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CN1900008A - Method for producing high strenght flyash ceramic sand - Google Patents

Method for producing high strenght flyash ceramic sand Download PDF

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Publication number
CN1900008A
CN1900008A CNA2006100170421A CN200610017042A CN1900008A CN 1900008 A CN1900008 A CN 1900008A CN A2006100170421 A CNA2006100170421 A CN A2006100170421A CN 200610017042 A CN200610017042 A CN 200610017042A CN 1900008 A CN1900008 A CN 1900008A
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China
Prior art keywords
fly ash
sintering
clay
kiln
fine
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Application number
CNA2006100170421A
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Chinese (zh)
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CN100408506C (en
Inventor
赵国明
李君兴
贾文光
矫云学
张云硕
袁存亮
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Jilin Academy of Agricultural Machinery
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Jilin Academy of Agricultural Machinery
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Priority to CNB2006100170421A priority Critical patent/CN100408506C/en
Publication of CN1900008A publication Critical patent/CN1900008A/en
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Publication of CN100408506C publication Critical patent/CN100408506C/en
Expired - Fee Related legal-status Critical Current
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P40/00Technologies relating to the processing of minerals
    • Y02P40/60Production of ceramic materials or ceramic elements, e.g. substitution of clay or shale by alternative raw materials, e.g. ashes

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  • Processing Of Solid Wastes (AREA)

Abstract

一种高强度粉煤灰陶砂的制造方法,属于粉煤灰利用及新型建材工业技术领域,以粉煤灰、粘土、微细锯末、煤粉为配料,加入搅拌机内混合均匀后,并喷入一定量预先配好的水玻璃水溶液,继续搅拌,控制含水率在20%左右。然后将和好的物料放入平磨制粒机内成型,再将成球后的颗粒放在圆盘成球机内成球,成球后就可放入烧结窑内焙烧。烧结结束后,在窑内冷却,粉煤灰陶砂制造结束。生产出来的产品粒级为3mm~5mm,且颗粒规整,均匀度高,其颗粒堆积密度一般在800kg/m3~900kg/m3,表观密度为1000kg/m3~1100kg/m3,筒压强度为10MPa~20MPa。产品可广泛应用于建筑墙体板骨料,在一定范围上可代替小粒砂石。A method for manufacturing high-strength fly ash pottery sand, which belongs to the technical field of fly ash utilization and new building materials industry, uses fly ash, clay, fine sawdust, and coal powder as ingredients, puts them into a mixer, mixes them evenly, and sprays them into A certain amount of water glass aqueous solution prepared in advance, continue to stir, and control the moisture content at about 20%. Then put the reconciled material into a flat mill granulator to shape, and then put the pellets into balls into a disc ball machine to form balls, and then put them into a sintering kiln for roasting. After sintering, it is cooled in the kiln, and the production of fly ash pottery sand is completed. The particle size of the produced product is 3mm ~ 5mm, and the particles are regular and high uniformity. The particle bulk density is generally 800kg/m 3 ~ 900kg/m 3 , and the apparent density is 1000kg/m 3 ~ 1100kg/m 3 . The compressive strength is 10MPa~20MPa. The product can be widely used in building wall slab aggregates, and can replace small-grained sand and gravel in a certain range.

Description

A kind of manufacture method of high strenght flyash ceramic sand
Technical field
The invention belongs to utilization of fly ash and building material industrial technology field, particularly a kind of manufacture method of high strenght flyash ceramic sand.
Background technology
Flyash is the waste of heat power plant, and discharge capacity is very big, if handle badly, can bring very big harm to environment.At present, also do not have to produce specially the technology and the equipment of flyash ceramic sand, existing flyash ceramic sand all screens, and limited amount, and shape irregularity substitute the granule sandstone fully and also have certain difficulty very much.Thus, the invention of flyash ceramic sand is imperative.
Summary of the invention
Technical problem to be solved by this invention is: develop a kind of small, evengranular flyash ceramic sand, have the building material aglite of lightweight, high-strength, insulation and fire-resistant characteristics.
Making method of the present invention is as follows:
With flyash, clay, fine sawdust, coal dust, water glass batching, its cooperation ratio is as follows by weight:
Flyash: 75%~80%
Clay: 12%~20%
Fine sawdust: 2%~5%
Coal dust or flue dust 3%~7%
Water glass: 0.5%~2%
Wherein used flyash is the fines of collecting in the boiler of power plant flue gas; Used clay is for pulverizing the back granularity less than 40 purpose clay powders; Fine saw art and coal dust (or flue dust) are less than 40 purpose powder.
Blending process
1) after scope took by weighing according to the above ratio with flyash, clay, fine sawdust, coal dust, putting together mixed;
2) water glass is made into 0.02%~0.03% the aqueous solution;
3) spray into a certain amount of aqueous solution for preparing, mix material, the control water ratio is between 15%~25%;
4) material that stirs being put into the flat-die nodulizer granulates;
5) made grain is put into the disk balling machine balling-up;
6) ball that is become is put into the sintering oven roasting, when the control sintering temperature reaches between 900 ℃~950 ℃, be incubated 20~30 minutes, continue then to give birth to temperature, when reaching 1200 ℃~1300 ℃, be incubated 30~60 minutes, sintering finishes;
7) after sintering finished, kiln internal cooling to 550 ℃~600 ℃, the kiln discharge naturally cooling was finished.
Preparation process is:
Get material → batch mixing → and material → granulation → moulding → sintering
Equipment used is all prior art in the above manufacture method, and raw materials used all being very easy to obtains.
The invention has the beneficial effects as follows: the flyash ceramic sand of producing has lightweight, high-strength, insulation and advantage such as fire-resistant, to a certain extent, alternative generation the granule sandstone, and surface attachment layer oxide film, water-intake rate is very low, add it and can improve the water resistance of material, weight reduction, improve the density uniformity of material, combine with heat pressing process, can improve the workability of material greatly, used the wallboard of this pottery sand, block, cutting edge or boring, ailing all be very easy to, and be and very reliable.The product grade is 3mm~5mm, and particle is regular, the uniformity coefficient height, and its packing density of particle is generally at 800kg/m 3~900kg/m 3, apparent density is 1000kg/m 3~1100kg/m 3, cylindrical compress strength is 10Mpa~20Mpa.
Specific embodiment
Embodiment 1
Prescription (weight ratio):
Changchun two heat power plant's flyash: 75%
Clay: 15%
Fine sawdust: 4.5%
Coal dust 5%
Water glass: 0.5%
Technology:
According to the above ratio Changchun two heat power plant's flyash, clay, fine sawdust, coal dust are added mix in the stirrer after, and spray into a certain amount of 0.02% the sodium silicate solution for preparing in advance, continue to stir, the control water ratio is about 20%.The material that to become reconciled is put into the moulding of plain grinding nodulizer then, again the particle after the balling-up is placed on balling-up in the disk balling machine, just can put into the sintering oven roasting after the balling-up.The control sintering temperature when sintering temperature reaches 920 ℃ ± 20 ℃, is incubated 25 minutes during roasting, and its each component is fully reacted, and continues then to give birth to temperature, when reaching 1300 ℃ ± 20 ℃, is incubated 40 minutes, and sintering finishes.After sintering finishes, when kiln internal cooling to the 600 ℃ left and right sides, the kiln discharge naturally cooling.The flyash ceramic sand manufacturing finishes.The product grade of producing is 3mm~5mm, and particle is regular, the uniformity coefficient height, and its packing density of particle is generally at 810kg/m 3~890kg/m 3, apparent density is 1000kg/m 3~1100kg/m 3, cylindrical compress strength is 11Mpa~18Mpa.
Embodiment 2
Prescription (weight ratio):
The thermoelectric factory's flyash in Changchun: 78%
Clay: 12%
Fine sawdust: 5%
Coal dust 4.5%
Water glass: 0.5%
Technology:
According to the above ratio the thermoelectric factory's flyash in Changchun, clay, fine saw art, coal dust are added mix in the stirrer after, and spray into a certain amount of 0.02% the sodium silicate solution for preparing in advance, continue to stir, the control water ratio is about 20%.The material that to become reconciled is put into the moulding of plain grinding nodulizer then, again the particle after the balling-up is placed on balling-up in the disk balling machine, just can put into the sintering oven roasting after the balling-up.The control sintering temperature when sintering temperature reaches 920 ℃ ± 20 ℃, is incubated 25 minutes during roasting, and its each component is fully reacted, and continues then to give birth to temperature, when reaching 1250 ℃ ± 20 ℃, is incubated 45 minutes, and sintering finishes.After sintering finishes, when kiln internal cooling to the 600 ℃ left and right sides, the kiln discharge naturally cooling.The flyash ceramic sand manufacturing finishes.The product grade of producing is 3mm~5mm, and particle is regular, the uniformity coefficient height, and its packing density of particle is generally at 820kg/m 3~900kg/m 3, apparent density is 1000kg/m 3~1100kg/m 3, cylindrical compress strength is 10Mpa~17Mpa.
Embodiment 3
Prescription (weight ratio):
Changchun two heat power plant's flyash: 80%
Clay: 12%
Fine sawdust: 3%
Flue dust 4.2%
Water glass: 0.8%
Technology:
According to the above ratio Changchun two heat power plant's flyash, clay, fine sawdust, flue dust are added mix in the stirrer after, and spray into a certain amount of 0.02% the sodium silicate solution for preparing in advance, continue to stir, the control water ratio is about 20%.The material that to become reconciled is put into the moulding of plain grinding nodulizer then, again the particle after the balling-up is placed on balling-up in the disk balling machine, just can put into the sintering oven roasting after the balling-up.The control sintering temperature when sintering temperature reaches 930 ℃ ± 20 ℃, is incubated 25 minutes during roasting, and its each component is fully reacted, and continues then to give birth to temperature, when reaching 1280 ℃ ± 20 ℃, is incubated 35 minutes, and sintering finishes.After sintering finishes, when kiln internal cooling to the 600 ℃ left and right sides, the kiln discharge naturally cooling.The flyash ceramic sand manufacturing finishes.The product grade of producing is 3mm~5mm, and particle is regular, the uniformity coefficient height, and its packing density of particle is generally at 800kg/m 3~900kg/m 3, apparent density is 1000kg/m 3~1100kg/m 3, cylindrical compress strength is 10Mpa~20Mpa.

Claims (2)

1、一种高强度粉煤灰陶砂的制造方法,是以粉煤灰和粘土为主料,其特征是:配比重量计:1. A method for manufacturing high-strength fly ash pottery sand, which uses fly ash and clay as the main ingredients, and is characterized in that: proportioning weight: 粉煤灰:          75%~80%Fly ash: 75%~80% 粘  土:          12%~20%Clay: 12%~20% 微细锯末:        2%~5%Fine sawdust: 2% to 5% 煤粉或烟道灰      3%~7%Coal powder or flue ash 3% to 7% 水玻璃:          0.5%~2%Water glass: 0.5%~2% 配制方法:Preparation method: 1)将粉煤灰、粘土、微细锯末、煤粉按上述比例范围称取后,放在一起混合均匀;1) After weighing fly ash, clay, fine sawdust, and coal powder according to the above ratio range, put them together and mix them evenly; 2)将水玻璃配成0.02%~0.03%的水溶液;2) Make water glass into 0.02%~0.03% aqueous solution; 3)喷入一定量配好的水溶液,搅拌混合物料,控制含水率在15%~25%之间;3) Spray a certain amount of prepared aqueous solution, stir the mixed material, and control the moisture content between 15% and 25%; 4)将搅拌好的物料放入平模制粒机内制粒;4) Put the stirred material into the flat die granulator to granulate; 5)将所制的粒放入圆盘成球机内成球;5) Put the prepared granules into a disc ball forming machine to form balls; 6)将所成的球放入烧结窑内焙烧,控制烧结温度达到900℃~950℃之间时,保温20~30分钟,然后继续生温,达到1150℃~1300℃时,保温30~60分钟,烧结结束;6) Put the formed balls into the sintering kiln for sintering. When the sintering temperature reaches 900°C-950°C, keep it warm for 20-30 minutes. Minutes, the sintering is over; 7)烧结结束后,在窑内冷却至550℃~600℃,出窑自然冷却完成。7) After sintering, cool in the kiln to 550°C to 600°C, and leave the kiln for natural cooling. 2、根据权利要求1所述的一种高强度粉煤灰陶砂的制造方法,其特征在于所用的粉煤灰为电厂锅炉烟气中收集到的微细粉末;所用粘土为粉碎后粒度小于40目的粘土粉末;微细锯末与煤粉或烟道灰均为小于40目的粉末。2. A method for manufacturing high-strength fly ash pottery sand according to claim 1, characterized in that the fly ash used is fine powder collected from boiler flue gas in a power plant; the clay used has a particle size of less than 40 Purpose clay powder; fine sawdust and coal powder or flue ash are powders less than 40 mesh.
CNB2006100170421A 2006-07-24 2006-07-24 A kind of manufacturing method of high-strength fly ash pottery sand Expired - Fee Related CN100408506C (en)

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Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101348364B (en) * 2008-04-29 2010-09-15 北京创导高科绝热材料有限公司 Method for producing light heat-insulating brick from sawdust and light heat-insulating brick thereof
CN102060562A (en) * 2010-11-18 2011-05-18 陕西科技大学 Preparation method of ceramic granules
WO2012089875A1 (en) * 2010-12-31 2012-07-05 Bou Cortes Maria Lidon Method for producing a ceramic product using fly ash as a raw material
RU2455247C1 (en) * 2011-03-21 2012-07-10 Юлия Алексеевна Щепочкина Mixture for making porous aggregate
CN101439964B (en) * 2008-12-01 2012-07-25 上海古猿人石材有限公司 Method for producing fly ash haydite
RU2473487C1 (en) * 2011-10-24 2013-01-27 Юлия Алексеевна Щепочкина Charge for production of porous filling agent
RU2481285C1 (en) * 2012-02-09 2013-05-10 Юлия Алексеевна Щепочкина Mixture for producing porous aggregate
RU2484030C1 (en) * 2012-02-22 2013-06-10 Юлия Алексеевна Щепочкина Mixture for making porous aggregate
RU2489375C1 (en) * 2012-04-24 2013-08-10 Юлия Алексеевна Щепочкина Mixure for making porous aggregate
RU2501753C1 (en) * 2012-09-14 2013-12-20 Юлия Алексеевна Щепочкина Charge for porous filling agent production
RU2514028C1 (en) * 2013-03-13 2014-04-27 Юлия Алексеевна Щепочкина Charge for production of porous filler
RU2521101C1 (en) * 2013-06-14 2014-06-27 Юлия Алексеевна Щепочкина Charge stock for production of porous aggregate
RU2562072C1 (en) * 2014-10-21 2015-09-10 Юлия Алексеевна Щепочкина Furnace charge for porous filler production
CN105174994A (en) * 2015-08-31 2015-12-23 宜昌朗天新型建材有限公司 Method for preparing sludge ceramsite by regenerating pottery sand and flue dust
CN105417977A (en) * 2015-12-31 2016-03-23 神华集团有限责任公司 Fly ash ceramsite sand, preparation method and applications thereof
CN107922263A (en) * 2015-06-15 2018-04-17 察克科技有限公司 Lightweight fine ceramics particle
CN111533535A (en) * 2020-05-08 2020-08-14 揭阳市汇兴环保建材有限公司 Ceramsite production process

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1100398A (en) * 1993-09-16 1995-03-22 刘生泰 Method for producing ceramic sand & ceramsite with caustic sludge and coal ash

Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101348364B (en) * 2008-04-29 2010-09-15 北京创导高科绝热材料有限公司 Method for producing light heat-insulating brick from sawdust and light heat-insulating brick thereof
CN101439964B (en) * 2008-12-01 2012-07-25 上海古猿人石材有限公司 Method for producing fly ash haydite
CN102060562A (en) * 2010-11-18 2011-05-18 陕西科技大学 Preparation method of ceramic granules
WO2012089875A1 (en) * 2010-12-31 2012-07-05 Bou Cortes Maria Lidon Method for producing a ceramic product using fly ash as a raw material
ES2385570A1 (en) * 2010-12-31 2012-07-26 María Lidón Bou Cortes Method for producing a ceramic product using fly ash as a raw material
RU2455247C1 (en) * 2011-03-21 2012-07-10 Юлия Алексеевна Щепочкина Mixture for making porous aggregate
RU2473487C1 (en) * 2011-10-24 2013-01-27 Юлия Алексеевна Щепочкина Charge for production of porous filling agent
RU2481285C1 (en) * 2012-02-09 2013-05-10 Юлия Алексеевна Щепочкина Mixture for producing porous aggregate
RU2484030C1 (en) * 2012-02-22 2013-06-10 Юлия Алексеевна Щепочкина Mixture for making porous aggregate
RU2489375C1 (en) * 2012-04-24 2013-08-10 Юлия Алексеевна Щепочкина Mixure for making porous aggregate
RU2501753C1 (en) * 2012-09-14 2013-12-20 Юлия Алексеевна Щепочкина Charge for porous filling agent production
RU2514028C1 (en) * 2013-03-13 2014-04-27 Юлия Алексеевна Щепочкина Charge for production of porous filler
RU2521101C1 (en) * 2013-06-14 2014-06-27 Юлия Алексеевна Щепочкина Charge stock for production of porous aggregate
RU2562072C1 (en) * 2014-10-21 2015-09-10 Юлия Алексеевна Щепочкина Furnace charge for porous filler production
CN107922263A (en) * 2015-06-15 2018-04-17 察克科技有限公司 Lightweight fine ceramics particle
CN105174994A (en) * 2015-08-31 2015-12-23 宜昌朗天新型建材有限公司 Method for preparing sludge ceramsite by regenerating pottery sand and flue dust
CN105417977A (en) * 2015-12-31 2016-03-23 神华集团有限责任公司 Fly ash ceramsite sand, preparation method and applications thereof
CN111533535A (en) * 2020-05-08 2020-08-14 揭阳市汇兴环保建材有限公司 Ceramsite production process

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