WO2017101269A1 - 一种陶瓷粉料配方及其制作工艺 - Google Patents

一种陶瓷粉料配方及其制作工艺 Download PDF

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WO2017101269A1
WO2017101269A1 PCT/CN2016/084757 CN2016084757W WO2017101269A1 WO 2017101269 A1 WO2017101269 A1 WO 2017101269A1 CN 2016084757 W CN2016084757 W CN 2016084757W WO 2017101269 A1 WO2017101269 A1 WO 2017101269A1
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weight
powder
parts
water
moisture
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PCT/CN2016/084757
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French (fr)
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梁海果
严苏景
梁志江
严文记
罗应钿
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佛山市博晖机电有限公司
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Publication of WO2017101269A1 publication Critical patent/WO2017101269A1/zh

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    • C—CHEMISTRY; METALLURGY
    • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/622—Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/626—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B
    • C04B35/62605—Treating the starting powders individually or as mixtures
    • C04B35/62695—Granulation or pelletising
    • C—CHEMISTRY; METALLURGY
    • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B33/00—Clay-wares
    • C04B33/02—Preparing or treating the raw materials individually or as batches
    • C—CHEMISTRY; METALLURGY
    • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/622—Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/62204—Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products using waste materials or refuse
    • C—CHEMISTRY; METALLURGY
    • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/622—Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/626—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B
    • C—CHEMISTRY; METALLURGY
    • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B2235/00—Aspects relating to ceramic starting mixtures or sintered ceramic products
    • C04B2235/02—Composition of constituents of the starting material or of secondary phases of the final product
    • C04B2235/30—Constituents and secondary phases not being of a fibrous nature
    • C04B2235/42—Non metallic elements added as constituents or additives, e.g. sulfur, phosphor, selenium or tellurium
    • C04B2235/422—Carbon

Definitions

  • the invention relates to the technical field of ceramic production, in particular to a ceramic powder formula and a manufacturing process thereof.
  • the traditional method adopts the wet method for powdering, and the raw material of the formula is added with water to be ground in the ball mill, and the water content of the slurry reaches 34% to 38%, and then granulated and dried by the spray tower.
  • the finished pellets retain moisture of 6% to 7%, and then go to the silo for obsolescence.
  • the traditional wet milling technology has a large floor space, large power consumption, scattered operators, and high personnel costs, which makes the cost of raw material manufacturing high.
  • the traditional wet milling technology dries from 34% to 38% of the moisture of the slurry to 6% to 7% of the moisture of the powder. It needs to consume a lot of heat energy, the combustion of coal powder, the emission of waste gas, and the discharge of sewage to the environment. Serious pollution has seriously deviated from the energy conservation and emission reduction policies advocated by the state.
  • the object of the invention is to solve the problem of high emission and high pollution in the traditional wet milling technology, overcome the deficiencies of the prior art, and provide a new ceramic powder dry milling technology with good production effect, low cost and simple and reliable manufacturing process. Process.
  • the technical solution provided by the present invention is: a ceramic powder formulation comprising a first portion of mud comprising 11.25 parts by weight of moisture and a dry content of 45, and a moisture content of 12.32 parts by weight.
  • the dry material is a second portion of 45, a moisture of 7.90 parts by weight, and a dry material of 200, a first stone, a weight of 4.10, and a dry material of 160, a second stone, parts by weight.
  • the soil part, the moisture of 8.92 parts by weight and the dry material of 110 third part of soil, the weight of 3.65 parts of water and the dry material of 90% of the coke, the weight of 3.67 parts of water and the dry material is 20 porcelain edge grinding material, 5.5 parts by weight of water and 40 pieces of ceramic tile broken particles and 1.5 parts by weight of water and dry material of 15 polished waste powder.
  • the solution also provides a manufacturing process for preparing the above ceramic powder formula, which comprises the following steps: S1, belt scale batching: separately drying the high-moisture mud material in the ceramic raw material, and the other components in the ceramic raw material are respectively passed.
  • the ceramic raw material comprises the following components: the weight percentage of the formulation is 20.0% water content and the mud material is 4.50% first The mud component, the weight percentage is the moisture content of 21.5% water and the second mud component of the mud material is 4.50%, the water content is 3.80% water content and the stone material is 20.0% One stone component, the weight percentage is 2.50% water content and the stone material is 16.0% of the second stone component
  • weight percentage is The third soil component with a water content of 7.5% moisture and 11.0% soil, the water content of 3.90% by weight, and the raw coke component of 9.0% of the raw coke, the water content is water content.
  • the rate is 15.5% moisture and the porcelain edge grinding material is 2.0% porcelain edge grinding component, the water content is 12.1% moisture and the ceramic tile broken particles are 4.0% broken.
  • the granule component and the weight percentage were water having a water content of 9.3% and the polishing waste powder was 1.5% of the polished waste toner component.
  • the ceramic tile product produced by the above dry process can be accurately controlled, the production effect is more excellent, and the quality is more stable.
  • a ceramic powder formulation of the present embodiment comprises a first portion of mud comprising a moisture content of 11.25 and a dry content of 45, and a moisture content of 12.32 and
  • the second batch of dry material is 45 parts by weight, the moisture of 7.90 parts by weight and the dry material is 200 pieces of the first stone, the weight part is 4.10 parts of water and the dry material is 160 pieces of the second stone, and the parts by weight are 3.82 of water and dry material is the third stone of 85, the weight of 2.67 of water and the dry material is the first of 100
  • the solution also provides a manufacturing process for preparing the above ceramic powder formula, which comprises the following steps: S1, belt scale batching: separately drying the high-moisture mud material in the ceramic raw material, and the other components in the ceramic raw material are respectively passed.
  • the independent feeder and belt scale system are precisely compounded according to the proportion of ceramic raw materials;
  • S2 raw material homogenization bin the mixed raw materials after precise formulation by the belt scale are transported to the raw material homogenization bin, and the raw material homogenization bin is transported to the multi-stage Ball milling operation in the ball mill;
  • S3, mill configured hot air to dry grinding the above-mentioned mixed raw materials entering the mill;
  • S5 powder Material homogenization bin The above-mentioned powder is transferred to the powder homogenization bin for homogenization to further ensure the stability of the raw material components;
  • the granules are dried to the required water content of the finished product to achieve particle hardening and difficult to disperse;
  • particle grading optimization the dried granules are sorted by particle size, unqualified granules, Re-return granulation;
  • S11, finished product is ready for use qualified pellets are transported to the silo for use in the processing of the whole system;
  • the moisture and mud is 4.50% of the second mud component, the water content is 3.80% water content and the stone material is 20.0% of the first stone component, and the water content is 2.50% by weight.
  • the water and stone is 16.0% of the second stone component, the water content is 4.30% water content and the stone material is 8.50% of the third stone component, and the water content is 2.60% by weight.
  • the soil material is 10.0% of the first soil component, the water content is 2.90% moisture and the soil material is 8.0% of the second soil component, and the water content is 7.5% by weight.
  • Water and soil is 11.0% of the third soil component, the weight percentage is 3.90% water and the coke is 9.0% of the coke component, and the water percentage is 15.5% water.
  • the porcelain edge grinding material is 2.0% porcelain edge grinding component, the water content is 12.1% water content and the ceramic tile broken particle is 4.0% ceramic tile broken particle component and weight percentage It is a polishing waste powder component having a water content of 9.3% moisture and a polishing waste powder of 1.5%.
  • the above ceramic raw materials pass through 12 feeder belt scales, according to the proportion of the formula, the precision is controlled.
  • the mixed formula raw materials are conveyed to the raw material homogenization bin through the belt, and the raw materials are multi-stage superimposed and conveyed raw materials to the mill grinding powder.
  • the mill is equipped with a hot air drying system, and is dried at the same time of grinding processing. materials.
  • the qualified powder with a particle size of ⁇ 250 mesh and a water content of ⁇ 1% is air-selected to the dust collector and then transported to the powder homogenization bin.
  • the powder conveyed from the powder homogenization bin is subjected to slag removal and iron removal to ensure the quality of the powder, and then the powder is transported to a granulator for humidification (the powder is mixed with water to control the moisture content of the powder at 11%).
  • Granules after granulation, to the fluidized bed for drying and hardening, the moisture is controlled between 6% and 7%, and then the particle grading is screened.
  • the unqualified granule powder is returned to the granulator for regranulation, and the qualified granules are passed.
  • the powder is transported to the old warehouse for use, and the powder processing of the whole system is completed.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Treatment Of Sludge (AREA)
  • Compositions Of Oxide Ceramics (AREA)

Abstract

一种陶瓷粉料配方及其制作工艺。该陶瓷粉料包括：重量份为11.25的水份且干料为45的第一份泥料，重量份为12.32的水份且干料为45的第二份泥料，重量份为7.90的水份且干料为200的第一份石料，重量份为4.10的水份且干料为160的第二份石料，重量份为3.82的水份且干料为85的第三份石料，重量份为2.67的水份且干料为100的第一份土料，重量份为2.39的水份且干料为80的第二份土料，重量份为8.92的水份且干料为110的第三份土料，重量份为3.65的水份且干料为90的生焦，重量份为3.67的水份且干料为20的瓷边磨边料，重量份为5.51的水份且干料为40的瓷片砖破碎颗粒以及重量份为1.54的水份且干料为15的抛光废粉。

Description

一种陶瓷粉料配方及其制作工艺 技术领域
本发明涉及陶瓷生产技术领域，尤其涉及到一种陶瓷粉料配方及其制作工艺。
背景技术
在陶瓷行业的粉料制备工艺中，传统方法都采用湿法制粉，把配方原料加水在球磨中研磨，其浆料含水率到达34％～38％，再通过喷雾塔造粒、烘干，成品颗粒料保持水分为6％～7％，再到料仓陈腐待用。
传统的湿法制粉技术，占地面积大、用电量大、操作人员分散，人员成本高，使得原料制造成本居高不下。
传统的湿法制粉技术，从浆料水分34％～38％烘干到粉料水分6％～7％，需要耗损大量的热能，煤粉的燃烧，废气的排放、污水的排放，给环境造成严重的污染，已经严重背离国家提倡的节能减排政策。
由鉴于此，对于传统的湿法制粉技术中，减少设备用地面积、降低人工成本、节省设备用电量、响应国家提倡的节能减排政策，简单可靠的新工艺就显得尤为重要。
发明内容
本发明的目的在于解决传统湿法制粉技术中高排放、高污染的问题，克服现有技术的不足，提供一种制作效果好、成本低廉且制作工艺简单可靠的陶瓷粉料干法制粉技术新工艺。
为实现上述目的，本发明所提供的技术方案为：一种陶瓷粉料配方，其包括包含重量份为11.25的水份且干料为45的第一份泥料、重量份为12.32的水份且干料为45的第二份泥料、重量份为7.90的水份且干料为200的第一份石料、重量份为4.10的水份且干料为160的第二份石料、重量份为3.82的水份且干料为85的第三份石料、重量份为2.67的水份且干料为100的第一份土料、重量份为2.39的水份且干料为80的第二份土料、重量份为8.92的水份且干料为110的第三份土料、重量份为3.65的水份且干料为90的生焦、重量份为3.67的水份且干料为20的瓷边磨边料、重量份为5.51的水份且干料为40的瓷片砖破碎颗粒以及重量份为1.54的水份且干料为15的抛光废粉。
同时，本方案还提供一种制作上述陶瓷粉料配方的制作工艺，其包括以下步骤:S1、皮带秤配料：将陶瓷原料中高水分的泥料进行单独干燥待用，陶瓷原料中其它成份分别通过独立的喂料机和皮带秤系统按照陶瓷原料配比精确配料；S2、原料均化仓：通过皮带秤精确 配方后的混合原料，输送到原料均化仓，由原料均化仓多级输送到球磨机内进行球磨作业；S3、磨机：配置热风对进入磨机的上述混合原料进行干燥粉磨；S4、粉料收存：将达到工艺要求的粉末料通过旋风级选收存；S5、粉料均化仓：将收存的上述粉料输送到粉料均化仓进行均化，进一步保证原料成份稳定；S6、粉料除渣除铁：将均化后的粉料多级输送并除去及粉料中的渣铁粉；S7、定量给水给料：粉料称重定量输送到造粒机，水组件定量给水增湿；S8、粉料增湿造粒：在造粒机内的粉料通过定量给水，保证粉料水份恒定，造粒机滚动搅拌，把粉料结粒，以便达到系统要求的粒径；S9、颗粒干燥硬化：造粒后的颗粒料，输送到流化床干燥系统，通过干燥，把颗粒了烘干到成品所需的含水量，达到颗粒硬化，不易分散；S10、颗粒级配优化：把干燥后的颗粒料，经过颗粒大小的分选，不合格的颗粒，重新返回造粒；S11、成品陈腐待用：合格的颗粒料输送到料仓陈腐待用完成了整套系统的粉料加工；S12、压机压制成型：把陈腐仓的成品粉料输送到压机压制成陶瓷砖产品；其中上述陶瓷原料包括以下组分：配方重量百分比为含水率为20.0％的水份且泥料为4.50％的第一份泥料组份、重量百分比为含水率为21.5％的水份且泥料为4.50％的第二份泥料组份、重量百分比为含水率为3.80％的水份且石料为20.0％的第一份石料组份、重量百分比为含水率为2.50％的水份且石料为16.0％的第二份石料组份、重量百分比为含水率为4.30％的水份且石料为8.50％的第三份石料组份、重量百分比为含水率为2.60％的水份且土料为10.0％的第一份土料组份、重量百分比为含水率为2.90％的水份且土料为8.0％的第二份土料组份、重量百分比为含水率为7.5％的水份且土料为11.0％的第三份土料组份、重量百分比为含水率为3.90％的水份且生焦为9.0％的生焦组份、重量百分比为含水率为15.5％的水份且瓷边磨边料为2.0％的瓷边磨边料组份、重量百分比为含水率为12.1％的水份且瓷片砖破碎颗粒为4.0％的瓷片砖破碎颗粒组份以及重量百分比为含水率为9.3％的水份且抛光废粉为1.5％的抛光废粉组份。
本方案通过采用上述干法工艺制作而成的陶瓷砖产品，其含水率可以得到精确控制，制作效果也更加优异，质量也更加稳定。
具体实施方式
下面结合具体实施例对本发明作进一步说明：
参见附图1所示，本实施例所述的一种陶瓷粉料配方，其包括包含重量份为11.25的水份且干料为45的第一份泥料、重量份为12.32的水份且干料为45的第二份泥料、重量份为7.90的水份且干料为200的第一份石料、重量份为4.10的水份且干料为160的第二份石料、重量份为3.82的水份且干料为85的第三份石料、重量份为2.67的水份且干料为100的第一份 土料、重量份为2.39的水份且干料为80的第二份土料、重量份为8.92的水份且干料为110的第三份土料、重量份为3.65的水份且干料为90的生焦、重量份为3.67的水份且干料为20的瓷边磨边料、重量份为5.51的水份且干料为40的瓷片砖破碎颗粒以及重量份为1.54的水份且干料为15的抛光废粉。
同时，本方案还提供一种制作上述陶瓷粉料配方的制作工艺，其包括以下步骤:S1、皮带秤配料：将陶瓷原料中高水分的泥料进行单独干燥待用，陶瓷原料中其它成份分别通过独立的喂料机和皮带秤系统按照陶瓷原料配比精确配料；S2、原料均化仓：通过皮带秤精确配方后的混合原料，输送到原料均化仓，由原料均化仓多级输送到球磨机内进行球磨作业；S3、磨机：配置热风对进入磨机的上述混合原料进行干燥粉磨；S4、粉料收存：将达到工艺要求的粉末料通过旋风级选收存；S5、粉料均化仓：将收存的上述粉料输送到粉料均化仓进行均化，进一步保证原料成份稳定；S6、粉料除渣除铁：将均化后的粉料多级输送并除去及粉料中的渣铁粉；S7、定量给水给料：粉料称重定量输送到造粒机，水组件定量给水增湿；S8、粉料增湿造粒：在造粒机内的粉料通过定量给水，保证粉料水份恒定，造粒机滚动搅拌，把粉料结粒，以便达到系统要求的粒径；S9、颗粒干燥硬化：造粒后的颗粒料，输送到流化床干燥系统，通过干燥，把颗粒了烘干到成品所需的含水量，达到颗粒硬化，不易分散；S10、颗粒级配优化：把干燥后的颗粒料，经过颗粒大小的分选，不合格的颗粒，重新返回造粒；S11、成品陈腐待用：合格的颗粒料输送到料仓陈腐待用完成了整套系统的粉料加工；S12、压机压制成型：把陈腐仓的成品粉料输送到压机压制成陶瓷砖产品；其中上述陶瓷原料包括以下组分：配方重量百分比为含水率为20.0％的水份且泥料为4.50％的第一份泥料组份、重量百分比为含水率为21.5％的水份且泥料为4.50％的第二份泥料组份、重量百分比为含水率为3.80％的水份且石料为20.0％的第一份石料组份、重量百分比为含水率为2.50％的水份且石料为16.0％的第二份石料组份、重量百分比为含水率为4.30％的水份且石料为8.50％的第三份石料组份、重量百分比为含水率为2.60％的水份且土料为10.0％的第一份土料组份、重量百分比为含水率为2.90％的水份且土料为8.0％的第二份土料组份、重量百分比为含水率为7.5％的水份且土料为11.0％的第三份土料组份、重量百分比为含水率为3.90％的水份且生焦为9.0％的生焦组份、重量百分比为含水率为15.5％的水份且瓷边磨边料为2.0％的瓷边磨边料组份、重量百分比为含水率为12.1％的水份且瓷片砖破碎颗粒为4.0％的瓷片砖破碎颗粒组份以及重量百分比为含水率为9.3％的水份且抛光废粉为1.5％的抛光废粉组份。
工作时，上述陶瓷原料通过12台喂料机皮带秤，按照配方比例配料，精度控制在 1％以内，将混合配方原料通过皮带输送到原料均化仓，从原料均化仓多级叠加输送原料到磨机磨粉，磨机配置有热风烘干系统，在磨粉加工的同时烘干物料。粒径<250目、水分<1％的合格粉料通过风选到集尘器，再输送到粉料均化仓。从粉料均化仓输送出来的粉料进行除渣除铁，保证粉料的品质，之后粉料输送到造粒机进行增湿(粉料加水搅拌，控制粉料含水率在11％)造粒，造粒后到流化床进行烘干硬化，水分控制在6％～7％之间，再进行颗粒级配筛选，不合格的颗粒粉料返回造粒机重新造粒，把合格的颗粒粉料输送到陈腐仓待用，完成整套系统的粉料加工。
另外，请参照下图表1所示，可以看出本方案中的上述干法制粉工艺相对于传统的湿法制粉工艺具有优异的技术效果：
Figure PCTCN2016084757-appb-000001
表一
以上所述之实施例子只为本发明之较佳实施例，并非以此限制本发明的实施范围，故凡依本发明之形状、原理所作的变化，均应涵盖在本发明的保护范围内。

Claims (2)

  1. 一种陶瓷粉料配方，其特征在于：包括包含重量份为11.25的水份且干料为45的第一份泥料、重量份为12.32的水份且干料为45的第二份泥料、重量份为7.90的水份且干料为200的第一份石料、重量份为4.10的水份且干料为160的第二份石料、重量份为3.82的水份且干料为85的第三份石料、重量份为2.67的水份且干料为100的第一份土料、重量份为2.39的水份且干料为80的第二份土料、重量份为8.92的水份且干料为110的第三份土料、重量份为3.65的水份且干料为90的生焦、重量份为3.67的水份且干料为20的瓷边磨边料、重量份为5.51的水份且干料为40的瓷片砖破碎颗粒以及重量份为1.54的水份且干料为15的抛光废粉。
  2. 一种用于制造权利要求1所述陶瓷粉料配方的制作工艺，其特征在于：包括以下步骤:S1、皮带秤配料：将陶瓷原料中高水分的泥料进行单独干燥待用，陶瓷原料中其它成份分别通过独立的喂料机和皮带秤系统按照陶瓷原料配比精确配料；S2、原料均化仓：通过皮带秤精确配方后的混合原料，输送到原料均化仓，由原料均化仓多级输送到球磨机内进行球磨作业；S3、磨机：配置热风对进入磨机的上述混合原料进行干燥粉磨；S4、粉料收存：将达到工艺要求的粉末料通过旋风级选收存；S5、粉料均化仓：将收存的上述粉料输送到粉料均化仓进行均化，进一步保证原料成份稳定；S6、粉料除渣除铁：将均化后的粉料多级输送并除去及粉料中的渣铁粉；S7、定量给水给料：粉料称重定量输送到造粒机，水组件定量给水增湿；S8、粉料增湿造粒：在造粒机内的粉料通过定量给水，保证粉料水份恒定，造粒机滚动搅拌，把粉料结粒，以便达到系统要求的粒径；S9、颗粒干燥硬化：造粒后的颗粒料，输送到流化床干燥系统，通过干燥，把颗粒了烘干到成品所需的含水量，达到颗粒硬化，不易分散；S10、颗粒级配优化：把干燥后的颗粒料，经过颗粒大小的分选，不合格的颗粒，重新返回造粒；S11、成品陈腐待用：合格的颗粒料输送到料仓陈腐待用完成了整套系统的粉料加工；S12、压机压制成型：把陈腐仓的成品粉料输送到压机压制成陶瓷砖产品；其中上述陶瓷原料包括以下组分：配方重量百分比为含水率为20.0％的水份且泥料为4.50％的第一份泥料组份、重量百分比为含水率为21.5％的水份且泥料为4.50％的第二份泥料组份、重量百分比为含水率为3.80％的水份且石料为20.0％的第一份石料组份、重量百分比为含水率为2.50％的水份且石料为16.0％的第二份石料组份、重量百分比为含水率为4.30％的水份且石料为8.50％的第三份石料组份、重量百分比为含水率为2.60％的水份且土料为10.0％的第一份土料组份、重量百分比为含水率为2.90％的水份且土料为8.0％的第二份土料组份、重量百分比为含水率为7.5％的水份且土料为11.0％的第三份土料组份、重量百分比为含水率为3.90％的水份且生焦为9.0％的生焦组份、重量百分比为含水率为15.5％的水份且瓷边磨边料 为2.0％的瓷边磨边料组份、重量百分比为含水率为12.1％的水份且瓷片砖破碎颗粒为4.0％的瓷片砖破碎颗粒组份以及重量百分比为含水率为9.3％的水份且抛光废粉为1.5％的抛光废粉组份。
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