Abstract:
The present invention relates to an apparatus for manufacturing a cement clinker which comprises: a first mixing and melting region which mixes and melts sub-material flowed in from a first inlet and molten slag flowed in from a second inlet; a second mixing and melting region which mixes and melts products from the first mixing and melting region for the second time; a first clinkering region which selectively sorts unreacted sub-materials which passed the second mixing and melting region to discharge to the lower part and clinkers remnants from the sorting process; and a second clinkering region which clinkers products passed through the first clinkering region to discharge for cooling and pulverizing processes. According to the present invention, molten slag which is wasted as a byproduct in iron industry is recycled and is environment-friendly. In addition, using the heat of slag in molten condition at a high temperature enables energy sources for manufacturing a clinker to be reduced and reduces CO2 generation due to combustion of fuel. Furthermore, processes for manufacturing clinkers are continuously performed to improve productivity, thereby ensuring uniform physical properties and quality of products.
Abstract:
PURPOSE: A composition for a cement clinker grinding agent is provided to prevent aggregation and shorten clinker grinding time by containing grinding aids with a zwitterion structure compound. CONSTITUTION: A composition for a cement clinker grinding aid comprises a grinding aid. The grinding aid comprises zwitterion structure compound represented by the chemical formula 1. X, Y, and Z of the chemical formula 1 are independently non-polar functional groups, and W is a polar functional group. The grinding aid includes at least one of glycol and amine. The composition for the cement clinker grinding aid further includes at least one of a hydration retarder and a hydration facilitator by 0.001-10,000 parts by weight. The cement clinker composition comprises the cement clinker and the composition for the cement clinker grinding aid. The composition for the cement clinker grinding aid is 0.001-1.0 parts by weight based on 100.0 of the cement clinker.
Abstract:
PURPOSE: A composition containing sodium silicate hydrate is provided to improve fineness and pulverization efficiency of minerals. CONSTITUTION: A composition for grinding minerals contains a glycol-based ingredient, an amine-based ingredient, and sodium silicate(Na2Sio3) hydrate. The glycol-based ingredient is selected from the group consisting of DEG(diethylene glycol), MEG(monoethylene glycol), and TEG(triethylene glycol). The amine-based ingredient is selected from the group consisting of DEG(diethylene glycol), MEG(monoethylene glycol), and TEG(triethylene glycol).
Abstract:
PURPOSE: Clinker using steel making sludge and municipal solid wastes-based incineration fly ash and a method for manufacturing the same are provided to improve the mobility and the expandability of the clinker by mixing steel making sludge, municipal solid wastes-based incineration fly ash, and gypsum in a pre-set ratio. CONSTITUTION: A method for manufacturing clinker includes the following: 20 to 50 weight% of municipal solid wastes-based incineration fly ash and 10 to 30 weight% of gypsum with 100 weight% of steel making sludge. A mixture is obtained. The mixture is sintered at temperature between 1000 and 1300 degrees Celsius. The gypsum is selected from a group including Phosphogypsum, titanium gypsum, flue-gas desulfurization gypsum, natural gypsum, and anhydrous gypsum.
Abstract:
본 발명은 시멘트의 초기 강도 발현 및 경화를 주도하거나 필요성에 의해 응결 또는 경화시간을 단축하거나 수화반응성의 촉진을 도모하기 위하여, 석회질원과 알루미나질원을 출발원료로 하여 이를 열처리하여 1차 소성한 후, 이를 수화시켜 수화물을 합성하고, 이 수화물을 다시 2차 소성하는 방법을 통해 CaO-Al 2 O 3 계 클링커를 제조하는 방법에 관한 것으로, 본 발명에 따르면, 수화반응성이 우수한 고품질 CaO-Al 2 O 3 계 클링커를 낮은 소성온도에서 합성할 수 있고, 이로 인하여 기능성 특수시멘트용 첨가제의 제조비용을 낮출 수 있고, 토목·건축분야에 고성능 콘크리트용 혼합재의 보급을 원활하게 공급할 수 있는 효과가 있다. C3A, C12A7, 수화물, C3AH6, 에트린자이트, 특수시멘트용 첨가제, 시멘트 혼화제
Abstract:
PURPOSE: A method for preparing a calcium-aluminate clinker through a hydride plasticization method is provided to produce C3A and C12A7 of high-quality CaO-Al2O3-based clinker without the repeated calcinations and fusions. CONSTITUTION: A method for preparing a calcium-aluminate clinker through a hydride plasticization method comprises the following steps of: mixing a calcareous source(CaO) and alumina source(Al2O3) in a ratio of 3:1 or 12:7 to obtain a mixture; calcining the mixture at 1,000 ~ 1,400°C and fast-cooling it to obtain a calciums-aluminate-based wettable compound; adding water to the calciums-aluminate-based wettable compound and obtaining a CaO-Al2O3-H2O-based hydrate; and re-calcining the CaO-Al2O3-H2O-based hydrate at 300 ~ 1,500°C and fast-cooling it in order to obtain a CaO-Al2O3-based clinker.
Abstract translation:目的:提供一种通过氢化物增塑法制备铝酸钙熟料的方法,以生产高质量CaO-Al2O3基熟料的C3A和C12A7,无需重复煅烧和熔融。 构成:通过氢化物增塑法制备铝酸钙熟料的方法包括以下步骤:以3:1或12:7的比例混合钙质源(CaO)和氧化铝源(Al 2 O 3),以获得混合物 ; 在1,000〜1400℃下煅烧该混合物并快速冷却,得到基于铝酸钙的可湿性化合物; 向基于铝酸钙的可湿性化合物中加入水,得到CaO-Al2O3-H2O类水合物; 并在300〜1500℃下重新煅烧CaO-Al2O3-H2O基水合物,并快速冷却,以获得CaO-Al2O3基熟料。
Abstract:
A process for producing a geopolymer cement from fly ash and granulated blast furnace slag is provided to reduce the energy consumption by simple processing steps, to prevent emission of CO2, and to improve the strength development and setting characteristics of a geopolymer cement product. A process for producing a geopolymer cement from fly ash and granulated blast furnace slag comprises the steps of: (a) finely milling and/or mechanically activating granulated blast furnace slag for 10-120 minutes to reduce the size of the granulated blast furnace slag to less than 100 micrometers; and (b) mixing 5-22 wt% of the micropowder of the granulated blast furnace slag obtained in step (a) intimately with 60-90 wt% of fly ash obtained from a thermal power generation system and 3-20 wt% of an alkaline activating agent in a mechanical mixer for 5-30 minutes.
Abstract:
Described is a method as well as a plant for preheating particulate or pulverulent material such as cement raw meal or similar material in a cyclone preheater (1), comprising at least two cyclone stages, each comprising a riser duct (2a, 2b, 2c, 2d) and a cyclone (1a, 1b, 1c, 1d). The method is peculiar in that a portion of the material which is fed to at least one cyclone stage is introduced to the first part of the riser duct, viewed in the direction of travel of the exhaust gases, and is heated from a temperature of maximum 450 °C to a temperature of at least 550 °C, and in that the remaining material which is fed to the same cyclone stage is introduced into the last part of the said riser duct. As a result, there will be a reduction in the amount of SO2 which is discharged from the cement plant preheater as emission, without a simultaneous increase in energy consumption.
Abstract:
Hydraulic cements are produced by combining a clay phase with calcium carbonate and then heating to 700-900 deg.C in the presence of a carbon dioxide atmosphere to prevent dissociation of calcium carbonate, to activate the clay phase by dehydroxylation (pozzolanic activation) and reaction with the calcium carbonate, mixing 95% of this material with an activating material e.g. conventional cement clinker. The process needs less energy and reduces environmental pollution.