioned raw materials medium clay soil is soft material, and other are the hard material.
The concrete operations step:
1) according to aforementioned proportion, in 5: 4 the ratio ball mill of packing into, the ball mill that turns round then is ground to fineness with it and reaches 400 orders, tails over 3% mud with clay and water.Look local water quality, when the dress mill, will add suitable water reducer, guarantee that mud has reasonable flowability.
2) diopside is worn into 250 orders with Vertical Mill, tail over 8% fine powder, the feed bin of packing into is for use.
3) porcelain stone is worn into 250 orders with Vertical Mill, tail over 8% fine powder, the feed bin of packing into is for use.
4) sandstone is worn into 250 orders with Vertical Mill, tail over 8% fine powder, the feed bin of packing into is for use.
5) Laiyang soil is worn into 250 orders with Vertical Mill, tail over 8% fine powder, the feed bin of packing into is for use.
6) with the green coke jewel, useless base mixes by formula rate in advance, and one reinstates vertical mill becomes 250 orders, tails over 8% fine powder, and the feed bin of packing into is for use.
7) use automatic batching system, press formula rate, once join the good dry powder of 850kg mill, wherein:
Fly-ash 280kg;
Porcelain stone powder 200kg;
Sandstone powder 150kg;
Laiyang soil powder 100kg;
The green coke jewel, the mixing fine powders 120kg of useless base;
The 850kg fine powder for preparing is transported to carries out mixing granulation in the mixing granulation machine.
8) use 1000 liters powerful mixing tablets press, with dry powder powerful mixing 2-3 minute, with rampump mud is squeezed into the mixing granulation machine then and carry out the humidification granulation earlier.Mud will fully atomize, and the time was controlled at 3-5 minute.The straying quatity of mud is 270kg.The particle water ratio of making is about 11%.
9) the particulate material powder that will make is emitted from tablets press; Being transported to 30 purpose vibratory screening apparatuss through conveying belt sieves; Qualified material powder enters into multi layer vibrating fluid bed and carries out drying; Underproof larger particles enters into particle optimization machine and carries out particle optimization, and then enters into the multi layer vibrating fluid bed drying.
10) be controlled at about 6.5% through the powder water ratio behind the fluidised bed drying.It is old to be transported to feed bin then, just can use after 24 hours excessively.
Claims (8)
1. the energy-conservation dry method flouring technology of architectural pottery is characterized in that comprising the following steps:
1) hard material in the body recipe and soft material are separated;
2) it is subsequent use to use the ball mill soft material that water content is high to be processed into moisture 40%～70% mud;
3) hard material that different water contents is low uses pulverizing mill to be processed into respectively and meets the requirements of fine powder, is delivered into feed bin separately;
4),,, become batch proportioning to mix with the hard material fine powder that processes by automatic material-dispensing system according to body recipe; Then the mud for preparing is carried out the powerful mixing granulation as moistening agent and the hard material fine powder that mixes in the mixing granulation machine, the weight percent of mud is 24%～28%, and the weight percent of hard material fine powder is 72%～76%;
5) after the granulation, screening and particle optimization, the influent stream bed dryer is dried to needed particulate state powder then, can use after old 24 hours.
2. the energy-conservation dry method flouring technology of architectural pottery according to claim 1 is characterized in that hard material granularity＜40mm.
3. the energy-conservation dry method flouring technology of architectural pottery according to claim 1 is characterized in that the moil fineness that soft material processes is controlled at 325 orders～400 orders, tails over 1%～3%.
4. the energy-conservation dry method flouring technology of architectural pottery according to claim 1 is characterized in that the fine powder fineness that the hard material processes is controlled at 250 orders～325 orders, tails over 1%～8%.
5. the energy-conservation dry method flouring technology of architectural pottery according to claim 1 is characterized in that the material powder water ratio after granulation and the particle optimization is 9～12%.
6. the energy-conservation dry method flouring technology of architectural pottery according to claim 1 is characterized in that being controlled at 4%～7% through the dried material powder of fluid bed dryer water ratio, and the material powder particles becomes normal distribution at 0.2mm～0.8mm, is the circular solids shape.
7. according to claim 1 or the energy-conservation dry method flouring technology of 2 or 4 described architectural potteries, it is characterized in that the hard material is feldspar, porcelain stone, green coke, ripe Jiao, talcum, high alumina sand, diopside, agalmatolite, Tangxian County soil, Hebei is native, Laiyang is native, a kind of or multiple combination arbitrarily among the Wen Zushi, green coke jewel, useless base, sandstone.
8. according to claim 1 or the energy-conservation dry method flouring technology of 3 described architectural potteries, it is characterized in that soft material is the combination of any or two kinds in black mud, the clay.
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| CN201210058977XA CN102557583A (en) | 2012-03-08 | 2012-03-08 | Energy-saving dry powder production method for building ceramics |
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| CN103332968A (en) * | 2013-06-25 | 2013-10-02 | 佛山市高明区新粤丰建材有限公司 | Full-polishing glaze production process and prepared product |
| CN103566818A (en) * | 2013-10-17 | 2014-02-12 | 陕西科技大学 | Architectural ceramic blank dry-method prilling device and method |
| CN104003695A (en) * | 2014-05-27 | 2014-08-27 | 福建省晋江市丹豪陶瓷有限公司 | Enameled ceramic tile and preparation method thereof |
| CN104128241A (en) * | 2014-08-15 | 2014-11-05 | 佛山市溶洲建筑陶瓷二厂有限公司 | Loop system of dry-method powder process |
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| CN103332968B (en) * | 2013-06-25 | 2015-06-17 | 佛山市高明区新粤丰建材有限公司 | Full-polishing glaze production process and prepared product |
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Application publication date: 20120711 |