CN115286269A - A method for improving the stability of clinker by using industrial flue gas - Google Patents
A method for improving the stability of clinker by using industrial flue gas Download PDFInfo
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Abstract
一种利用工业烟气提高熟料安定性的方法。涉及建筑材料制备技术领域。包括以下步骤:步骤1,将常规水泥生料经常规煅烧工艺高温煅烧后,自然或加速冷却至室温,获得常规熟料;步骤2,将步骤1制得的熟料破碎或粉磨至粒径≤1mm,储存至熟料库;步骤3,将含CO2的烟气注入熟料库中,保证熟料库中CO2浓度至少为注入烟气的80%,制得安定性优异的熟料。步骤3中烟气注入时间为30min~360min。步骤3中含CO2的烟气中CO2浓度≥20%。本发明通过工业烟气对已制成熟料的碳化处置,有效降低熟料中对水泥安定性不利的主要成分(即游离氧化钙和氧化镁)含量,相应生成了性能稳定的碳酸盐,为改善或提升熟料安定性提供了新路径。
A method for improving the stability of clinker by utilizing industrial flue gas. The invention relates to the technical field of construction material preparation. The following steps are included: Step 1, after the conventional cement raw meal is calcined at a high temperature by a conventional calcination process, and cooled to room temperature naturally or accelerated to obtain conventional clinker; Step 2, the clinker obtained in step 1 is crushed or ground to a particle size ≤1mm, store it in the clinker silo; Step 3, inject the flue gas containing CO 2 into the clinker silo to ensure that the CO 2 concentration in the clinker silo is at least 80% of the injected flue gas, so as to obtain clinker with excellent stability . In step 3, the flue gas injection time is 30 min to 360 min. In step 3, the concentration of CO 2 in the flue gas containing CO 2 is ≥20%. The present invention effectively reduces the content of main components (namely free calcium oxide and magnesium oxide) in the clinker that are unfavorable to the stability of the cement through the carbonization treatment of the prepared clinker by industrial flue gas, and accordingly generates carbonate with stable performance. It provides a new way to improve or enhance the stability of clinker.
Description
技术领域technical field
本发明涉及建筑材料制备技术领域,尤其涉及一种利用工业烟气提高熟料安定性的方法。The invention relates to the technical field of building material preparation, in particular to a method for improving the stability of clinker by using industrial flue gas.
背景技术Background technique
水泥的安定性亦称水泥体积安定性,反映水泥在凝结硬化过程中体积变化的均匀情况,是水泥生产企业、工程单位重点关注指标之一;安定性不合格的水泥是引发工程事故的原因之一。The stability of cement, also known as cement volume stability, reflects the uniformity of the volume change of cement in the process of setting and hardening, and is one of the key indicators for cement production enterprises and engineering units; cement with unqualified stability is one of the causes of engineering accidents one.
水泥的安定性主要源于熟料质量,硅酸盐熟料经常规煅烧工艺煅烧后,一般残存有少量的游离氧化钙和氧化镁,按照水泥水化相关理论,游离氧化钙和氧化镁的水化会引起水泥试体膨胀开裂,引发安定性问题。如何保证熟料的安定性成为水泥安定性质量控制的关键。目前已知的熟料安定性的提升办法主要侧重于熟料烧成工艺的控制,尚无对已制成的熟料的安定性提升的有效办法。李卫宁在《改善水泥安定性提高熟料质量的方法》一文中提出了一种在立窑煅烧中对助燃空气增湿来改善出窑熟料安定性的方式,但该方式对喷水量控制较为严苛,喷水量过高会降低熟料强度。The stability of cement is mainly due to the quality of the clinker. After the silicate clinker is calcined by the conventional calcination process, there are generally a small amount of free calcium oxide and magnesium oxide remaining. According to the relevant theory of cement hydration, the water content of free calcium oxide and magnesium oxide Melting will cause the cement specimen to expand and crack, causing stability problems. How to ensure the stability of clinker becomes the key to the quality control of cement stability. The currently known methods for improving the stability of clinker mainly focus on the control of the clinker firing process, and there is no effective method for improving the stability of clinker that has been produced. Li Weining proposed a way to improve the stability of the kiln clinker by humidifying the combustion-supporting air in the vertical kiln calcination in the article "Methods for Improving the Stability of Cement and Improving the Quality of Clinker", but this method is relatively difficult to control the amount of water sprayed. Strict, excessive water spray will reduce the clinker strength.
水泥、石灰行业作为典型的高碳排放行业,是国家“双碳”政策落实过程中的重点关注对象。以水泥行业为例,我国水泥年产量约23亿吨,按照熟料占比80%计,全国熟料年产量约18.4亿吨,吨熟料碳排放按850~860kg计,年二氧化碳排放量约15.6亿吨,占全国碳排放总量的15%左右。在应对气候变化过程中,碳排放权交易被视为长期视角下最具操作性的政策工具。全国碳市场于2021年7月16日启动,火电企业率先进入全国碳交易市场,石化、化工、建材、钢铁、有色金属、造纸、航空其他7个高排放行业将陆续纳入,碳排放配额的分配以免费分配为主,适时引入有偿分配,通过低成本手段降低熟料的碳排放总量成为水泥行业未来重点发展和研究方向。Cement and lime industries, as typical high-carbon emission industries, are the focus of attention during the implementation of the national "double carbon" policy. Taking the cement industry as an example, the annual output of cement in my country is about 2.3 billion tons. Based on clinker accounting for 80%, the national annual output of clinker is about 1.84 billion tons. The carbon emission per ton of clinker is 850-860kg, and the annual carbon dioxide emission is about 1.56 billion tons, accounting for about 15% of the country's total carbon emissions. In the process of addressing climate change, carbon emissions trading is considered the most operational policy tool from a long-term perspective. The national carbon market will be launched on July 16, 2021. Thermal power companies will take the lead in entering the national carbon trading market. Petrochemical, chemical, building materials, steel, non-ferrous metals, papermaking, and aviation will be included in seven other high-emission industries one after another. The allocation of carbon emission quotas Focusing on free distribution, timely introduction of paid distribution, and reducing the total carbon emissions of clinker through low-cost means have become the key development and research directions of the cement industry in the future.
发明内容Contents of the invention
本发明针对以上问题,提供了一种有效提升熟料安定性同时吸收工业烟气中的CO2,降低工业碳排放总量的一种利用工业烟气提高熟料安定性的方法。Aiming at the above problems, the present invention provides a method for improving the stability of clinker by using industrial flue gas to effectively improve the stability of clinker while absorbing CO 2 in industrial flue gas and reducing the total amount of industrial carbon emissions.
本发明的技术方案是:一种利用工业烟气提高熟料安定性的方法,包括以下步骤:The technical solution of the present invention is: a method for improving the stability of clinker by using industrial flue gas, comprising the following steps:
步骤1,将常规水泥生料经常规煅烧工艺高温煅烧后,自然或加速冷却至室温,获得常规熟料;Step 1. After the conventional cement raw meal is calcined at a high temperature by a conventional calcination process, it is naturally or accelerated cooled to room temperature to obtain conventional clinker;
步骤2,将步骤1制得的熟料破碎或粉磨至粒径≤1mm,储存至熟料库;Step 2, crushing or grinding the clinker prepared in step 1 to a particle size ≤ 1mm, and storing it in a clinker warehouse;
步骤3,将含CO2的烟气注入熟料库中,保证熟料库中CO2浓度至少为注入烟气的80%,制得安定性优异的熟料。Step 3, injecting the flue gas containing CO 2 into the clinker storehouse, ensuring that the CO 2 concentration in the clinker storehouse is at least 80% of the injected flue gas, and producing clinker with excellent stability.
具体的,步骤3中烟气注入时间为30min~360min。Specifically, the flue gas injection time in step 3 is 30 minutes to 360 minutes.
具体的,步骤3中含CO2的烟气中CO2浓度≥20%。Specifically, the concentration of CO 2 in the flue gas containing CO 2 in step 3 is ≥20%.
具体的,含CO2的烟气包括水泥行业排放的烟气或石灰行业排放的烟气。Specifically, the flue gas containing CO 2 includes the flue gas emitted from the cement industry or the flue gas emitted from the lime industry.
具体的,步骤3中烟气的温度为200℃~500℃。Specifically, the temperature of the flue gas in step 3 is 200°C to 500°C.
本发明的有益效果:Beneficial effects of the present invention:
1)本发明通过工业烟气对已制成熟料的碳化处置,有效降低熟料中对水泥安定性不利的主要成分(即游离氧化钙和氧化镁)含量,相应生成了性能稳定的碳酸盐,为改善或提升熟料安定性提供了新路径。1) The present invention effectively reduces the content of the main components (ie, free calcium oxide and magnesium oxide) in the clinker that are unfavorable to the stability of cement through the carbonization treatment of the clinker produced by industrial flue gas, and correspondingly generates carbonic acid with stable performance. Salt provides a new way to improve or enhance the stability of clinker.
2)我国作为水泥大国,水泥熟料产量同样位居世界第一,按游离氧化钙0.8%,氧化镁3.50%计,完全反应时可吸收CO2 4.48%,按全国熟料年产量18.4亿吨计算,可吸收CO20.824亿吨,2021年中国碳市场年报显示,中国全年碳配额均价为42.85元/吨,可间接降低水泥行业碳排放成本35.32亿元,颇具发展潜力和前景。2) China, as a big cement country, also ranks first in the world in terms of cement clinker output, based on 0.8% of free calcium oxide and 3.50% of magnesium oxide, it can absorb 4.48% of CO 2 when fully reacted, and the annual output of clinker in the country is 1.84 billion tons According to calculations, 82.4 million tons of CO 2 can be absorbed. The 2021 China Carbon Market Annual Report shows that the average price of China's annual carbon allowances is 42.85 yuan/ton, which can indirectly reduce the carbon emission cost of the cement industry by 3.532 billion yuan, which has considerable development potential and prospects.
3)利用工业烟气中的高温,可以实现熟料二次激活,提升熟料水化活性,对熟料活性提升有利。3) Using the high temperature in industrial flue gas, the secondary activation of clinker can be realized, and the hydration activity of clinker can be improved, which is beneficial to the improvement of clinker activity.
附图说明Description of drawings
图1是本发明方法实施流程图。Fig. 1 is the flow chart of the implementation of the method of the present invention.
具体实施方式Detailed ways
针对重大工程对水泥安定性提出的严格要求,结合当前国家对高碳排放行业绿色低碳转型的迫切需要,以熟料绿色低碳、高质量制备为目标导向,本发明提出了一种利用工业烟气提高熟料安定性的方法,目的在于有效提升熟料安定性同时吸收工业烟气中的CO2,降低工业碳排放总量。In view of the strict requirements on the stability of cement put forward by major projects, combined with the current national urgent needs for green and low-carbon transformation of high-carbon emission industries, and with the goal of clinker green, low-carbon, and high-quality preparation, the present invention proposes a method of using industrial The method for improving the stability of clinker by flue gas aims to effectively improve the stability of clinker while absorbing CO 2 in industrial flue gas and reducing the total amount of industrial carbon emissions.
碳捕集及利用技术被誉为实现碳中和、碳达峰目标最有效的措施之一,将烟气中的CO2低成本捕集或直接利用则是碳捕集及利用技术的核心目标。根据酸碱中和理论,熟料中的游离氧化钙和氧化镁为典型的高活性碱金属氧化物,理论上可以与CO2这类酸性气体其他反应,生成稳定性良好的碳酸盐,如碳酸钙和碳酸镁。可提升熟料安定性同时减少水泥工业碳排放。熟料中游离氧化钙一般在0.3%~1.3%,平均值约0.8%,氧化镁一般在1.0%~4.8%,平均值均3.50%。按游离氧化钙0.8%,氧化镁3.50%计,完全反应时可吸收CO2 4.48%,按全国熟料年产量18.4亿吨计算,可吸收CO2 0.824亿吨,2021年中国碳市场年报显示,中国全年碳配额均价为42.85元/吨,可间接降低水泥行业碳排放成本35.32亿元,颇具发展潜力和前景。Carbon capture and utilization technology is known as one of the most effective measures to achieve carbon neutrality and carbon peaking goals. The low-cost capture or direct utilization of CO2 in flue gas is the core goal of carbon capture and utilization technology . According to the theory of acid-base neutralization, free calcium oxide and magnesium oxide in clinker are typical highly active alkali metal oxides, which can theoretically react with other acid gases such as CO2 to form carbonates with good stability, such as Calcium Carbonate and Magnesium Carbonate. It can improve the stability of clinker and reduce carbon emissions in the cement industry. Free calcium oxide in clinker is generally 0.3%~1.3%, with an average value of about 0.8%, and magnesium oxide is generally 1.0%~4.8%, with an average value of 3.50%. Based on 0.8% of free calcium oxide and 3.50% of magnesium oxide, 4.48% of CO 2 can be absorbed when fully reacted, and 82.4 million tons of CO 2 can be absorbed based on the national annual clinker output of 1.84 billion tons. According to the 2021 China Carbon Market Annual Report, The average price of China's annual carbon quota is 42.85 yuan/ton, which can indirectly reduce the carbon emission cost of the cement industry by 3.532 billion yuan, which has considerable development potential and prospects.
一种利用工业烟气提高熟料安定性的方法,包括以下步骤:A method for improving the stability of clinker by using industrial flue gas, comprising the following steps:
步骤1,将常规水泥生料经常规煅烧工艺高温煅烧后,自然或加速冷却至室温,获得常规熟料;Step 1. After the conventional cement raw meal is calcined at a high temperature by a conventional calcination process, it is naturally or accelerated cooled to room temperature to obtain conventional clinker;
步骤2,将步骤1制得的熟料破碎或粉磨至粒径≤1mm,储存至熟料库;Step 2, crushing or grinding the clinker prepared in step 1 to a particle size ≤ 1mm, and storing it in a clinker warehouse;
本发明将熟料破碎或粉磨至粒径≤1mm目的为:In the present invention, the purpose of crushing or grinding the clinker to a particle size ≤ 1mm is:
生产制备过程中气固反应的速率同时与气体浓度和接触面积相关,熟料中游离氧化钙和氧化镁与CO2的反应速率与熟料的粒度或细度成反比,即粒度或细度越小,反应越快越充分。The rate of gas-solid reaction in the production and preparation process is related to the gas concentration and contact area at the same time. The reaction rate of free calcium oxide and magnesium oxide in the clinker and CO2 is inversely proportional to the particle size or fineness of the clinker, that is, the finer the particle size or fineness The smaller, the quicker and fuller the response.
步骤3,将含CO2的烟气注入熟料库中,保证熟料库中CO2浓度至少为注入烟气的80%,制得安定性优异的熟料。Step 3, injecting the flue gas containing CO 2 into the clinker storehouse, ensuring that the CO 2 concentration in the clinker storehouse is at least 80% of the injected flue gas, and producing clinker with excellent stability.
进一步限定,步骤3中烟气注入时间为30min~360min。It is further defined that the flue gas injection time in step 3 is 30 minutes to 360 minutes.
进一步限定,步骤3中含CO2的烟气中CO2浓度≥20%。It is further defined that the concentration of CO 2 in the flue gas containing CO 2 in step 3 is ≥20%.
高浓度的CO2氛围条件下,硅酸盐熟料中游离氧化钙和氧化镁会逐步发生碳化,即与CO2反应生成碳酸钙和碳酸镁。Under the condition of high-concentration CO2 atmosphere, the free calcium oxide and magnesium oxide in the silicate clinker will be gradually carbonized, that is, they will react with CO2 to form calcium carbonate and magnesium carbonate.
进一步限定,含CO2的烟气包括但不限于水泥行业排放的烟气或石灰行业排放的烟气。Further defined, CO2 -containing flue gas includes, but is not limited to, flue gas emitted from the cement industry or flue gas emitted from the lime industry.
进一步限定,步骤3中烟气的温度为200℃~500℃,可以对熟料进行二次激活,提升熟料的水化活性。It is further defined that the temperature of the flue gas in step 3 is 200°C to 500°C, which can reactivate the clinker to increase the hydration activity of the clinker.
实施例1Example 1
一种利用工业烟气提高熟料安定性的方法。首先采用常规工艺烧制普通硅酸盐水泥熟料,将所烧得熟料快速冷却至室温,并将其破碎至粒径≤1mm,转入熟料库。向熟料库中持续通入水泥窑烟气,其中烟气CO2含量24%,仓内实际CO2含量21%。持续通入烟气180min后制得改性普通硅酸盐水泥熟料。随后按熟料94%,石膏6%比例混合并粉磨,制得硅酸盐水泥。A method for improving the stability of clinker by using industrial flue gas. First, ordinary portland cement clinker is fired by conventional technology, and the clinker is quickly cooled to room temperature, crushed to a particle size of ≤1mm, and transferred to the clinker storage. The cement kiln flue gas is continuously fed into the clinker warehouse, the CO 2 content of the flue gas is 24%, and the actual CO 2 content in the warehouse is 21%. The modified ordinary Portland cement clinker was prepared after continuously feeding flue gas for 180 minutes. Then mix and grind according to the ratio of 94% clinker and 6% gypsum to make Portland cement.
实施例2Example 2
一种利用工业烟气提高熟料安定性的方法。首先采用常规工艺烧制普通硅酸盐水泥熟料,将所烧得熟料快速冷却至室温,并将其破碎至粒径≤1mm,转入熟料库。向熟料库中持续通入石灰窑烟气,其中烟气CO2含量36%,仓内实际CO2含量29%。持续通入烟气180min后制得改性普通硅酸盐水泥熟料。随后按熟料94%,石膏6%比例混合并粉磨,制得硅酸盐水泥。A method for improving the stability of clinker by using industrial flue gas. First, ordinary portland cement clinker is fired by conventional technology, and the clinker is quickly cooled to room temperature, crushed to a particle size of ≤1mm, and transferred to the clinker storage. The lime kiln flue gas is continuously fed into the clinker storehouse, the CO 2 content of the flue gas is 36%, and the actual CO 2 content in the warehouse is 29%. The modified ordinary Portland cement clinker was prepared after continuously feeding flue gas for 180 minutes. Then mix and grind according to the ratio of 94% clinker and 6% gypsum to make Portland cement.
实施例3Example 3
一种利用工业烟气提高熟料安定性的方法。首先采用常规工艺烧制中热硅酸盐水泥熟料,将所烧得熟料快速冷却至室温,并将其破碎至粒径≤1mm,转入熟料库。向熟料库中持续通入水泥窑烟气,其中烟气CO2含量26%,仓内实际CO2含量22%。持续通入烟气180min后制得改性中热硅酸盐水泥熟料。随后按熟料94%,石膏6%比例混合并粉磨,制得硅酸盐水泥。A method for improving the stability of clinker by using industrial flue gas. Firstly, medium-heat Portland cement clinker is fired by conventional technology, and the fired clinker is rapidly cooled to room temperature, crushed to a particle size of ≤1mm, and transferred to the clinker storage. The cement kiln flue gas is continuously fed into the clinker warehouse, the CO 2 content of the flue gas is 26%, and the actual CO 2 content in the warehouse is 22%. The modified medium-heat Portland cement clinker was prepared after continuously feeding flue gas for 180 minutes. Then mix and grind according to the ratio of 94% clinker and 6% gypsum to make Portland cement.
实施例4Example 4
一种利用工业烟气提高熟料安定性的方法。首先采用常规工艺烧制低热硅酸盐水泥熟料,将所烧得熟料快速冷却至室温,并将其破碎至粒径≤1mm,转入熟料库。向熟料库中持续通入水泥窑烟气,其中烟气CO2含量29%,仓内实际CO2含量23%。持续通入烟气180min后制得改性低热硅酸盐水泥熟料。随后按熟料94%,石膏6%比例混合并粉磨,制得硅酸盐水泥。A method for improving the stability of clinker by using industrial flue gas. Firstly, the low-heat Portland cement clinker is fired by the conventional process, and the burned clinker is rapidly cooled to room temperature, crushed to a particle size ≤ 1mm, and transferred to the clinker storage. The cement kiln flue gas is continuously fed into the clinker warehouse, the CO 2 content of the flue gas is 29%, and the actual CO 2 content in the warehouse is 23%. The modified low-heat Portland cement clinker was prepared after continuously feeding flue gas for 180 minutes. Then mix and grind according to the ratio of 94% clinker and 6% gypsum to make Portland cement.
将实施例1-4中采用的未改性熟料按熟料94%,石膏6%比例混合并粉磨分别制得对照组水泥。按照GB/T 176-2017水泥化学分析方法测定游离氧化钙(f-CaO)、游离氧化镁(f-CaO)含量,按照GB/T 1346-2011水泥标准稠度用水量、凝结时间、安定性检验方法采用雷氏夹法检验各实施例及对照组水泥安定性。各实施例及对照组体积安定性及及游离氧化钙、游离氧化镁含量如表1所示。The unmodified clinker used in Examples 1-4 was mixed at a ratio of 94% clinker and 6% gypsum and ground to prepare the cement of the control group. Determination of free calcium oxide (f-CaO) and free magnesium oxide (f-CaO) content according to GB/T 176-2017 cement chemical analysis method, water consumption, setting time and stability inspection according to GB/T 1346-2011 cement standard consistency Methods The stability of the cement in each example and control group was tested by Rayleigh clip method. The volume stability and free calcium oxide and free magnesium oxide contents of each embodiment and control group are shown in Table 1.
表1 各实施例、对照组体积安定性及游离氧化钙、游离氧化镁含量Table 1 Volume stability and free calcium oxide, free magnesium oxide content of each embodiment, control group
按照参照GB/T 17671-1999水泥胶砂强度检验方法(ISO法)制作水泥胶砂强度试件并进行物理性能试验,对比实施例与对照组物理性能。各实施例与对照组抗压强度发展如表2所示。According to the reference GB/T 17671-1999 cement mortar strength test method (ISO method), the cement mortar strength test piece was made and the physical property test was carried out, and the physical properties of the examples and the control group were compared. The development of compressive strength of each embodiment and control group is shown in Table 2.
表2 各实施例、对照实现体积安定性及及氧化钙含量Table 2 each embodiment, control realize volume stability and calcium oxide content
本发明专利旨在利用硅酸盐熟料中的游离氧化钙和氧化镁来吸收工业烟气中二氧化碳,实现熟料安定性质量整体提升同时,达成熟料低碳制备目标,为熟料质量提升和传统高碳排放工业低碳转型提供新路径。The patent of the invention aims to use the free calcium oxide and magnesium oxide in the silicate clinker to absorb carbon dioxide in the industrial flue gas, realize the overall improvement of the stability and quality of the clinker, and at the same time achieve the goal of low-carbon preparation of the clinker, and improve the quality of the clinker It provides a new path for the low-carbon transformation of traditional high-carbon emission industries.
对于本案所公开的内容,还有以下几点需要说明:Regarding the content disclosed in this case, the following points need to be explained:
(1)、本案所公开的实施例附图只涉及到与本案所公开实施例所涉及到的结构,其他结构可参考通常设计;(1) The drawings of the embodiments disclosed in this case only relate to the structure involved in the embodiments disclosed in this case, other structures can refer to the general design;
(2)、在不冲突的情况下,本案所公开的实施例及实施例中的特征可以相互组合以得到新的实施例;(2) In the case of no conflict, the embodiments disclosed in this case and the features in the embodiments can be combined with each other to obtain new embodiments;
以上,仅为本案所公开的具体实施方式,但本公开的保护范围并不局限于此,本案所公开的保护范围应以权利要求的保护范围为准。The above are only the specific implementation methods disclosed in this case, but the protection scope of the present disclosure is not limited thereto, and the protection scope disclosed in this case should be based on the protection scope of the claims.
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20100319586A1 (en) * | 2009-06-19 | 2010-12-23 | Savannah River Nuclear Solutions, Llc | Carbon dioxide capture from a cement manufacturing process |
| CN104446058A (en) * | 2014-11-19 | 2015-03-25 | 济南大学 | Carbon dioxide mineralization preparation method of low-temperature calcined clinker and product thereof |
| CN111925141A (en) * | 2020-07-25 | 2020-11-13 | 大同冀东水泥有限责任公司 | Method for preparing cement clinker from high-magnesium high-soda limestone |
| CN113750774A (en) * | 2021-09-16 | 2021-12-07 | 天津中材工程研究中心有限公司 | Method and system for mineralizing and absorbing carbon dioxide by using bypass air bleeding and dust collecting ash of cement kiln |
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Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20100319586A1 (en) * | 2009-06-19 | 2010-12-23 | Savannah River Nuclear Solutions, Llc | Carbon dioxide capture from a cement manufacturing process |
| CN104446058A (en) * | 2014-11-19 | 2015-03-25 | 济南大学 | Carbon dioxide mineralization preparation method of low-temperature calcined clinker and product thereof |
| CN111925141A (en) * | 2020-07-25 | 2020-11-13 | 大同冀东水泥有限责任公司 | Method for preparing cement clinker from high-magnesium high-soda limestone |
| CN113750774A (en) * | 2021-09-16 | 2021-12-07 | 天津中材工程研究中心有限公司 | Method and system for mineralizing and absorbing carbon dioxide by using bypass air bleeding and dust collecting ash of cement kiln |
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